DE102023126509A1 - Method and arrangement for converting energy from an industrial process - Google Patents

Abstract

Arrangement for converting energy from a process gas stream originating from an industrial plant, comprising: a process gas cooling device, in particular a process gas condenser, with which at least a portion of the process gas stream can be condensed, wherein thermal energy can be extracted from the process gas stream; a working medium circuit for transporting at least a portion of the thermal energy extracted from the process gas stream, which thermal energy can be injected into a working medium; a heat engine arranged in the working medium circuit, with which at least a portion of the thermal energy injected into the working medium can be converted into mechanical energy.

Description

Technical area

The present invention relates to a method and an arrangement for converting energy from an industrial process, in particular for recovering and/or utilizing thermal energy in the form of a higher-value or more usable form of energy (e.g. mechanical and/or electrical energy).

State of the art

Process gas can be used as a medium in certain process steps for the manufacture of products in order to bring about certain technical effects, such as drying, in a process step. For the purposes of the present invention, a process gas is understood to be a gas or gas mixture which serves to have a technical effect on the product to be manufactured. Depending on the product and industrial process, the process gas can be an inert or non-inert gas or gas mixture. In particular, in the case of non-inert process gas, air or air-like gas mixtures are often used. In this case, the term process air is often used synonymously with process gas. In industrial processes, the process gas can absorb operating materials, for example solvents, or their reaction products, whereby the process gas is often released into the environment after leaving the industrial process. However, such operating materials can contain pollutants or solvents that have a negative impact on the environment. To reduce the negative environmental impact, enriched process gas (also known as exhaust gas) must be treated appropriately, also to comply with given legal limits for the exhaust gas released into the environment. If the process gas is process air, the exhaust gas is often synonymously referred to as exhaust air. A key distinguishing feature between exhaust gas and exhaust air can be the _O2 concentration in the underlying gas mixture. Pollutants or pollutant-containing solvents are particularly understood to be substances that, at a certain quantity or concentration in the gas outlet, can harm plants, animals and/or people in the surrounding area. The pollutants can be, for example, solvents (e.g. NMP, NEP, TEP, EAA, GBL, etc.), hydrocarbons, nitrogen oxides, ammonia, hydrogen fluoride, etc.

Conventional devices for treating process gas often contain a main flow channel through which a process gas stream is conducted. The main flow channel, particularly in the case of condensable pollutants in a process gas, is typically arranged between an outlet for discharging process gas to be purified from the industrial process and an inlet for introducing the same into a process gas condenser; in particular, it connects the outlet to the inlet. The pollutants or solvents contained in the process gas can be condensed in the process gas condenser, and the condensed pollutants or solvents can thus preferably be at least partially separated from the process gas.

In the prior art, processes with a condensation step are known in particular, whereby condensates are separated from the process gas and solvents can thereby be recovered

CA2214542A1 shows a process in which a solvent can be recovered during the production of lithium-ion batteries by condensing the solvent from solvent-containing process air.

When condensing process gas, it is advantageous to lower the temperature of the process gas. This primarily extracts heat energy from the process gas, although the heat energy extracted from the process gas is often dissipated into the environment.

Description of the invention

The present invention is based on the object of creating an improved arrangement for converting energy from an industrial plant/industrial process.

This object is achieved according to the invention with an arrangement for converting energy from a process gas stream originating from an industrial plant. The arrangement comprises the following: a process gas cooling device, in particular a process gas condenser, with which at least a portion of the process gas stream can be cooled or condensed, wherein thermal energy can be extracted from the process gas stream; a working fluid circuit for transporting at least a portion of the thermal energy extracted from the process gas stream, which can be injected into a working fluid; a heat engine arranged in the working fluid circuit, with which at least a portion of the thermal energy injected into the working fluid can be converted into mechanical energy.

The inventors have found that it can be advantageous to recover the heat energy used in the treatment of process gas recover or make it more usable. In particular, the thermal energy extracted from the process gas cooling device or the process gas condenser, in particular from a condensation step exposed to the process gas stream, can be used on the one hand to reheat the process gas and on the other hand for conversion in a heat engine. In a multi-stage process gas cooling device or process gas condenser with cooling devices arranged one behind the other, a respective coolant can be used for each cooling device in order to be able to cool the process gas to a different temperature in each cooling stage. In particular, for example, cooling water can be used in a second stage of the process gas cooling device or the process gas condenser and refrigerant cooled by a refrigeration machine can be used in a third stage, whereby thermal energy can be extracted from the process gas in each stage. According to the invention, the coolant can absorb heat, which is processed or recovered into a more usable form. The inventors therefore chose the inventive approach of extracting the thermal energy extracted from the process gas from the process gas stream and converting it into a more usable form of energy, such as mechanical and/or electrical energy, via a heat engine. This can be achieved, for example, by dual-using the working fluid to be expanded in the heat engine, for example, as a medium for directly cooling the process gas stream on the one hand, and within a working fluid evaporator, in which an indirect cooling capacity for the process gas stream can be provided on the other.

The process gas cooling device can preferably be designed as part of a heat-displacing device, wherein thermal energy is initially extracted from the process gas stream and at a later point in time, in particular after at least one use and/or treatment step following the aforementioned thermal energy extraction, is at least partially injected back into the process gas stream. The process gas stream is thereby cooled. In particular, the process gas cooling device can be part of a distillation device, wherein a heating device for heating the process gas is arranged upstream of the process gas cooling device.

For the purposes of this application, the process gas cooling device can also be a process gas condenser, provided that the process gas is cooled and condensed.

The process gas condenser can be designed, in particular, to condense the process gas. The process gas can thus be cooled in a condensation step using the process gas condenser, so that a condensate is formed and can be separated. The condensation step in the process gas condenser preferably comprises several cooling stages, each with a cooling device or cooling unit, wherein the process gas is cooled step by step to different temperature levels. A cooling device can, in particular, be a heat exchanger, for example a cross-flow heat exchanger. In a process gas condenser with several cooling stages, several cooling devices, i.e. several heat exchangers, can be arranged one behind the other, with each cooling device cooling the process gas to a predetermined temperature level. Particularly preferably, the process gas is cooled more significantly with each cooling stage. A cooling stage arranged further downstream therefore has a lower temperature level. It is also conceivable for the process gas to be condensed at each cooling stage. A cooling stage can therefore also be a condensation stage. A condensation step can therefore also comprise several condensation stages. In particular, for example, a front cooling stage can cool the process gas and a rear cooling stage can cool the process gas so that it also condenses.

The process gas cooling device, in particular the process gas condenser, can therefore have at least one heat exchanger, wherein the process gas stream, as a heat-emitting flow, is thermally connected to a heat-absorbing flow via heat conduction elements, for example metal lines or metal plates forming flow channels. The aforementioned working fluid or an intermediate medium can in particular be provided as the heat-absorbing flow, wherein the working fluid or the intermediate medium is assigned to a separate flow circuit. Thermal energy can be extracted from the process gas stream and coupled into a working fluid circuit. The thermal energy can therefore be transferred from the process gas stream to a working fluid circuit. The process gas cooling device or the process gas condenser is in particular assigned to the process gas stream and can simultaneously be assigned to a working fluid circuit or an intermediate fluid circuit. The transfer of thermal energy to the working fluid circuit can take place directly or indirectly. For example, the process gas cooling device or the process gas condenser can be flowed through by the process gas and the working fluid, whereby thermal energy within the process gas cooling device or the process gas condenser is transferred from the process gas to the working fluid. On the other hand, thermal energy within the process gas cooling device l device or the process gas condenser, the heat can also be transferred indirectly from the process gas to an intermediate medium, which is located or circulates in a preferably separate intermediate medium circuit, before the heat energy extracted from the process gas is transferred via the intermediate medium circuit to the working medium, for example in a working medium evaporator.

The intermediate medium is defined in the context of this disclosure as a carrier medium for thermal energy, which is intended in particular to transport thermal energy between the process gas stream and the working medium circuit. The intermediate medium can be an organic or inorganic medium, in particular a medium, and can be used in the gaseous or, particularly preferably, in the liquid state. The liquid state of the intermediate medium can in particular have better heat transfer and heat transport properties. The intermediate medium can therefore in particular be a fluid. In particular, the intermediate medium can be water or oil, in particular a thermal oil. The intermediate medium preferably circulates in the intermediate medium circuit. The intermediate medium circuit is preferably designed or constructed as a closed media circuit.

Within the process gas condenser, the process gas can be cooled and subsequently phase-transformed into a liquid condensate. In particular, a process gas mist can be formed during condensation of the process gas. A separation device for separating solvent-containing condensate can be arranged in the process gas condenser, through which the mist-like process gas is passed.

The working fluid circuit is designed to transport at least a portion of the thermal energy with the aid of the working fluid, for example, to the heat engine and convert it there, wherein the thermal energy is extracted from the process gas stream. The heat engine is in particular assigned to the working fluid circuit, wherein the working fluid is expanded in the heat engine and a portion of the thermal energy in the working fluid is converted into mechanical energy. The working fluid can in particular be an organic medium for performing work in the heat engine. The working fluid circuit can therefore comprise an ORC cycle (Organic Rankine Cycle). In particular, the working fluid circuit can be designed such that the energy required to operate the working fluid circuit, for example, to transport the working fluid, comes from the thermal energy converted in the heat engine. The working fluid circuit can therefore be designed such that it can supply itself with energy and is not dependent on an external energy source, such as a power grid.

In particular, an organic working fluid can be used, for example cyclohexane, butane, pentane, benzene, toluene, R134a, R12, R123, R113, n-perfluoropentane. The working fluid circuit can in particular refer to a thermodynamic cycle. The working fluid that circulates in the working fluid circuit of the arrangement can therefore be involved in or subject to a thermodynamic cycle. The working fluid can in particular be removed from the heat engine in a circulating circuit or circuit within the arrangement and finally fed back into the heat engine or supplied to the heat engine. The working fluid circuit can therefore in particular refer to a working fluid circulating in a circuit.

In the context of this disclosure, "A" and "an" are to be read as indefinite articles unless expressly stated otherwise, and thus always as "at least one" or "at least one". Directional terms such as "downstream" or "after" or "upstream" or "before" generally refer to the main flow direction of the respective fluid. The fluid circulating in a circuit can also be understood as a fluid located or flowing in a circuit. For the purposes of the invention, expressions such as "coupleable", "decoupleable", "convertible" in connection with material and/or energy flows can alternatively or additionally, in particular optionally, include expressions such as "can be or is coupled in", "can be or is decoupled", "can or is converted". The coupling of heat/thermal energy can therefore be understood in particular as transferring it, i.e., "coupleable" can be understood in particular as "transferable to the corresponding medium" or "is coupled in." This can therefore also preferably be understood in the sense of "transferred to the corresponding medium."

The heat engine can, in particular, be a turbine, preferably of a radial or axial design. However, the heat engine can also be designed as a piston engine or as a scroll or so-called screw expander. In particular, the arrangement can also comprise a generator coupled to the heat engine for generating electrical energy. Thus, by means of the generator, at least a portion of the thermal energy converted into mechanical energy can be converted into electrical energy.

A preferred embodiment of the invention further comprises a working medium condenser arranged in the working medium circuit downstream of the heat engine, by means of which the working medium can be condensed, wherein heat energy can be extracted from the working medium.

After expansion in the heat engine, the working fluid can be fed to a working fluid condenser, in which the essentially still gaseous working fluid can be condensed. Thermal energy can be extracted during the condensation process in the working fluid condenser, for example, to be fed into the process gas stream and/or into an intermediate circuit. The working fluid condenser can therefore be designed in the form of a heat exchanger or cooler, whereby the thermal energy can also be extracted into an environment, where the thermal energy is dissipated. Extracting thermal energy from the working fluid can be particularly advantageous for reducing waste heat from the system by recovering the extracted thermal energy. By extracting thermal energy into the environment, a particularly simple, compact, and economical design can be realized, for example in the form of an air cooler. An air cooler can, for example, be a heat exchanger operated by a fan, whereby a conveyed air stream is used to dissipate thermal energy into the environment.

In an advantageous embodiment, the thermal energy to be extracted from the working medium can be at least partially coupled into the process gas flow, in particular at a point downstream of the process gas cooling device or the process gas condenser.

In a further preferred embodiment of the invention, a process gas heating device for heating at least a portion of the process gas stream is arranged downstream of the process gas cooling device or the process gas condenser, by means of which process gas heating device thermal energy can be coupled into the process gas stream.

The inventors have further determined that the amount of thermal energy extracted during the condensation of the process gas can be higher than the thermal energy returned to the process gas by means of the process gas heating device, which can result in waste heat. In particular, the temperature of the process gas upon entering the process gas cooling device or the process gas condenser can be higher than the temperature of the process gas upon exiting the process gas heating device. The temperature gradient, i.e. the resulting heat flow of the waste heat, can be comparatively small. Instead of simply dissipating the waste heat into the environment, the waste heat can advantageously be used not only to partially convert it in the heat engine as described above, but also via a process gas heating device to heat at least a portion of the process gas stream downstream of the process gas cooling device or the process gas condenser. The process gas heating device can therefore be used to feed the thermal energy not used for conversion back into the process gas stream.

The return of thermal energy to the process gas stream can generally be understood as a thermal shift. In this case, at least a portion of the thermal energy present in the process gas stream is shifted from one location to another location in the process gas stream. The process gas heating device can thus couple thermal energy into the process gas stream, with the coupling of thermal energy into the process gas stream representing a thermal shift of thermal energy that was previously extracted from the process gas stream.

The process gas heating device can, for example, be designed in the form of a heat exchanger, wherein thermal energy can be coupled into the process gas stream by means of a heat-carrying flow, for example the working fluid located in the working fluid circuit or an intermediate fluid located in an intermediate fluid circuit. The process gas heating device can, for example, be designed as a gas-to-gas heat exchanger or as a gas-to-liquid heat exchanger. The transfer of thermal energy between the working fluid circuit and the process gas stream can therefore take place directly between two adjacent flows in a heat-conducting device such as a heat exchanger. In particular, the thermal energy to be extracted from the working fluid can be at least partially coupled into the process gas stream via the process gas heating device.

The transfer of thermal energy between the working fluid circuit and the process gas flow can also be carried out indirectly via an intermediate circuit, whereby the thermal energy to be transferred to the process gas flow initially takes place by means of a heat exchanger between the working fluid circuit and the intermediate circuit and then takes place in process terms between the intermediate circuit and the process gas flow by means of a further heat exchanger, for example by means of the process gas heating device.

In a further preferred embodiment of the invention, the working fluid circuit comprises the following: a first working fluid line to the heat engine, by means of which the working fluid can be fed to an inlet of the heat engine; a second working fluid line, by means of which the working fluid can be discharged from an outlet of the heat engine; a third working fluid line, by means of which the working fluid can be fed to a working fluid inlet of a working fluid heating device, in particular for evaporating the working fluid.

In particular, the first working fluid line can be used to supply the working fluid from a working fluid outlet of the process gas cooling device or the process gas condenser to the inlet of the heat engine. Furthermore, the second working fluid line can be used to supply the working fluid from an outlet of the heat engine to a working fluid inlet of the process gas heating device. The third working fluid line can be used to supply the working fluid to the process gas cooling device or the process gas condenser as a working fluid heating device for absorbing thermal energy from the process gas stream.

The first working fluid line is particularly intended to transport vaporized working fluid to the heat engine. The second working fluid line is particularly intended to discharge the working fluid, which was previously expanded in the heat engine, from the heat engine. Particularly preferably, the second working fluid line is also intended to conduct working fluid, in particular to a working fluid condenser. The third working fluid line is particularly intended to conduct working fluid to a working fluid heating device, in which the working fluid can absorb thermal energy, in particular for evaporating the working fluid.

With the help of the process gas cooling device or the process gas condenser, thermal energy can be transferred from the process gas stream to the working fluid circuit as a heat-absorbing flow, whereby the working fluid is evaporated. The working fluid is therefore preferably evaporated directly in the process gas cooling device or in the process gas condenser. The first working fluid line is preferably designed to conduct a gaseous or vaporous working fluid from the process gas cooling device or the process gas condenser to the inlet of the heat engine. After expansion in the heat engine, the second working fluid line can conduct the working fluid to a working fluid inlet of the process gas heating device. In the process gas heating device, thermal energy can be transferred from the working fluid to the process gas stream, whereby the working fluid can be condensed. The working fluid is therefore preferably condensed directly in the process gas heating device. The third working fluid line is designed to conduct condensed working fluid from the process gas heating device to the process gas cooling device or to the process gas condenser.

A further preferred embodiment of the invention further comprises a working medium evaporator for evaporating working medium, wherein thermal energy can be transferred from an intermediate medium to the working medium by means of the working medium evaporator; at least one intermediate medium circuit comprising: a first intermediate medium line to the working medium evaporator, by means of which first intermediate medium line an intermediate medium can be fed to an intermediate medium inlet of the working medium evaporator for supplying intermediate medium, wherein the thermal energy extracted from the process gas stream can be transported to the working medium evaporator by means of the intermediate medium, and/or a second intermediate medium line to the process gas heating device, by means of which second intermediate medium line an intermediate medium can be fed to an intermediate medium inlet of the process gas heating device for supplying intermediate medium, wherein at least part of the thermal energy from the intermediate medium can be transferred to the process gas stream via the process gas heating device.

The first intermediate medium line can in particular be able to supply an intermediate medium from an intermediate medium outlet of the process gas cooling device or of the process gas condenser for discharging intermediate medium to an intermediate medium inlet of the working medium evaporator for supplying intermediate medium, wherein the thermal energy extracted from the process gas flow can be transported to the working medium evaporator with the aid of the intermediate medium.

Particularly suitable intermediaries are heat-conducting liquids, which can be either organic or inorganic. The intermediary preferably has a high heat capacity and/or a high critical temperature. Water or oil can be used as intermediaries, in particular.

The working medium evaporator is particularly assigned to both the working medium circuit and the intermediate medium circuit, and is therefore preferably flowed through by the intermediate medium on the one hand and the working medium on the other hand, whereby heat energy, which has been extracted from the process gas flow, is transferred from the intermediate medium to the working medium. By means of the first The intermediate medium can be fed from the process gas cooling device or the process gas condenser into the working medium evaporator via an intermediate medium line. The working medium can therefore be heated and converted into a gaseous state, i.e. evaporated, when thermal energy is supplied within the working medium evaporator. The intermediate medium circuit can also have a second intermediate medium line that feeds the intermediate medium to the process gas heating device. In particular, the second intermediate medium line can feed the intermediate medium from the working medium evaporator, in which part of the thermal energy was transferred to the working medium, to the process gas heating device. In the process gas heating device, a further part of the thermal energy contained in the intermediate medium can be transferred to the process gas stream.

Optionally, the intermediate medium circuit can have a working medium condenser, which can be arranged downstream of the working medium evaporator with respect to the main flow direction of the intermediate medium, whereby the working medium condenser can also be assigned to the working medium circuit and is flowed through by both the intermediate medium and the working medium. The working medium condenser is preferably arranged downstream of the heat engine with respect to the working medium circuit. After expansion in the heat engine, the still gaseous working medium can be condensed in the working medium condenser, whereby heat energy is transferred to the intermediate medium. Alternatively, the second intermediate medium line can carry the intermediate medium from a working medium condenser, in which heat energy has been transferred from the working medium to the intermediate medium, to the process gas heating device. In the process gas heating device, the heat energy transferred to the intermediate medium can be transferred to the process gas stream accordingly. In particular, heat transfer can take place indirectly via the intermediate medium from the process gas cooling device or the process gas condenser to the process gas heating device. Thermal energy can therefore be indirectly coupled from the process gas stream via the intermediate medium back into the process gas stream by means of the process gas heating device.

In particular, an intermediate medium cooler can be arranged in the intermediate medium circuit upstream of the working medium condenser, in which the intermediate medium is cooled before the intermediate medium is fed into the working medium condenser to absorb heat energy. The intermediate medium can therefore first be cooled by means of the intermediate medium cooler before the intermediate medium is heated in the working medium condenser. The intermediary medium cooler can therefore limit the amount of heat energy that the intermediate medium couples into the process gas stream via the process gas heating device. Without the intermediate medium cooler, more heat energy can be coupled into the process gas stream overall, which should be avoided under certain circumstances, for example to maintain a predetermined maximum temperature of the process gas stream as it flows through the process gas heating device.

The arrangement can in particular have two intermediate medium circuits, wherein in a first intermediate medium circuit, a first intermediate medium is guided from the process gas cooling device or the process gas condenser via the first intermediate medium line to the working medium evaporator. The first intermediate medium can then be guided back in the circuit to the process gas cooling device or to the process gas condenser. In a second intermediate medium circuit, a second intermediate medium, which flows through the process gas heating device, can be guided from the process gas heating device. The second intermediate medium can then be guided to the working medium condenser. The second intermediate medium can be guided to an inlet of the process gas heating device via the second intermediate medium line.

In a further preferred embodiment of the invention, the process gas cooling device, in particular the process gas condenser, has at least two cooling devices arranged one behind the other for cooling at least a portion of the process gas flow, each of which is intended for a cooling stage. A front cooling device is intended to transfer at least a portion of the thermal energy from the process gas flow to the working fluid for expansion in the heat engine and, in the process, to cool at least a portion of the process gas flow; a rear cooling device arranged downstream of the front cooling device is intended to transfer at least a portion of the thermal energy from the process gas flow to a coolant flow and, in the process, to cool, in particular, to condense, at least a portion of the process gas flow. The coolant flow is further intended to absorb thermal energy at a point in an intermediate circuit and/or in the working fluid circuit. For example, this occurs at a point in the working fluid circuit downstream of the heat engine, with thermal energy being absorbed from the working fluid. The coolant flow can therefore generally be intended to absorb additional thermal energy than that from the process gas. It can therefore also be used to cool the intermediate or working medium after the process gas has cooled down.

The process gas cooling device or process gas condenser can, in particular, have three cooling devices arranged one behind the other. As described above, the respective cooling device can cool the process gas stream to a predetermined temperature level, wherein the process gas stream is cooled successively. The temperature level preferably refers, in particular, to an average, lowest temperature of the process gas reached within the cooling stage. A respective coolant can flow through a cooling device for cooling the process gas stream. The temperature level of the process gas thus drops further with each cooling device arranged downstream. Analogously, the temperature level of the process gas can also decrease with each cooling stage arranged downstream.

Particularly preferably, the front cooling device can be the first of the cooling devices arranged one behind the other within the process gas cooling device or the process gas condenser in the downstream direction of the process gas flow. The directions refer to the main flow direction of the process gas. The process gas can therefore preferably flow first through the first cooling device within the process gas cooling device or the process gas condenser, then through the second and finally through the third cooling device. Thus, with respect to the main flow direction of the process gas, the first cooling device can in particular be the front cooling device. A rear cooling device can accordingly be the second or third cooling device. The flow direction can generally mean the main flow direction.

The cooling devices are each particularly intended for a cooling stage. Thus, the first cooling device can particularly preferably be intended for a first cooling stage, the second cooling device for a second cooling stage, and the third cooling device for a third cooling stage, etc.

A coolant flow can therefore be an intermediate medium, a cooling water flow, or even a refrigerant flow, whereby the refrigerant flow is cooled using a coupled refrigeration machine. For example, the first cooling device can be a cooling device cooled by an intermediate medium, the second cooling device can be a water-cooled cooling device, and the third cooling device can be a cooling device cooled by refrigerant. With regard to the flow direction of the coolant flow, the respective coolant can absorb further thermal energy from an intermediate medium circuit and/or from the working medium circuit after flowing through a cooling device. The coolant flow can therefore be advantageously used to absorb additional thermal energy.

In an arrangement variant in which two intermediate medium circuits are used, the intermediate medium located in the second intermediate medium circuit can preferably be cooled with the aid of the coolant flow, with heat energy being absorbed by the coolant flow. In this arrangement variant, the second intermediate medium circuit can be intended to transport heat energy from the working medium circuit to the process gas heating device. For example, a cooling water flow can absorb heat energy from the second intermediate medium circuit after the cooling water flow has absorbed heat energy from the process gas flow. The absorption of heat energy from the second intermediate medium circuit can occur, for example, with the aid of a heat exchanger assigned to the second intermediate medium circuit. Analogously, in a further example, a refrigerant flow cooled by a refrigeration machine can absorb heat energy from the second intermediate medium circuit. This can also occur, for example, with the aid of a heat exchanger assigned to the second intermediate medium circuit.

An intermediate medium pump for circulating intermediate medium can be arranged in each intermediate medium circuit. The respective intermediate medium pump can be operated with at least a portion of the electrical energy generated by a generator coupled to the heat engine.

Particularly preferably, the coolant flow, i.e., optionally a cooling water flow or a refrigerant flow, can absorb thermal energy from the working fluid circuit in an analogous embodiment, whereby the working fluid can preferably condense during the heat release. The coolant flow will therefore preferably absorb thermal energy from the working fluid circuit downstream of the heat engine. The coolant flow can thus support the condensation of the working fluid in the working fluid circuit downstream of the heat engine. The coolant flow can also be used as a heat-absorbing flow within the working fluid condenser.

In a further preferred embodiment of the invention, the arrangement comprises a refrigeration machine for cooling the coolant flow, wherein at least a part of the thermal energy, in particular that which is coupled from the coolant flow into the refrigeration machine, can be coupled out of the refrigeration machine for coupling into the process gas flow and/or into an intermediate circuit and/or into the working medium circuit.

The coolant can in particular be a refrigerant which is cooled in a refrigeration machine. Thermal energy can be transferred into the refrigeration machine. machine and fed into the process gas stream. Thermal energy from the refrigeration machine can also be fed into an intermediate medium circuit, thereby heating the intermediate medium. The intermediate medium circuit can be designed to transport thermal energy from the process gas stream into the working medium circuit. The coupling into the intermediate medium circuit can preferably be arranged upstream of the process gas cooling device or the process gas condenser with regard to the flow direction of the intermediate medium. The intermediate medium can therefore be preheated before it is fed to the process gas cooling device or the process gas condenser. Overall, it is conceivable to advantageously couple the thermal energy coupled out into the refrigeration machine into any desired material stream. This can be, for example, at a point in the working medium circuit upstream of the heat engine.

It is also conceivable and preferred that the thermal energy that can be coupled into the process gas flow and/or into an intermediate circuit and/or into the working fluid circuit can simply be extracted from the refrigeration machine as waste heat. Thus, it is also possible for the sources of thermal energy from the refrigeration machine to originate from both a compressor and the coolant flow. The coolant flow can, in particular, be a refrigerant flow.

In a further preferred embodiment of the invention, the arrangement comprises a generator coupled to the heat engine for generating electrical energy. In particular, the electrical energy generated by the generator can be used to operate an electromechanical converter, for example, to operate a working fluid pump. In particular, the current generated by the generator can be fed as direct current to an inverter of the working fluid pump. The working fluid pump can also be a feed pump, wherein the working fluid pump can transport the working fluid in a working fluid circuit. In particular, the working fluid pump can circulate the working fluid in the working fluid circuit.

In a further preferred embodiment of the invention, the process gas cooling device, in particular the process gas condenser, comprises the following: three cooling devices arranged one behind the other for cooling at least a portion of the process gas flow, wherein the first cooling device can be flowed through by an intermediate medium located in an intermediate medium circuit, wherein the thermal energy originating from at least a portion of the process gas flow can be transferred to the intermediate medium for re-coupling into the process gas flow, the second cooling device can be flowed through by a first coolant, in particular cooling water, wherein thermal energy can be transferred from the process gas flow to the first coolant, the third cooling device can be flowed through by a second cooled coolant, in particular a refrigerant which is cooled by means of a refrigeration machine, wherein thermal energy can be transferred from the process gas flow to the second coolant, in which arrangement the intermediate medium located in an intermediate medium circuit can be flowed through a working medium evaporator for evaporating the working medium, wherein at least a portion of the thermal energy contained in the working medium can be converted into electrical energy via the heat engine and the generator a process gas heating device arranged downstream of the process gas cooling device or the process gas condenser can be flowed through by the intermediate medium located in an intermediate medium circuit, wherein thermal energy can be coupled into the process gas flow.

The present invention further relates to a method for converting energy from an industrial process.

The object of the invention is achieved alternatively or additionally by a method for converting energy from a process gas stream originating from an industrial process, in which method at least a portion of the process gas stream is exposed to or subjected to a condensation step, wherein at least a portion of the thermal energy from the process gas stream is transferred to a working medium for conversion in a heat engine which is arranged in a working medium circuit.

During the conversion process in the heat engine, the working fluid is preferably expanded, allowing mechanical energy to be extracted for further conversion into electrical energy. The industrial process takes place primarily in the industrial plant.

In a further preferred embodiment of the invention, the working fluid is condensed downstream of the conversion in the heat engine, whereby heat energy is extracted from the working fluid.

The heat engine is particularly associated with a working fluid circuit, for example an ORC circuit. After conversion in the heat engine, the predominantly still gaseous working fluid can preferably be condensed. In particular, the condensation of the working fluid downstream of the heat engine can be part of a working fluid cycle process or a ORC cycle. Thermal energy can be released into the environment, for example, using an air cooler. Preferably, the thermal energy released from the working fluid can also be injected into the process gas stream. For this purpose, the thermal energy can first be injected into an intermediate circuit before being injected into the process gas stream. Optionally, the thermal energy can also be injected into a coolant stream, particularly a cooling water stream or a refrigerant stream.

In a further preferred embodiment of the invention, thermal energy from the working medium is transferred to the process gas during a heating process of the process gas stream.

With the help of the heating process, in particular, a heat shift can take place in the process gas stream, whereby at least part of the heat energy extracted from the process gas stream is transferred back into the process gas stream.

In a further preferred embodiment of the invention, the method comprises at least one intermediate medium circuit which can be coupled to the process gas stream and/or to the working medium circuit in a heat-conducting or heat-transferring manner, in which the following method steps are carried out: during the condensation step of the process gas stream, thermal energy is transferred directly to an intermediate medium located in the intermediate medium circuit, flowing or circulating; at least part of the thermal energy transferred from the process gas to the intermediate medium is transferred directly to the working medium located in the working medium circuit upstream of the conversion in the heat engine, whereby the working medium is evaporated; the evaporated working medium is fed to the heat engine.

Furthermore, downstream of the heat engine, thermal energy can be transferred from the working medium directly to the intermediate medium located in an intermediate medium circuit; during the heating process of the process gas stream, the process gas in the process gas stream is directly heated by means of thermal energy from the intermediate medium located in an intermediate medium circuit.

During the condensation step of the process gas stream, the thermal energy is preferably transferred directly or immediately from the process gas stream to the intermediate medium. This can particularly refer to intermediate medium flowing adjacent to the process gas stream and located in the intermediate medium circuit. Similarly, the direct transfer of thermal energy between the intermediate medium and the working medium upstream of the conversion in the heat engine can be understood. In the context of this invention, direct transfer can therefore be understood as a transfer of thermal energy between two fluids arranged adjacent to one another or flowing through one another, for example in a heat exchanger. Similarly, the process gas is heated by directly transferring thermal energy from the intermediate medium to the adjacent process gas flowing through. During the conversion in the heat engine, this can particularly mean an expansion of the working medium, whereby thermal energy is converted into mechanical energy. In particular, the condensation step can comprise several cooling stages. In particular, during the condensation step in the first cooling stage, the thermal energy can be transferred to the intermediate medium when cooling the process gas stream, whereby the process gas stream is only condensed in the second and/or third cooling stage.

In a preferred intermediate circuit arrangement, the thermal energy extracted from the process gas stream can therefore have the following transfer paths: first, directly from the process gas stream to the intermediate circuit. Second, directly from the intermediate circuit to the working fluid circuit for conversion in the heat engine. Third, after conversion, from the working fluid circuit directly to the intermediate circuit. Fourth, from the intermediate circuit to the process gas stream. Advantageously, in this embodiment, an intermediate circuit can be used to realize both the heat transfer in the process gas stream and the conversion of excess thermal energy in the heat engine, with the excess thermal energy arising primarily from the different temperature levels during the condensation of the process gas and during the heating process of the process gas.

In a likewise preferred embodiment with two intermediate circuits, i.e. with a first and a second intermediate circuit, the thermal energy can have the following transfer paths: first, directly from the process gas flow to the first intermediate circuit. Second, from the first intermediate circuit directly to the working fluid circuit. Third, from the working fluid circuit to the second intermediate circuit. Fourth, from the second intermediate circuit to the process gas flow. A separate intermediate medium can be used in each intermediate circuit. For example, two different organic intermediate media can be used in each intermediate circuit. Advantageously, due to the different temperature levels of the first and second intermediate circuit, a temperature-optimized Intermediates may be used. For example, the first intermediary may have a higher critical temperature than the second intermediary.

In a further preferred embodiment of the invention, the following method steps are carried out: during the condensation step of the process gas stream, thermal energy is transferred directly to a working medium, whereby the working medium is evaporated; the evaporated working medium is fed to the heat engine; during the heating process of the process gas stream, thermal energy is transferred directly to the process gas, whereby the working medium is condensed in the working medium circuit downstream of the heat engine as heat is released to the process gas. The condensation step can comprise at least one cooling stage, preferably several cooling stages. In particular, thermal energy can be transferred directly to a working medium in a preferably first cooling stage of the condensation step.

In this preferred embodiment, the process gas stream is directly coupled to the working fluid circuit in a heat-conducting manner, allowing the transfer of thermal energy without any intermediate means. The condensation step of the process gas stream can thus simultaneously be an evaporation step of the working fluid circuit. The heating process of the process gas stream can simultaneously be a condensation step of the working fluid circuit. Advantageously, such an embodiment can potentially be implemented more compactly and less cost-intensively, since the functions of a working fluid evaporator and a working fluid condenser are already realized during the condensation step or heating process of the process gas stream.

In a further preferred embodiment of the invention, the condensation step of the process gas stream comprises at least two cooling stages taking place one after the other, in which method the following method steps are carried out: Thermal energy from the process gas stream is transferred to a working medium in a front, i.e. upstream arranged or provided, cooling stage; In a rear cooling stage arranged downstream of the front cooling stage, thermal energy from the process gas stream is transferred to a coolant located in a coolant stream; Thermal energy from the working medium is transferred to the coolant located in a coolant stream at a point in the working medium circuit downstream of the conversion in the heat engine.

The process gas flow can therefore be cooled successively by means of at least two cooling stages, each cooling stage having its own, in particular predetermined, temperature level, which decreases in the order according to the main flow direction.

The transfer of thermal energy from the process gas stream to a working medium can occur both directly and indirectly with the aid of an intermediate medium. In an arrangement with three or more cooling stages, the front cooling stage can be designed as the first cooling stage. The position "front" refers to the main flow direction of the process gas stream. A coolant can be water or refrigerant, for example, with the refrigerant being cooled in a refrigeration machine. In an arrangement with three cooling stages, thermal energy can be transferred to a cooling water stream in the second cooling stage and thermal energy can be transferred to a refrigerant stream in the third cooling stage.

Thermal energy from the working fluid can be transferred to both a cooling water flow and a refrigerant flow, particularly at a point in the working fluid circuit downstream of the conversion in the heat engine. In particular, this transfer of thermal energy from the working fluid to the cooling water flow or refrigerant flow can occur after the cooling water flow or refrigerant flow has absorbed thermal energy from the process gas flow. Advantageously, the coolant flow—generally speaking, the cooling water or refrigerant flow—can absorb further thermal energy, thus better utilizing the heat absorption capacity of the coolant flow.

In a further preferred embodiment of the invention, the following method steps are carried out: a coolant is cooled in a coolant stream using a refrigeration machine, wherein thermal energy is extracted from the coolant into the refrigeration machine; the coolant is guided to the rear cooling stage of the process gas stream; downstream of the rear cooling stage of the process gas stream, thermal energy from the working fluid is absorbed by the coolant in the coolant stream, wherein the working fluid in the working fluid circuit is cooled and condensed, and/or in the working fluid circuit, the thermal energy previously extracted into the refrigeration machine is transferred to an intermediate medium or to the working fluid for coupling into the process gas stream and/or for coupling into the working fluid circuit. Thus, the intermediate medium and/or the working fluid can preferably be preheated using the thermal energy previously extracted into the refrigeration machine, i.e., waste heat from the refrigeration machine. This can bring about a temperature increase in the working fluid and/or the intermediate medium. The work equipment can circulate in particular in the work equipment circuit.

In a further aspect of the invention, the arrangement or the method is used for converting energy from a process gas stream, in particular from a circulating or recirculating air of a dryer for treating process gas of a dryer, in particular from the process gas of a production plant for producing electrodes of a battery and/or a device for separating or recovering at least one solvent from the process gas of a production plant.

Examples of implementation

The invention is explained in more detail below using several exemplary embodiments, without distinguishing between the different claim categories. Furthermore, it is clarified that the proposed solutions according to the invention can be applied to various different industrial processes. An energy conversion device coupled to an electrode coating system is presented below as an example.

List of characters

• 1 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit direkter Kopplung mit einem Arbeitsmittelkreis;
• 1a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 1;
• 2 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit direkter Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms im Arbeitsmittelkreis;
• 2a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 2;
• 3 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit direkter Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms im Arbeitsmittelkreis;
• 3a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 3;
• 4 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit direkter Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 4a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 4;
• 5 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit direkter Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 5a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 5;
• 6 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis;
• 6a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 6;
• 7 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms im Zwischenmittelkreis;
• 7a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 7;
• 8 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms sowie mit Nutzung der Abwärme der Kältemaschine im Zwischenmittelkreis;
• 8a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 8;
• 9 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms im Zwischenmittelkreis;
• 9a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 9;
• 10 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms sowie mit Nutzung der Abwärme der Kältemaschine im Zwischenmittelkreis;
• 10a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 10;
• 11 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 11a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 11;
• 12 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms im Arbeitsmittelkreis;
• 12a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 12;
• 13 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms im Arbeitsmittelkreis;
• 13a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 13;
• 14 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 14a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 14;
• 15 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 15a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 15;
• 16 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms zum Kondensieren eines Arbeitsmittels;
• 16a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 16;
• 17 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kältemittelstroms zum Kondensieren eines Arbeitsmittels sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 17a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 17;
• 18 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms zum Kondensieren eines Arbeitsmittels;
• 18a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 18;
• 19 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur Kopplung mit einem Arbeitsmittelkreis und mit Nutzung des Kühlwasserstroms zum Kondensieren eines Arbeitsmittels sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 19a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 19;
• 20 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur direkten Verdampfung und Kondensation des Arbeitsmittels;
• 20a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 20;
• 21 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur direkten Verdampfung und Kondensation des Arbeitsmittels sowie mit Nutzung der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 21a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 21;
• 22 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur direkten Verdampfung und Vorkühlung des Arbeitsmittels sowie mit Nutzung des Kältemittelstroms im Arbeitsmittelkreis;
• 22a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 22;
• 23 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur direkten Verdampfung und Vorkühlung des Arbeitsmittels sowie mit Nutzung des Kältemittelstroms und der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 23a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 23;
• 24 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur direkten Verdampfung und Vorkühlung des Arbeitsmittels sowie mit Nutzung des Kühlwasserstroms im Arbeitsmittelkreis;
• 24a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 24;
• 25 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit einem Zwischenmittelkreis zur direkten Verdampfung und Vorkühlung des Arbeitsmittels sowie mit Nutzung des Kühlwasserstroms und der Abwärme der Kältemaschine im Arbeitsmittelkreis;
• 25a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 25;
• 26 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit zwei Zwischenmittelkreisen zur direkten Verdampfung und Kondensation des Arbeitsmittels;
• 26a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 26;
• 27 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit zwei Zwischenmittelkreisen zur direkten Verdampfung und Kondensation des Arbeitsmittels sowie mit Nutzung des Kältemittelstroms in einem Zwischenmittelkreis;
• 27a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 27;
• 28 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit zwei Zwischenmittelkreisen zur direkten Verdampfung und Kondensation des Arbeitsmittels sowie mit Nutzung des Kältemittelstroms in einem Zwischenmittelkreis und der Abwärme der Kältemaschine in einem anderen Zwischenmittelkreis;
• 28a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 28;
• 29 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit zwei Zwischenmittelkreisen zur direkten Verdampfung und Kondensation des Arbeitsmittels sowie mit Nutzung des Kühlwasserstroms in einem Zwischenmittelkreis;
• 29a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 29;
• 30 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit zwei Zwischenmittelkreisen zur direkten Verdampfung und Kondensation des Arbeitsmittels sowie mit Nutzung des Kühlwasserstroms in einem Zwischenmittelkreis und der Abwärme der Kältemaschine in einem anderen Zwischenmittelkreis;
• 30a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 30;
• 31 eine schematische Darstellung einer erfindungsgemäßen Anordnung zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage mit zwei Zwischenmittelkreisen zur direkten Verdampfung und Kondensation des Arbeitsmittels sowie mit Nutzung der Abwärme der Kältemaschine in einem Zwischenmittelkreis;
• 31a eine schematische Darstellung eines erfindungsgemäßen Verfahrens, vorzugsweise zur Ausführung in einer Anordnung nach 31.

The drawings show:

• 1 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with direct coupling to a working medium circuit;
• 1a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 1 ;
• 2 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with direct coupling to a working medium circuit and with use of the refrigerant flow in the working medium circuit;
• 2a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 2 ;
• 3 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with direct coupling to a working fluid circuit and with use of the cooling water flow in the working fluid circuit;
• 3a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 3 ;
• 4 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with direct coupling to a working fluid circuit and with use of the refrigerant flow and with use of the waste heat of the refrigeration machine in the working fluid circuit;
• 4a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 4 ;
• 5 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with direct coupling to a working fluid circuit and with use of the cooling water flow and with use of the waste heat of the refrigeration machine in the working fluid circuit;
• 5a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 5 ;
• 6 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit;
• 6a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 6 ;
• 7 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the cooling water flow in the intermediate circuit;
• 7a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 7 ;
• 8 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the cooling water flow and with use of the waste heat of the refrigeration machine in the intermediate circuit;
• 8a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 8 ;
• 9 a schematic representation of an arrangement according to the invention for converting generation of energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the refrigerant flow in the intermediate circuit;
• 9a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 9 ;
• 10 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the refrigerant flow and with use of the waste heat of the refrigeration machine in the intermediate circuit;
• 10a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 10 ;
• 11 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the waste heat of the refrigeration machine in the working medium circuit;
• 11a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 11 ;
• 12 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the refrigerant flow in the working medium circuit;
• 12a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 12 ;
• 13 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the cooling water flow in the working medium circuit;
• 13a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 13 ;
• 14 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the cooling water flow and with use of the waste heat of the refrigeration machine in the working medium circuit;
• 14a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 14 ;
• 15 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the refrigerant flow and with use of the waste heat of the refrigeration machine in the working medium circuit;
• 15a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 15 ;
• 16 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the refrigerant flow for condensing a working medium;
• 16a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 16 ;
• 17 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the refrigerant flow for condensing a working medium and with use of the waste heat of the refrigeration machine in the working medium circuit;
• 17a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 17 ;
• 18 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the cooling water flow for condensing a working medium;
• 18a a schematic representation of a method according to the invention, preferably for execution in an arrangement according to 18 ;
• 19 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for coupling to a working medium circuit and with use of the cooling water flow for condensing a working medium and with use of the waste heat of the refrigeration machine in the working medium circuit;
• 19a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 19 ;
• 20 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for direct evaporation and condensation of the working medium;
• 20a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 20 ;
• 21 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for direct evaporation and condensation of the working medium and with use of the waste heat of the refrigeration machine in the working medium circuit;
• 21a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 21 ;
• 22 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for direct evaporation and pre-cooling of the working medium and with use of the refrigerant flow in the working medium circuit;
• 22a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 22 ;
• 23 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for direct evaporation and pre-cooling of the working medium and with use of the refrigerant flow and the waste heat of the refrigeration machine in the working medium circuit;
• 23a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 23 ;
• 24 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for direct evaporation and pre-cooling of the working medium and with use of the cooling water flow in the working medium circuit;
• 24a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 24 ;
• 25 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with an intermediate circuit for direct evaporation and pre-cooling of the working medium and with use of the cooling water flow and the waste heat of the refrigeration machine in the working medium circuit;
• 25a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 25 ;
• 26 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with two intermediate circuits for direct evaporation and condensation of the working medium;
• 26a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 26 ;
• 27 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with two intermediate circuits for direct evaporation and condensation of the working medium and with use of the refrigerant flow in one intermediate circuit;
• 27a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 27 ;
• 28 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with two intermediate circuits for direct evaporation and condensation of the working medium and with use of the refrigerant flow in an intermediate circuit and the Waste heat from the refrigeration machine in another intermediate circuit;
• 28a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 28 ;
• 29 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with two intermediate circuits for direct evaporation and condensation of the working medium and with use of the cooling water flow in one intermediate circuit;
• 29a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 29 ;
• 30 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with two intermediate circuits for direct evaporation and condensation of the working fluid and with use of the cooling water flow in one intermediate circuit and the waste heat of the refrigeration machine in another intermediate circuit;
• 30a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 30 ;
• 31 a schematic representation of an arrangement according to the invention for converting energy from an electrode coating system with two intermediate circuits for direct evaporation and condensation of the working medium and with use of the waste heat of the refrigeration machine in one intermediate circuit;
• 31a a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 31 .

Preferred embodiment of the invention

Show at a glance 1 to 5a schematic representations of arrangements and methods according to the invention of a variant 1 with a direct heat coupling of the process gas stream A with a working medium circuit C.

6 to 11a show schematic representations of a variant 2 with an intermediate circuit B for the heat-conducting coupling of the process gas flow A with the working fluid circuit C. In addition, in the representations of the main variant 2, an air heat exchanger 8 is arranged in the working fluid circuit C.

12 to 19a show schematic representations of a variant 3 with the intermediate circuit B and a coolant heat exchanger 63, which is arranged for condensing the working fluid in the working fluid circuit C.

20 to 25a show schematic representations of a variant 4 with the intermediate circuit B, which has a heat coupling with the working fluid circuit C for direct evaporation and for condensing or cooling the working fluid.

26 to 31a show schematic representations of a variant 5 with two intermediate circuits Ba and Bb for heat coupling of the process gas flow A with the working medium circuit C.

• 1 zeigt schematisch ein Ausführungsbeispiel einer erfindungsgemäßen Anordnung 100 zur Umwandlung von Energie aus einer Elektrodenbeschichtungsanlage 1 mit direkter Kopplung mit einem Arbeitsmittelkreis C.

Now the characters are described in detail:

• 1 shows schematically an embodiment of an arrangement 100 according to the invention for converting energy from an electrode coating system 1 with direct coupling to a working medium circuit C.

Reference numeral 1 denotes an exemplary electrode coating system in which electrodes for the production of lithium-ion batteries are coated in an electrode coating process S1. For example, one of the above-mentioned solvents can be used; in particular, a mixture of, for example, TEP and EAA can also be used as the solvent.

• Ein Prozessgasstrom A wird mithilfe eines Gebläses 3 aus einem Auslass der Elektrodenbeschichtungsanlage 1 über einen Prozessgaseinlass 25 zu einem Prozessgaskondensator 2 geführt. Mithilfe des Prozessgaskondensators 2 ist zumindest ein Teil des Prozessgasstroms A kondensierbar, wobei Wärmeenergie aus dem Prozessgasstrom auskoppelbar ist. Die Temperatur des im Prozessgasstrom A befindlichen Prozessgases beträgt typischerweise ca. 120 °C, beispielsweise in einem Bereich zwischen 100 bis 150 °C beim Eintritt in den Prozessgaskondensator 2. Im Prozessgaskondensator 2 wird das Prozessgas sukzessive vorzugsweise auf ca. 15 °C als Zieltemperatur heruntergekühlt. Der Prozessgaskondensator 2 weist drei hintereinander angeordnete als Wärmetauscher ausgebildete Kühlapparate 21, 22, 23 zum Ausführen eines dreistufigen Kondensationsschrittes S2 auf, wobei dem Prozessgasstrom A Wärmeenergie ausgekoppelt, also entzogen wird. Die Kühlapparate sind jeweils für eine Kühlstufe bestimmt. Mithilfe des ersten Kühlapparats 21 wird also die erste Kühlstufe S21a, im zweiten Kühlapparat 22 die zweite Kühlstufe S22a und im dritten Kühlapparat 23 die dritte Kühlstufe S23a ausgeführt, wobei das Prozessgas im ersten Kühlapparat 21 auf 60 °C, im zweiten Kühlapparat 22 auf 30 °C, im dritten Kühlapparat 23 auf 15 °C heruntergekühlt wird. Die Kühlapparate 21, 22, 23 sind beispielhaft als Kreuzstromwärmetauscher ausgeführt.

First, the arrangement along the process gas flow A is described:

• A process gas stream A is guided by means of a fan 3 from an outlet of the electrode coating system 1 via a process gas inlet 25 to a process gas condenser 2. With the aid of the process gas condenser 2, at least a portion of the process gas stream A can be condensed, wherein thermal energy can be extracted from the process gas stream. The temperature of the process gas in the process gas stream A is typically approximately 120 °C, for example in a range between 100 and 150 °C upon entry into the process gas condenser 2. In the process gas condenser 2, the process gas is successively cooled, preferably to approximately 15 °C as the target temperature. The process gas condenser 2 has three cooling devices 21, 22, 23 arranged one behind the other and designed as heat exchangers for carrying out a three-stage condensation step. tes S2, whereby heat energy is extracted from the process gas stream A. The cooling devices are each intended for a cooling stage. The first cooling stage S21a is carried out with the help of the first cooling device 21, the second cooling stage S22a in the second cooling device 22, and the third cooling stage S23a in the third cooling device 23, whereby the process gas is cooled to 60 °C in the first cooling device 21, to 30 °C in the second cooling device 22, and to 15 °C in the third cooling device 23. The cooling devices 21, 22, 23 are designed, for example, as cross-flow heat exchangers.

Downstream of the process gas condenser 2, a process gas heating device 24 in the form of a cross-flow heat exchanger is arranged, in which heat is supplied to the process gas stream A. After flowing through the process gas heating device 24, the process gas stream is fed back into the electrode coating system 1. By way of example, the process gas heating device 24 and the process gas condenser 2 are shown in a housing unit.

• Im ersten Kühlapparat 21 des Prozessgaskondensators 2 wird mindestens ein Teil des Prozessgasstroms A gekühlt. Die aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird in ein Arbeitsmittel eingekoppelt, welches sich in einem Arbeitsmittelkreis C zirkuliert. Der Arbeitsmittelkreis C kann mindestens eines Teils der Wärmeenergie transportieren, die in das Arbeitsmittel eingekoppelt ist. Eine Arbeitsmittelpumpe 7 wälzt das Arbeitsmittel im Kreis um, wobei die dafür benötigte elektrische Energie aus einem Generator 51 stammt. Eine nicht-dargestellte elektrische Leitung verbindet den Generator 51 mit der Arbeitsmittelpumpe 7, um diese mit Strom zu versorgen. Der erste Kühlapparat 21 wird also mithilfe des Arbeitsmittels gekühlt, wobei das Arbeitsmittel verdampft wird. In der Gesamtschau transportiert der Arbeitsmittelkreis C also mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelten Wärmeenergie aus dem Prozessgaskondensator 2 zu einer als Turbine ausgebildeten Wärmekraftmaschine 5. Danach führt der Arbeitsmittelkreis C zur Prozessgasheizvorrichtung 24, in welcher Wärmeenergie aus dem Arbeitsmittelkreis C auf den Prozessgasstrom A übertragen wird. Mittels der Prozessgasheizvorrichtung 24 kann also Wärmeenergie in den Prozessgasstrom A eingekoppelt werden. Dabei kondensiert sich das im Arbeitsmittelkreis C befindlichen Arbeitsmittel und wird zurück zum ersten Kühlapparat 21 geführt.

Now the arrangement along the working medium circuit C is described:

• In the first cooling device 21 of the process gas condenser 2, at least a portion of the process gas stream A is cooled. The thermal energy extracted from the process gas stream A is coupled into a working fluid that circulates in a working fluid circuit C. The working fluid circuit C can transport at least a portion of the thermal energy coupled into the working fluid. A working fluid pump 7 circulates the working fluid, with the electrical energy required for this coming from a generator 51. An electrical line (not shown) connects the generator 51 to the working fluid pump 7 to supply it with power. The first cooling device 21 is thus cooled using the working fluid, whereby the working fluid is evaporated. Overall, the working fluid circuit C transports at least a portion of the thermal energy extracted from the process gas stream A from the process gas condenser 2 to a heat engine 5 designed as a turbine. The working fluid circuit C then leads to the process gas heating device 24, in which thermal energy is transferred from the working fluid circuit C to the process gas stream A. By means of the process gas heating device 24, thermal energy can therefore be coupled into the process gas stream A. The working fluid in the working fluid circuit C condenses and is fed back to the first cooling device 21.

The working fluid circuit C has, in particular, a first working fluid line C1, which carries the largely gaseous working fluid from a working fluid outlet 21ii of the process gas condenser to an inlet 5i of the heat engine 5. Furthermore, the working fluid circuit C has a second working fluid line C2, which carries the working fluid from an outlet 5ii of the heat engine 5 to a working fluid inlet 24i of the process gas heating device 24. Downstream of the process gas heating device 24, the working fluid circuit C has a third working fluid line C3, which carries the now condensed working fluid from a working fluid outlet 24ii of the process gas heating device 24 to a working fluid inlet 21i of the process gas condenser 2. The working fluid is guided via the working fluid inlet 21i to the first cooling device 21, which simultaneously serves as a working fluid heating device for heating the working fluid. The working fluid is evaporated in the first cooling device 21.

The heat engine 5 is coupled to a generator 51, by means of which mechanical energy is converted into electrical energy, for example for feeding into a public power grid 53.

A cooling water stream D flows through the second cooling device 22 and is cooled by means of the cooling water contained therein. At least a portion of the thermal energy from the process gas stream A is thus transferred from the process gas stream to the cooling water stream D. At least a portion of the process gas stream A is cooled by means of the second cooling device 22. The cooling water stream D originates, for example, from an environment and is returned to the environment after flowing through the second cooling device 22.

The third cooling device 23 is cooled by a refrigerant flow E, similar to the second cooling device. At least part of the thermal energy from the process gas flow A is transferred to the refrigerant contained in the refrigerant flow. The refrigerant flow E, unlike the cooling water flow, is cooled in a refrigeration machine 6. Thermal energy is extracted from the refrigerant flow E and fed into the refrigeration machine 6. The refrigerant flow E originates, for example, from a source of the refrigeration machine (not shown), into which the refrigerant can be returned after flowing through the third cooling device 23. The reference symbol F schematically denotes a heat flow of the refrigeration machine 6, wherein the thermal energy extracted from the refrigerant flow E is transported away from the refrigeration machine 6.

1a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 1 .

• S1: Das Prozessgas kommt bei dem Elektrodenbeschichtungsprozess S1 zum Einsatz, wobei ein Lösemittel bei einer Trocknung von Elektroden in das Prozessgas übergeht.

The following process steps are carried out with respect to process gas stream A:

• S1: The process gas is used in the electrode coating process S1, whereby a solvent is transferred into the process gas during the drying of electrodes.

• S21a: Das Prozessgas wird in einer ersten Kühlstufe S21a eines Kondensationsschrittes S2 von ca. 120°C auf 60 °C abgekühlt. Wärmeenergie wird aus dem Prozessgasstrom A ausgekoppelt. Die gestrichelte Linie kennzeichnet beispielhaft den Wärmestrom, der aus S21a ausgekoppelt wird und direkt in den Verfahrensschritt S21b eingekoppelt wird.
• S22a: Das Prozessgas wird in einer zweiten Kühlstufe S22a des Kondensationsschrittes S2 von ca. 60 °C auf ca. 30 °C abgekühlt. Wärmeenergie wird aus dem Prozessgasstrom A ausgekoppelt. Die gestrichelte Linie kennzeichnet beispielhaft den Wärmestrom, der aus S22a ausgekoppelt wird und in den Verfahrensschritt S22b eingekoppelt wird.
• S23a: Das Prozessgas wird in einer dritten Kühlstufe S23a des Kondensationsschrittes S2 von ca. 30 °C auf ca. 15 °C abgekühlt. Wärmeenergie wird aus dem Prozessgasstrom A ausgekoppelt. Die gestrichelte Linie kennzeichnet beispielhaft den Wärmestrom, der aus S23a ausgekoppelt wird und in den Verfahrensschritt S23b eingekoppelt wird.
• S24a: Das Prozessgas wird in einem Heizvorgang von ca. 15°C auf ca. 60 °C aufgeheizt. Wärmeenergie wird in den Prozessgasstrom A eingekoppelt, wobei Wärmeenergie auf das Prozessgas übertragen wird. Die gestrichelte Linie kennzeichnet beispielhaft den Wärmestrom, der in S24b ausgekoppelt wird und direkt in den Verfahrensschritt S24a eingekoppelt wird.

The condensation step S2 comprises, for example, three cooling stages S21a, S22a, S23a.

• S21a: The process gas is cooled from approximately 120°C to 60°C in a first cooling stage S21a of a condensation step S2. Thermal energy is extracted from the process gas stream A. The dashed line indicates, as an example, the heat flow extracted from S21a and directly injected into process step S21b.
• S22a: The process gas is cooled from approximately 60 °C to approximately 30 °C in a second cooling stage S22a of the condensation step S2. Thermal energy is extracted from the process gas stream A. The dashed line indicates, as an example, the heat flow extracted from S22a and injected into process step S22b.
• S23a: The process gas is cooled from approximately 30 °C to approximately 15 °C in a third cooling stage S23a of the condensation step S2. Thermal energy is extracted from the process gas stream A. The dashed line indicates, as an example, the heat flow extracted from S23a and injected into process step S23b.
• S24a: The process gas is heated from approximately 15°C to approximately 60°C in a heating process. Thermal energy is coupled into process gas stream A, whereby thermal energy is transferred to the process gas. The dashed line indicates, as an example, the heat flow that is extracted in S24b and directly coupled into process step S24a.

• S21b: Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt in den Arbeitsmittelkreis C eingekoppelt. Das im Arbeitsmittelkreis C befindliche Arbeitsmittel wird erhitzt und verdampft.
• S5: In einer Wärmekraftmaschine 5 wird mindestens ein Teil der im Arbeitsmittel aufweisenden Wärmeenergie in mechanische Energie umgewandelt. Das Arbeitsmittel wird dabei entspannt.
• S24b: Das Arbeitsmittel wird gekühlt und dabei mindestens ein Teil der im Arbeitsmittel aufweisenden Wärmeenergie ausgekoppelt. Das Arbeitsmittel wird beim Kühlvorgang kondensiert.
• S51: Mechanische Energie wird in elektrische Energie umgewandelt.
• S53: Elektrische Energie wird aus der Anordnung abgeführt.

With regard to the working medium circuit C, the following process steps are carried out:

• S21b: At least part of the thermal energy extracted from the process gas stream A is directly coupled into the working fluid circuit C. The working fluid in the working fluid circuit C is heated and evaporated.
• S5: In a heat engine 5, at least a portion of the thermal energy contained in the working fluid is converted into mechanical energy. The working fluid is thereby expanded.
• S24b: The working fluid is cooled, and at least part of the thermal energy contained in the working fluid is extracted. The working fluid is condensed during the cooling process.
• S51: Mechanical energy is converted into electrical energy.
• S53: Electrical energy is dissipated from the device.

• S4: Kühlwasser wird zu einer zweiten Kühlstufe des Prozessgaskondensators 2 geführt.
• S22b: Mindestens ein Teil der aus dem Verfahrensschritt S22a ausgekoppelten Wärmeenergie wird in den Kühlwasserstrom D eingekoppelt. Das im Kühlwasserstrom D befindliche Kühlwasser wird dabei erwärmt.
• S11: Das Kühlwasser wird in eine Umgebung geführt.

The following process steps are carried out with respect to the cooling water flow D:

• S4: Cooling water is fed to a second cooling stage of the process gas condenser 2.
• S22b: At least a portion of the thermal energy extracted from process step S22a is coupled into the cooling water stream D. The cooling water in the cooling water stream D is thereby heated.
• S11: The cooling water is discharged into an environment.

• S6: Der Kältemittelstrom E wird in einer Kältemaschine 6 gekühlt.
• S23b: Mindestens ein Teil der aus dem Verfahrensschritt S22a ausgekoppelten Wärmeenergie wird in den Kältemittelstrom E eingekoppelt. Das im Kältemittelstrom E befindliche Kältemittel wird dabei erwärmt.

The following process steps are carried out with respect to the refrigerant flow E:

• S6: The refrigerant flow E is cooled in a chiller 6.
• S23b: At least a portion of the thermal energy extracted from process step S22a is coupled into the refrigerant stream E. The refrigerant in the refrigerant stream E is thereby heated.

The refrigerant is discharged after process step S22a and returned to the refrigeration machine 6.

2 shows a schematic representation of an arrangement 101 according to the invention for converting energy from an electrode coating system 1 with direct coupling to the working medium circuit C and with use of the refrigerant flow E in the working medium circuit C.

To illustrate the arrangement 101 according to the invention in 2 is made with reference to 1 Unless otherwise indicated, reference is made analogously to the above description in full.

Compared to 1 is in the arrangement in 2 Downstream of the process gas heating device 24, a coolant heat exchanger 63 designed as a working medium condenser is arranged, which is assigned to the working medium circuit C. The coolant Heat exchanger 63 can be cooled by a coolant to condense the working fluid. In this exemplary illustration, the coolant heat exchanger 63 is cooled by a refrigerant flow E. The working fluid circuit C and the refrigerant flow E flow through the coolant heat exchanger 63. Downstream of the heat engine 5, thermal energy is transferred from the working fluid to the process gas with the aid of the process gas heating device 24, whereby the working fluid is still essentially gaseous at the working fluid outlet 24. In the coolant heat exchanger 63, thermal energy can be extracted from the working fluid, whereby the working fluid is condensed and liquefied. The process gas heating device 24 can therefore have a function for pre-cooling the working fluid before the working fluid is condensed. The coolant heat exchanger 63 is designed here, for example, as a cross-flow heat exchanger. The coolant heat exchanger 63 is cooled by means of the refrigerant flow E, which is designed as a coolant flow and is guided to the coolant heat exchanger 63 after flowing through the second cooling device 23. The refrigerant flow E can optionally be returned to the refrigeration machine 6 after flowing through the coolant heat exchanger 63.

2a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 2 .

To illustrate the method according to the invention in 2a is made with reference to 1a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1a is used in the process in 2a After process step S5, the working fluid circulating in the working fluid circuit C is first led to process step S24c and then to process steps S63b, S21b. The refrigerant flow E leads to process step S63a after process step S23b.

• S24c: Das Arbeitsmittel wird gekühlt und dabei mindestens ein Teil der im Arbeitsmittel aufweisenden Wärmeenergie ausgekoppelt. Die gestrichelte Linie stellt schematisch den Wärmefluss zum Verfahrensschritt S24a dar.
• S63b: Das Arbeitsmittel wird gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird. Die gestrichelte Linie stellt schematisch den Wärmefluss zum S63a dar.
• S63a: Wärmeenergie wird in den Kältemittelstrom E eingekoppelt.

The following procedural steps are therefore carried out in addition:

• S24c: The working fluid is cooled, and at least a portion of the thermal energy contained in the working fluid is extracted. The dashed line schematically represents the heat flow to process step S24a.
• S63b: The working fluid is cooled and condensed, whereby heat energy is extracted from the working fluid located in the working fluid circuit C. The dashed line schematically represents the heat flow to S63a.
• S63a: Heat energy is coupled into the refrigerant flow E.

3 shows a schematic representation of an arrangement 102 according to the invention for converting energy from an electrode coating system 1 with direct coupling to the working medium circuit C and with use of the cooling water flow D in the working medium circuit C.

To illustrate the arrangement 102 according to the invention in 3 is made with reference to 1 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1 is arranged in 3 The cooling water flow D is led downstream of the second cooling device 22 to the coolant heat exchanger 63, wherein the coolant heat exchanger 63 is cooled by means of the cooling water flow D. Thermal energy is transferred from the working fluid to the cooling water.

3a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 3 .

To illustrate the method according to the invention in 3a is made with reference to 1a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1a is used in the process in 3a The cooling water flow D is led to process step S63c after process step S22b, before the cooling water flow D is led to process step S11. Furthermore, in the working fluid circuit C, process step S24c takes place after process step S5, followed by process steps S63b and S21b.

• S63b: Das Arbeitsmittel wird kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird. Die gestrichelte Linie stellt schematisch den Wärmefluss zum S63c dar.
• S63c: Wärmeenergie wird in den Kühlwasserstrom D eingekoppelt.

The following procedural steps are therefore carried out in addition:

• S63b: The working fluid is condensed, whereby heat energy is extracted from the working fluid located in the working fluid circuit C. The dashed line schematically represents the heat flow to S63c.
• S63c: Thermal energy is coupled into the cooling water flow D.

4 shows a schematic representation of an arrangement 103 according to the invention for converting energy from an electrode coating system 1 with direct coupling to the working medium circuit C and with use of the refrigerant flow E as well as with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 103 according to the invention in 4 is made with reference to 1 and 2 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1 is arranged in 4 in analogy to 2 The refrigerant flow E is conducted to the coolant heat exchanger 63. Waste heat from the refrigeration machine 6 is conducted by means of a refrigeration machine heat flow F to the working fluid preheater 66 for coupling at least a portion of the thermal energy into the working fluid, which thermal energy is extracted from the refrigeration machine 6, wherein the thermal energy was previously coupled from the refrigerant flow E into the refrigeration machine 6. The refrigeration machine heat flow F can also be understood as waste heat from the refrigeration machine 6.

4a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 4 .

To illustrate the method according to the invention in 4a is made with reference to 1a and 2a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 2a takes place in the procedure in 4a In the working fluid circuit C, after process step S63b, process step S66 takes place. In process step S66, at least a portion of the heat energy extracted from the refrigeration machine is coupled into the working fluid circuit C as refrigeration machine heat flow F.

5 shows a schematic representation of an arrangement 104 according to the invention for converting energy from an electrode coating system 1 with direct coupling to the working medium circuit C and with use of the cooling water flow D as well as with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 104 according to the invention in 5 is made with reference to 1 and 3 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1 is arranged in 5 the cooling water flow D analogously as in 3 to the coolant heat exchanger 63. Waste heat from the refrigeration machine 6 is conveyed by means of a refrigeration machine heat flow F to the working medium preheater 66 for coupling at least a portion of the thermal energy into the working medium, which thermal energy is extracted from the refrigeration machine 6, wherein the thermal energy was previously coupled into the refrigeration machine 6 from the refrigerant flow E.

5a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 5 .

To illustrate the method according to the invention in 5a is made with reference to 1a and 3a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 3a takes place in the procedure in 5a In the working fluid circuit C, after process step S63b, process step S66 takes place. In process step S66, at least a portion of the heat energy extracted from the refrigeration machine is coupled into the working fluid circuit C as refrigeration machine heat flow F.

6 shows a schematic representation of an arrangement 105 according to the invention for converting energy from an electrode coating system 1, comprising an intermediate circuit B for coupling to the working fluid circuit C. The reference symbol B generally designates the intermediate circuit and can comprise the intermediate fluid in both the gaseous and liquid states. This is also the case for the reference symbol C, which generally designates the working fluid circuit and can comprise the working fluid in both the gaseous and liquid states.

To illustrate the arrangement 105 according to the invention in 6 is made with reference to 1 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1 includes the order 105 in 6 an intermediate medium circuit B, in which, for example, water circulates as an intermediate medium for transporting thermal energy. An intermediate medium pump 71 circulates the intermediate medium in the circuit, whereby the electrical energy required for this comes from the generator 51 and an electrical line (not shown) connects the generator 51 to the intermediate medium pump 71 for the power supply. In the first cooling device 21, at least a portion of the thermal energy present in the process gas stream A is transferred to the intermediate medium circuit B. From an intermediate medium outlet 21iv of the process gas condenser 2, the intermediate medium is discharged by means of a first intermediate medium line B1 and guided to an intermediate medium inlet 9i of the working medium evaporator 9. The working medium evaporator 9 is both by both the intermediate medium and the working medium. In the working medium evaporator 9, at least a portion of the thermal energy present in the intermediate medium is coupled into the working medium circuit C for evaporating the working medium. The thermal energy coupled out of the process gas stream A can therefore be transported to the working medium evaporator 9 with the aid of the intermediate medium. After flowing through the working medium evaporator 9, the intermediate medium is discharged from an intermediate medium outlet 9ii of the working medium evaporator 9 with the aid of a second intermediate medium line B2. After being discharged from the working medium evaporator 9, the intermediate medium is guided by means of the second intermediate medium line B2 to an intermediate medium inlet 24iii of the process gas heating device 24. In the process gas heating device 24, at least a portion of the thermal energy present in the intermediate medium is transferred to the process gas stream A. After flowing through the process gas heating device 24, the intermediate medium is discharged from the process gas heating device 24 via an intermediate medium outlet 24iv. By means of a third intermediate medium line B3, the intermediate medium circulating in the intermediate medium circuit B is led back to an intermediate medium inlet 21iii of the process gas condenser 2.

The working fluid circuit C comprises the working fluid evaporator 9 for evaporating the working fluid, the heat engine 5 for converting thermal energy into mechanical energy and an air heat exchanger 8 designed as a working fluid condenser. The circulation of the working fluid in the circuit is analogous to 1 realized with the help of the working fluid pump 7. The working fluid is thus fed to a working fluid inlet 9iii of the working fluid evaporator 9. In the working fluid evaporator 9, thermal energy from the intermediate fluid is coupled into the working fluid. The working fluid is evaporated and then discharged from the working fluid outlet 9iv of the working fluid evaporator 9 and fed to the inlet 5i of the heat engine. After the working fluid has been expanded in the heat engine, it is fed to the outlet 5ii of the heat engine and to the air heat exchanger 8, in which thermal energy is extracted from the working fluid and transferred to an air stream. The working fluid condenses in the process. After the working fluid has condensed, the working fluid is fed back to the working fluid inlet 9iii of the working fluid evaporator 9.

6a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 6 .

To illustrate the method according to the invention in 6a is made with reference to 1a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 1a indicates the procedure in 6a an intermediate center circle B.

• S21c: Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt in den Zwischenmittelkreis B eingekoppelt. Die gestrichelte Linie zwischen S21a und S21c stellt den Wärmefluss zwischen beiden Verfahrensschritten dar.
• S9a: Wärmeenergie wird zur Verdampfung des Arbeitsmittels aus dem Zwischenmittelkreis B ausgekoppelt. Die gestrichelte Linie zwischen S9a und S9b stellt den Wärmefluss zwischen beiden Verfahrensschritten dar.
• S24d: Wärmeenergie wird zum Aufheizen des Prozessgasstroms A aus dem Zwischenmittelkreis B ausgekoppelt. Die gestrichelte Linie zwischen S24d und S24a stellt den Wärmefluss zwischen beiden Verfahrensschritten dar.

The following process steps are carried out with regard to the intermediate center circle B:

• S21c: At least a portion of the heat energy extracted from the process gas stream A is directly coupled into the intermediate circuit B. The dashed line between S21a and S21c represents the heat flow between the two process steps.
• S9a: Thermal energy is extracted from the intermediate circuit B to evaporate the working fluid. The dashed line between S9a and S9b represents the heat flow between the two process steps.
• S24d: Thermal energy is extracted from the intermediate circuit B to heat the process gas stream A. The dashed line between S24d and S24a represents the heat flow between the two process steps.

• S9b: Wärmeenergie wird zur Verdampfung des Arbeitsmittels in den Arbeitsmittelkreis C eingekoppelt und das Arbeitsmittel verdampft.

With regard to the working medium circuit C, the following process steps are carried out:

• S9b: Heat energy is coupled into the working fluid circuit C to evaporate the working fluid and the working fluid evaporates.

• S5: In der Wärmekraftmaschine 5 wird mindestens ein Teil der im Arbeitsmittel aufweisenden Wärmeenergie in mechanische Energie umgewandelt. Das Arbeitsmittel wird dabei entspannt.
• S8: Wärmeenergie wird aus dem Arbeitsmittel ausgekoppelt und in eine Umgebung abgeführt.

Evaporated working fluid is then fed to heat engine 5.

• S5: In heat engine 5, at least a portion of the thermal energy contained in the working fluid is converted into mechanical energy. The working fluid is thereby expanded.
• S8: Heat energy is extracted from the working fluid and dissipated into the environment.

7 shows a schematic representation of an arrangement 106 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the cooling water flow D in the intermediate circuit B.

To illustrate the arrangement 106 according to the invention in 7 is made with reference to 6 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 6 is arranged in 7 the cooling water flow D downstream of the second cooling device 22 to the coolant heat exchanger 63, wherein the coolant heat exchanger 63 is cooled by means of the cooling water flow D. At least a portion of the thermal energy is transferred from the intermediate medium to the cooling water. In the coolant heat exchanger 63, the intermediate medium is cooled, and thermal energy is extracted from the intermediate medium circuit B. After flowing through the coolant heat exchanger 63, the cooling water is discharged into the environment.

7a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 7 .

To illustrate the method according to the invention in 7a is made with reference to 6a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 6a takes place in the procedure in 7a Method step S63e takes place after method step S24c.

In process step S63e, the intermediate medium is cooled, whereby heat energy is extracted from the intermediate medium located in the intermediate medium circuit B. The dashed line schematically represents the heat flow to S63c.

8 shows a schematic representation of an arrangement 107 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the cooling water flow D as well as with use of the waste heat of the refrigeration machine 6 in the intermediate circuit B.

To illustrate the arrangement 107 according to the invention in 8 is made with reference to 7 Unless otherwise indicated, reference is made analogously to the above description in full.

When arranging in 8 the refrigerant flow E is cooled by means of the refrigeration machine 6, whereby a portion of the thermal energy is extracted from the refrigerant flow E and fed into the refrigeration machine 6. At least a portion of the waste heat of the refrigeration machine 6 can therefore comprise the thermal energy extracted from the refrigerant flow E.

Deviating from 7 is arranged in 8 the waste heat of the refrigeration machine 6 is led to an intermediate medium preheater 64, in which thermal energy from the refrigerant flow E can be coupled into the intermediate medium circuit B. At least part of the waste heat of the refrigeration machine 6 can therefore be used to recycle it by preheating the intermediate medium flow B before it is led to the first cooling device 21.

8a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 8 .

To illustrate the method according to the invention in 8a is made with reference to 7a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 7a takes place in the procedure in 8a After process step S63e, process step S64 takes place. The dashed line between process steps S6 and S64 indicates the heat flow that is added to process step S64 as waste heat from the refrigeration machine 6. In process step S64, thermal energy is coupled into the intermediate circuit B.

9 shows a schematic representation of an arrangement 108 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the refrigerant flow E in the intermediate circuit B.

To illustrate the arrangement 108 according to the invention in 9 is made with reference to 6 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 6 is arranged in 9 The refrigerant flow E is conducted downstream of the second cooling device 22 to the coolant heat exchanger 63, wherein the coolant heat exchanger 63 is cooled by means of the refrigerant flow E. At least part of the thermal energy is transferred from the intermediate medium to the refrigerant. In the coolant heat exchanger 63, the intermediate medium is cooled, and thermal energy is extracted from the intermediate medium circuit B. After flowing through the coolant heat exchanger 63, the refrigerant can optionally be conducted back to the refrigeration machine 6.

9a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 9 .

To illustrate the method according to the invention in 9a is made with reference to 6a , unless otherwise indicated, analogue Please refer in full to the above description.

Deviating from 6a takes place in the procedure in 9a Method step S63e takes place after method step S24d.

In process step S63e, the intermediate medium is cooled, whereby heat energy is extracted from the intermediate medium located in the intermediate medium circuit B. The dashed line schematically represents the heat flow to S63a.

In process step S63a, thermal energy is coupled into the refrigerant flow E.

10 shows a schematic representation of an arrangement 109 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the refrigerant flow E as well as with use of the waste heat of the refrigeration machine 6 in the intermediate circuit B.

To illustrate the arrangement 109 according to the invention in 10 is made with reference to 9 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 9 is arranged in 10 At least part of the waste heat of the refrigeration machine 6 is led to the intermediate medium preheater 64 and coupled into the intermediate medium circuit B. Analogous to the above embodiment for 8 Thus, at least part of the waste heat from the refrigeration machine 6 can be reused by preheating the intermediate medium flow B with the waste heat from the refrigeration machine 6 before it is fed to the first cooling device 21.

10a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 10 .

To illustrate the method according to the invention in 10a is made with reference to 9a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 9a takes place in the procedure in 10a After process step S63e, process step S64 takes place. The dashed line between process steps S6 and S64 indicates the heat flow that is added to process step S64 as waste heat from the refrigeration machine 6. In process step S64, at least a portion of the heat energy extracted from the refrigeration machine 6 is coupled into the intermediate circuit B as refrigeration machine heat flow F.

11 shows a schematic representation of an arrangement 110 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling to the working medium circuit C and with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 110 according to the invention in 11 is made with reference to 6 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 6 is in the arrangement in 11 The working fluid preheater 66 is arranged downstream of the air heat exchanger 8, which is designed as a working fluid condenser. The operation of the working fluid preheater 66 can be seen in the above description. With the help of the working fluid preheater 66, the working fluid can be preheated before it is fed to the working fluid evaporator 9. Waste heat from the refrigeration machine 6 is coupled into the working fluid as thermal energy via the refrigeration machine heat flow F.

11a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 11 .

To illustrate the method according to the invention in 11a is made with reference to 6a Unless otherwise indicated, reference is made analogously to the above description in full.

• S66: Mindestens ein Teil der aus der Kältemaschine 6 ausgekoppelten Wärmeenergie wird als Kältemaschine-Wärmefluss F in den Arbeitsmittelkreis C eingekoppelt.

Deviating from 6a is used in the process in 11a after process step S8, process step S66 is carried out:

• S66: At least part of the heat energy extracted from the refrigeration machine 6 is coupled into the working fluid circuit C as refrigeration machine heat flow F.

12 shows a schematic representation of an arrangement 111 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the refrigerant flow E in the working medium circuit C.

To illustrate the arrangement 111 according to the invention in 12 is made with reference to 6 , unless otherwise indicated, ana Logically, reference is made to the above description in full.

Deviating from 6 is in the arrangement in 12 A working fluid cooler 81 for cooling the working fluid is assigned to the working fluid circuit C downstream of the heat engine 5. A coolant heat exchanger 63, as a working fluid condenser, is further arranged downstream of the working fluid cooler 81. The condensation process of the working fluid can thus be divided into two separate steps with this arrangement. In a first step, the temperature of the working fluid can be lowered using the working fluid cooler 81, whereby at least part of the thermal energy can be released to the environment. In a further subsequent step, the working fluid can then be condensed and liquefied using the coolant heat exchanger 63. The working fluid can then be fed in a largely liquid state to the working fluid inlet 9iii of the working fluid evaporator 9. Advantageously, the present arrangement also allows the refrigerant flow E to be additionally used to extract thermal energy from the working fluid circuit C. Optionally, the refrigerant flow E can be fed back to the refrigeration engine 6 downstream of the coolant heat exchanger 63.

12a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 12 .

To illustrate the method according to the invention in 12a is made with reference to 6a Unless otherwise indicated, reference is made analogously to the above description in full.

• S81: Wärmeenergie wird dem Arbeitsmittel entzogen. Die Temperatur des Arbeitsmittels wird gesenkt.
• S63b: Das Arbeitsmittel wird gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird. Die gestrichelte Linie stellt schematisch den Wärmefluss zum S63a dar.
• S9b: Wärmeenergie wird zur Verdampfung des Arbeitsmittels in den Arbeitsmittelkreis C eingekoppelt und das Arbeitsmittel verdampft.

Deviating from 6a is used in the process in 12a After process step S5, process step S81 is performed. After process step S9b, process step S5 takes place. The following process steps are therefore performed with respect to working fluid circuit C:

• S81: Heat energy is removed from the working fluid. The temperature of the working fluid is reduced.
• S63b: The working fluid is cooled and condensed, whereby heat energy is extracted from the working fluid located in the working fluid circuit C. The dashed line schematically represents the heat flow to S63a.
• S9b: Heat energy is coupled into the working fluid circuit C to evaporate the working fluid and the working fluid evaporates.

• Abweichend zu 6a findet nach dem Verfahrensschritt S23b der Verfahrensschritt S63a statt. Nach dem Verfahrensschritt S63a wird der Kältemittelstrom E beispielhaft zurück zum Verfahrensschritt S6 geführt.
• S63a: Wärmeenergie wird in den Kältemittelstrom E eingekoppelt.

The following process steps are carried out with respect to the refrigerant flow E:

• Deviating from 6a After process step S23b, process step S63a takes place. After process step S63a, the refrigerant stream E is, for example, returned to process step S6.
• S63a: Heat energy is coupled into the refrigerant flow E.

13 shows a schematic representation of an arrangement 112 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling to the working medium circuit C and with use of the cooling water flow D in the working medium circuit C.

To illustrate the arrangement 112 according to the invention in 13 is made with reference to 12 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 12 is arranged in 13 the coolant heat exchanger 63 designed as a working medium condenser is cooled with the cooling water flow D. The cooling water flow D can, for example, originate from an environment, for example from a cooling water source, and first flows through the second cooling apparatus 22 to absorb thermal energy from the process gas flow A. The present arrangement allows the cooling water flow D to be advantageously used to absorb even more thermal energy in addition to the part from the process gas flow A. In particular, a usable residual heat capacity of the cooling water flow D can be further utilized to condense the working medium.

The usable residual heat capacity of the cooling water flow D can therefore be understood as the thermal energy absorption capacity that is still available after thermal energy has already been absorbed, in this example after flowing through the second cooling device 22. Technically, a certain usable residual heat capacity of the cooling water flow D can be achieved if condensation of the working fluid in the coolant heat exchanger 63 can be realized with the aid of the cooling water flow D.

The concept of usable residual heat capacity can generally also be applied to a coolant flow, i.e. both to the cooling water flow D and to the refrigerant flow E. Technically, in this sense, a usable residual heat capacity of a coolant flow can generally be given if a cooling effect can be achieved with the help of the coolant flow.

13a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 13 .

To illustrate the method according to the invention in 13a is made with reference to 12a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 12a takes place in the procedure in 13a The heat flow takes place between process step S63b and process step S63c. The heat flow resulting from process step S63b is thus coupled into process step S63c.

In process step S63c, thermal energy is coupled into the cooling water stream D.

After process step S63c, process step S11 takes place, wherein the cooling water flow D is discharged into an environment.

14 shows a schematic representation of an arrangement 113 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the cooling water flow D as well as with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 113 according to the invention in 14 is made with reference to 13 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 13 is in the arrangement in 14 With respect to the working fluid circuit C, the working fluid preheater 66 is arranged downstream of the coolant heat exchanger 63. Waste heat from the refrigeration machine 6 is conducted by means of the refrigeration machine heat flow F to the working fluid preheater 66 for coupling at least a portion of the thermal energy into the working fluid, which thermal energy is extracted from the refrigeration machine 6, wherein the thermal energy was previously coupled into the refrigeration machine 6 from the refrigerant flow E.

14a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 14 .

To illustrate the method according to the invention in 14a is made with reference to 13a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 13a takes place in the procedure in 14a With regard to the working fluid circuit C, process step S66 takes place downstream of process step S63b.

In method step S66, at least a portion of the heat energy extracted from the refrigeration machine 6 is coupled into the working fluid circuit C, represented as refrigeration machine heat flow F.

15 shows a schematic representation of an arrangement 114 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the refrigerant flow E as well as with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 114 according to the invention in 15 is made with reference to 14 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 14 is arranged in 15 the coolant heat exchanger 63 designed as a working medium condenser is cooled with the refrigerant flow E. The refrigerant flow E is cooled in the refrigeration machine 6 downstream of the third cooling device 23. After flowing through the third cooling device 23, the refrigerant flow E is guided to the coolant heat exchanger 63. Downstream of the coolant heat exchanger 63, the refrigerant flow E can optionally be guided back to the refrigeration machine. The present arrangement therefore allows the refrigerant flow E to be advantageously used to absorb even more thermal energy in the third cooling device 23, wherein the refrigerant flow E has already previously absorbed a certain amount of thermal energy from the process gas flow A. In particular, a usable residual heat capacity of the refrigerant flow E can be used to condense the working medium. In this arrangement, too, analogous to the above description in 12 The condensation process of the working fluid is carried out separately. This is done using the working fluid cooler 81, first to lower the working fluid temperature, and then using the coolant heat exchanger 63 to condense the working fluid.

As in 14 is also in this order 114 according to 15 Waste heat from the refrigeration machine 6 is coupled into the working fluid circuit C using the working fluid preheater 66. Particularly energetic Advantageous in this arrangement is the use of the waste heat of the refrigeration machine 6, wherein at least a part of the total thermal energy coupled into the refrigerant flow E, which originates both from the third cooling apparatus 23 and from the coolant heat exchanger 63, can be coupled into the working medium circuit C for preheating the working medium.

15a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 15 .

To illustrate the method according to the invention in 15a is made with reference to 14a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 14a takes place in the procedure in 15a After method step S81, method step S63b takes place.

In process step S63b, the working fluid is cooled and condensed. Thermal energy is extracted from the working fluid located in the working fluid circuit C. The dashed line represents a heat flow to S63a.

In process step S63a, thermal energy is coupled into the refrigerant flow E. The refrigerant flow E then returns to process step S6, where thermal energy is extracted from the refrigerant flow E. The dashed line represents the heat flow to S66.

16 shows a schematic representation of an arrangement 115 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the refrigerant flow E for condensing a working medium.

To illustrate the arrangement 115 according to the invention in 16 is made with reference to 6 Unless otherwise indicated, reference is made analogously to the above description in full.

With regard to the working fluid circuit C, the arrangement in 16 The working fluid is led downstream of the heat engine 5 to the coolant heat exchanger 63, which is designed as a working fluid condenser. The coolant heat exchanger 63 is cooled by means of the refrigerant flow E, with at least a portion of the thermal energy being extracted from the working fluid circuit and coupled into the refrigerant flow E. The working fluid is thereby cooled and condensed.

The refrigerant flow E cooled by the refrigeration machine 6 is fed to the third cooling device 23. Downstream of the third cooling device 23, the refrigerant flow E is fed to the coolant heat exchanger 63 for further absorption of thermal energy. Optionally, the refrigerant flow E can be fed back to the refrigeration machine 6 downstream of the coolant heat exchanger 63.

16a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 16 .

To illustrate the method according to the invention in 16a is made with reference to 6a Unless otherwise indicated, reference is made analogously to the above description in full.

• Nach dem Verfahrensschritt S23b findet der Verfahrensschritt S63a statt.
• S63a: Wärmeenergie wird in den Kältemittelstrom E eingekoppelt. Die gestrichelte Linie stellt den Wärmefluss dar, welcher in den Verfahrensschritt S63a eingekoppelt wird.
• Der Kältemittelstrom E wird nach dem Verfahrensschritt S63a zurück zum Verfahrensschritt S6 geführt.
• Nach dem Verfahrensschritt S5 findet der Verfahrensschritt S63b statt.
• S63b: Das Arbeitsmittel wird gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird. Die gestrichelte Linie stellt schematisch den Wärmefluss zum S63a dar.

Deviating from 6a are used in the process 16a The following procedural steps are carried out:

• After process step S23b, process step S63a takes place.
• S63a: Heat energy is coupled into the refrigerant flow E. The dashed line represents the heat flow that is coupled into process step S63a.
• After process step S63a, the refrigerant flow E is returned to process step S6.
• After process step S5, process step S63b takes place.
• S63b: The working fluid is cooled and condensed, whereby heat energy is extracted from the working fluid located in the working fluid circuit C. The dashed line schematically represents the heat flow to S63a.

17 shows a schematic representation of an arrangement 116 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the refrigerant flow E for condensing a working medium and with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 116 according to the invention in 17 is made with reference to 16 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 16 is in the arrangement 116 in 17 With respect to the working fluid circuit C, a working fluid preheater 66 is arranged downstream of the coolant heat exchanger 63. Waste heat from the refrigeration machine 6 is conducted by means of the refrigeration machine heat flow F to the working fluid preheater 66 for coupling at least a portion of the thermal energy into the working fluid, which thermal energy is extracted from the refrigeration machine 6, wherein the thermal energy from the refrigerant flow E was injected into the refrigeration machine 6.

17a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 17 .

To illustrate the method according to the invention in 17a is made with reference to 16a Unless otherwise indicated, reference is made analogously to the above description in full.

• S66: Mindestens ein Teil der aus der Kältemaschine ausgekoppelten Wärmeenergie wird als Kältemaschine-Wärmefluss F in den Arbeitsmittelkreis C eingekoppelt.

Deviating from 16a is used in the process in 17a after process step S63b, process step S66 is carried out:

• S66: At least part of the heat energy extracted from the chiller is coupled into the working fluid circuit C as chiller heat flow F.

18 shows a schematic representation of an arrangement 117 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the cooling water flow D for condensing a working medium.

To illustrate the arrangement 117 according to the invention in 18 is made with reference to 16 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 16 is arranged in 18 the coolant heat exchanger 63 designed as a working medium condenser is cooled with the cooling water flow D. The cooling water flow D can, for example, originate from an environment, for example from a cooling water source, and first flows through the second cooling apparatus 22 to absorb thermal energy from the process gas flow A. The present arrangement allows the cooling water flow D to be advantageously used to absorb even more thermal energy in addition to the part from the process gas flow A.

In particular, a usable residual heat capacity of the cooling water flow D can be used to condense the working fluid.

18a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 18 .

To illustrate the method according to the invention in 18a is made with reference to 16a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 16a takes place in the procedure in 18a The heat flow takes place between process step S63b and process step S63c. The heat flow resulting from process step S63b is thus coupled into process step S63c.

In process step S63c, thermal energy is coupled into the cooling water flow D. The description of process step S63b can be found in the above description.

With regard to the cooling water flow D, the method step S11 is carried out after the method step S63c, in which the cooling water flow D is discharged into an environment.

19 shows a schematic representation of an arrangement 118 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for coupling with the working medium circuit C and with use of the cooling water flow D for condensing a working medium and with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 118 according to the invention in 19 is made with reference to 18 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 18 is in the arrangement in 19 With respect to the working fluid circuit C, the working fluid preheater 66 is arranged downstream of the coolant heat exchanger 63. Waste heat from the refrigeration machine 6 is conducted by means of a refrigeration machine heat flow F to the working fluid preheater 66 for coupling at least a portion of the thermal energy into the working fluid, which thermal energy is extracted from the refrigeration machine 6, wherein the thermal energy from the refrigerant flow E was injected into the refrigeration machine 6.

19a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 19 .

To illustrate the method according to the invention in 19a is made with reference to 18a Unless otherwise indicated, reference is made analogously to the above description in full.

• S66: Mindestens ein Teil der aus der Kältemaschine ausgekoppelten Wärmeenergie wird als Kältemaschine-Wärmefluss F in den Arbeitsmittelkreis C eingekoppelt.

Deviating from 18a is used in the process in 19a after process step S63b, process step S66 is carried out:

• S66: At least part of the heat energy extracted from the chiller is coupled into the working fluid circuit C as chiller heat flow F.

20 shows a schematic representation of an arrangement 119 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for direct evaporation and condensation of the working medium.

To illustrate the arrangement 119 according to the invention in 20 is made with reference to 6 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 6 The intermediate center circle B includes the arrangement in 20 an air cooler 82 for cooling an intermediate medium circulating in the intermediate medium circuit B. The air cooler 82 is arranged downstream of the working medium evaporator 9. Furthermore, the intermediate medium circuit B comprises an intermediate medium heat exchanger 68 designed as a working medium condenser, which is cooled by means of the intermediate medium to condense the working medium. The intermediate medium heat exchanger 68 is flowed through both as a heat-absorbing flow by the intermediate medium and as a heat-releasing flow by the working medium, with heat energy being transferred from the working medium to the intermediate medium. The working medium is thus condensed directly with the aid of the intermediate medium, with heat energy being transferred between two adjacent flows. In this case, the flows of the intermediate medium circuit B and the working medium circuit C are arranged adjacent to one another within the intermediate medium heat exchanger 68. The direct heat transfer in the intermediate medium heat exchanger 68 thus takes place analogously to the working medium evaporator 9, whereby the heat flow in the case of the condensation process of the working medium in the intermediate medium heat exchanger 68 is directed in the opposite direction to the evaporation process in the working medium evaporator 9.

By means of a first intermediate medium line B1, the intermediate medium is guided to an intermediate medium inlet 9i of the working medium evaporator. Via a second intermediate medium line B2, the intermediate medium is discharged from an intermediate medium outlet 9ii of the working medium evaporator 9. The intermediate medium is guided to the air cooler 82, in which the intermediate medium is cooled and thermal energy is extracted from the intermediate medium. The thermal energy is dissipated into the environment via a fan of the air cooler 82. The intermediate medium is guided downstream of the air cooler 82 to the intermediate medium heat exchanger 68, by means of which the intermediate medium is heated, with thermal energy being extracted during the condensation of the working medium and injected into the intermediate medium. The heated intermediate medium is discharged from the intermediate medium heat exchanger 68 via an intermediate medium outlet of the intermediate medium heat exchanger 68 and guided to the process gas heating device 24.

With regard to the working equipment circuit C, in deviation from 6 when arranging in 20 The working fluid is conducted downstream of the heat engine 5 via a working fluid inlet 68iii of the intermediate fluid heat exchanger 68 to the intermediate fluid heat exchanger 68, in which the working fluid is condensed. After the condensation process, the working fluid is conducted back to an inlet 9iii of the working fluid evaporator 9 via a working fluid outlet 68iv of the intermediate fluid heat exchanger 68.

20a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 20 .

To illustrate the method according to the invention in 20a is made with reference to 6a Unless otherwise indicated, reference is made analogously to the above description in full.

• S82: Wärmeenergie wird aus dem Zwischenmittel ausgekoppelt. Das Zwischenmittel wird gekühlt.
• S68a: Wärmeenergie wird mithilfe des Zwischenmittelwärmetauschers 68 in das Zwischenmittel eingekoppelt. Das Zwischenmittel wird aufgeheizt. Die gestrichelte Linie stellt einen Wärmefluss zwischen S68b und S68a dar.

In the process in 20a The following procedural steps are carried out with regard to the intermediate center circle B:

• S82: Heat energy is extracted from the intermediate medium. The intermediate medium is cooled.
• S68a: Thermal energy is coupled into the intermediate medium using the intermediate medium heat exchanger 68. The intermediate medium is heated. The dashed line represents a heat flow between S68b and S68a.

• S68b: Wärmeenergie wird mithilfe des Zwischenmittelwärmetauschers 68 aus dem Arbeitsmittel ausgekoppelt. Das Arbeitsmittel wird gekühlt und kondensiert. Die aus dem Arbeitsmittel ausgekoppelte Wärmeenergie wird in den Verfahrensschritt S68a eingekoppelt.

With regard to the working fluid circuit C, process step S68b is carried out after process step S5:

• S68b: Thermal energy is extracted from the working fluid using the intermediate heat exchanger 68. The working fluid is cooled and condensed. The thermal energy extracted from the working fluid is fed into process step S68a.

21 shows a schematic representation of an arrangement 120 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for direct evaporation and pre-cooling of the working medium and with use of the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 120 according to the invention in 21 is made with reference to 20 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 20 is in the arrangement in 21 With respect to the working fluid circuit C, the working fluid preheater 66 is arranged downstream of the intermediate fluid heat exchanger 68. The working fluid preheater 66 is heated using the refrigeration machine heat flow F. The working fluid can be preheated using the working fluid preheater 66 before the working fluid is supplied to the working fluid evaporator 9. In particular, the heat energy required in the working fluid evaporator 9 to evaporate the working fluid can be reduced using the working fluid preheater 66. The functioning of the working fluid preheater 66 can be seen in the above description.

21a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 21 .

To illustrate the method according to the invention in 21a is made with reference to 20a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 20a is used in the process in 21a After method step S68b, method step S66 is executed. The description of method step S66 can be found above.

22 shows a schematic representation of an arrangement 121 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for direct evaporation and pre-cooling of the working medium and with use of the refrigerant flow E in the working medium circuit C.

To illustrate the arrangement 121 according to the invention in 22 is made with reference to 20 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 20 is in the arrangement in 22 With respect to the working fluid circuit C, downstream of the heat engine 5, a working fluid precooler 69 is arranged for precooling the working fluid. The working fluid precooler 69 is cooled using the intermediate medium, whereby thermal energy is extracted from the working fluid and fed into the intermediate medium. Furthermore, in the working fluid circuit C, downstream of the working fluid precooler 69, the coolant heat exchanger 63 is arranged for condensing the working fluid, in which the working fluid is cooled and condensed. In summary, after expansion in the heat engine 5, the working fluid is first precooled in a first step, i.e., its temperature is lowered, and then condensed in a second step before the working fluid is fed to the working fluid evaporator 9.

Regarding the intermediate medium circuit B, the intermediate medium is first fed to the direct evaporation in the working medium evaporator 9 and then used for direct pre-cooling in the working medium pre-cooler 69. The terms direct evaporation and direct pre-cooling can be used analogously as in the above description to 20 In particular, they are aimed at heat transfer between two adjacent flows.

22a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 22 .

To illustrate the method according to the invention in 22a is made with reference to 20a Unless otherwise indicated, reference is made analogously to the above description in full.

• S69b: Wärmeenergie wird mithilfe des Arbeitsmittelvorkühlers 69 aus dem Arbeitsmittel ausgekoppelt. Die gestrichelte Linie stellt den Wärmefluss dar, der aus dem Verfahrensschritt S69b ausgekoppelt und in den Verfahrensschritt S69a eingekoppelt wird.
• S69a: Wärmeenergie mithilfe des Arbeitsmittelvorkühlers 69 wird in das Zwischenmittel eingekoppelt.
• S63b: Das Arbeitsmittel wird gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird. Die gestrichelte Linie stellt schematisch den Wärmefluss zum S63a dar.

In the process in 22a the following procedural steps are also carried out:

• S69b: Thermal energy is extracted from the working fluid using the working fluid precooler 69. The dashed line represents the heat flow extracted from process step S69b and injected into process step S69a.
• S69a: Heat energy is coupled into the intermediate medium using the working medium pre-cooler 69.
• S63b: The working fluid is cooled and condensed, whereby heat energy from the working fluid in the working fluid circuit C The dashed line schematically represents the heat flow to S63a.

23 shows a schematic representation of an arrangement 122 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for direct evaporation and cooling of the working medium and with use of the refrigerant flow E and the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 122 according to the invention in 23 is made with reference to 22 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 22 is in the arrangement in 23 With respect to the working fluid circuit C, the working fluid preheater 66 is arranged downstream of a coolant heat exchanger 63. For the functioning of the working fluid preheater 66, reference is made to the above description, in particular to the 21 referred to.

23a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 23 .

To illustrate the method according to the invention in 23a is made with reference to 22a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 22a is used in the process in 23a In the working fluid circuit C, process step S66 is carried out after process step S63b. Process step S66 can be found in the description above.

24 shows a schematic representation of an arrangement 123 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for direct evaporation and pre-cooling of the working medium and with use of the cooling water flow D in the working medium circuit C.

To illustrate the arrangement 123 according to the invention in 24 is made with reference to 22 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 22 the coolant heat exchanger 63 is arranged in 24 cooled by means of the cooling water flow D, whereby thermal energy is extracted from the working fluid and a temperature reduction and condensation of the working fluid is brought about. The cooling water flow D can be discharged into the environment downstream of the coolant heat exchanger 63.

24a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 24 .

To illustrate the method according to the invention in 24a is made with reference to 22a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 22a is used in the process in 24a the heat flow from process step S63b is coupled into process step S63c, in which heat energy is coupled into the cooling water flow D. Instead of using the refrigerant flow E in 22a will be in 24a The cooling capacity, i.e. the heat flow between process steps S63b and S63a, is provided by means of the cooling water flow D. The corresponding process steps S4, S22b, S63c and S11 of the cooling water flow D can be taken from the description above.

25 shows a schematic representation of an arrangement 124 according to the invention for converting energy from an electrode coating system 1 with an intermediate circuit B for direct evaporation and cooling of the working medium and with use of the cooling water flow D and the waste heat of the refrigeration machine 6 in the working medium circuit C.

To illustrate the arrangement 124 according to the invention in 25 is made with reference to 23 Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from 23 the coolant heat exchanger 63 is arranged in 25 cooled by means of a cooling water flow D, whereby thermal energy is extracted from the working fluid and a temperature reduction and condensation of the working fluid is brought about. The cooling water flow D can be discharged into the environment downstream of the coolant heat exchanger 63.

25a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 25 .

To illustrate the method according to the invention in 25a is made with reference to 23a , unless otherwise indicated, analogue Please refer in full to the above description.

Deviating from 23a connects the process in 25a a heat flow connects process step S63b with process step S63c. Thermal energy is therefore coupled into the cooling water flow D in process step S63c. Instead of using the refrigerant flow E in 23a is used in the process in 25a The cooling capacity, i.e. the heat flow between process steps S63b and S63a, is provided by means of the cooling water flow D. The corresponding process steps S4, S22b, S63c and S11 of the cooling water flow D can be taken from the description above.

26 shows a schematic representation of an arrangement 125 according to the invention for converting energy from an electrode coating system 1 with two intermediate circuits (Ba, Bb) for direct evaporation and condensation of the working medium.

For the illustration of the arrangement according to the invention, unless otherwise indicated, reference is made analogously to the above description in its entirety.

The description of the arrangement along the process gas flow A can be derived analogously from the above description, for example from the description of 1 The arrangement in 26 differs from those in 6 until 25 in particular in that the arrangement 115 comprises two intermediate center circles Ba and Bb.

A first intermediate circuit Ba and a second intermediate circuit Bb each connect the process gas stream A to the working fluid circuit C in a heat-conducting manner. The first intermediate circuit Ba is particularly intended to couple at least a portion of the thermal energy extracted from the process gas stream A into the working fluid circuit C for conversion in the heat engine 5. The second intermediate circuit Bb is particularly intended to couple at least a portion of the thermal energy extracted from the working fluid circuit C into the process gas stream A. The main transfer directions of the heat flow between the process gas stream A and the working fluid circuit C are therefore opposite to one another in the two intermediate circuits Ba, Bb. Because the intermediate circuits Ba, Bb are separated from one another, this arrangement makes it possible, in particular, to achieve different operating temperatures for the respective intermediate circuits Ba, Bb. Different intermediate media can therefore advantageously be used in the respective intermediate circuit Ba and Bb. In particular, the first intermediate circuit Ba can be operated at higher temperatures than the second intermediate circuit Bb. For example, an inorganic intermediate agent such as water can be used in the first intermediate circuit Ba, and an organic intermediate agent such as isopentane, isooctane, or silicone oil can be used in the second intermediate circuit Bb. A corresponding intermediate agent can circulate in the respective intermediate circuit Ba or Bb, i.e., a first intermediate agent can circulate in the first intermediate circuit Ba, and a second intermediate agent can circulate in the second intermediate circuit Bb.

The first intermediate medium can be fed into the first cooling device 21 via the intermediate medium inlet 21iii of the process gas condenser 2 to absorb thermal energy and can be discharged from the first cooling device 21 via the intermediate medium outlet 21iv. The first intermediate medium can be supplied to the intermediate medium inlet 9ii of the working medium evaporator 9 by means of the first intermediate medium line B1, in particular for evaporating working medium, wherein the thermal energy extracted from the process gas stream A can be transported to the working medium evaporator 9 with the aid of the first intermediate medium.

The second intermediate medium can be fed into the second intermediate medium heat exchanger 83 via an intermediate medium inlet 83iii of the second intermediate medium heat exchanger 83, designed as a working medium condenser, to absorb thermal energy, whereby the working medium is cooled and condensed. The working medium is introduced into the second intermediate medium heat exchanger 83 via a working medium inlet 83i of the second intermediate medium heat exchanger 83. After the condensation process, the working medium is discharged via a working medium outlet 83ii of the second intermediate medium heat exchanger 83. By means of the third working medium line C3, the working medium can be fed to the working medium inlet 9iii of the working medium evaporator 9, designed as a working medium heating device, for evaporating the working medium.

The intermediate medium can be discharged from the second intermediate medium heat exchanger 83 via an intermediate medium outlet 83iv of the second intermediate medium heat exchanger 83. The second intermediate medium can be supplied to the intermediate medium inlet 24iii of the process gas heating device 24 for supplying intermediate medium via the second intermediate medium line B2, wherein at least part of the thermal energy from the working medium can be transferred to the process gas stream A via the process gas heating device 24. The second intermediate medium can be discharged from the process gas heating device 24 via the intermediate medium outlet 24iv of the process gas heating device 24 and subsequently to the intermediate medium inlet 83iii of the second intermediate heat exchanger 83.

26a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 26 .

To illustrate the method according to the invention in 26a Unless otherwise indicated, reference is made analogously to the above description in full.

The inventive method in 26a differs, for example, from that in 20a in particular by the fact that it comprises process steps along two intermediate circles Ba and Bb.

• S9c: Wärmeenergie wird zur Verdampfung des Arbeitsmittels aus dem ersten Zwischenmittelkreis Ba ausgekoppelt. Die gestrichelte Linie zwischen S9c und S9b stellt den Wärmefluss zwischen beiden Verfahrensschritten dar.
• S21d: Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt auf ein im ersten Zwischenmittelkreis Ba strömendes Zwischenmittel eingekoppelt.

The following process steps are carried out with respect to the first intermediate center circle Ba:

• S9c: Thermal energy is extracted from the first intermediate circuit Ba to evaporate the working fluid. The dashed line between S9c and S9b represents the heat flow between the two process steps.
• S21d: At least part of the thermal energy extracted from the process gas stream A is directly coupled to an intermediate medium flowing in the first intermediate medium circuit Ba.

• S83a: Wärmeenergie wird auf das im zweiten Zwischenmittelkreis Bb befindliche Zwischenmittel übertragen. Die gestrichelte Linie stelle den Wärmefluss dar, mit welchem der Verfahrensschritt S83b mit dem Verfahrensschritt S83a direkt gekoppelt ist.
• S24e: Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt auf ein im zweiten Zwischenmittelkreis Bb strömendes Zwischenmittel eingekoppelt.

The following process steps are carried out with respect to the second intermediate center circle Bb:

• S83a: Thermal energy is transferred to the intermediate medium located in the second intermediate medium circuit Bb. The dashed line represents the heat flow, with which process step S83b is directly coupled to process step S83a.
• S24e: At least part of the thermal energy extracted from the process gas stream A is directly coupled to an intermediate medium flowing in the second intermediate medium circuit Bb.

• S83b: Das Arbeitsmittel wird insbesondere mithilfe des zweiten Zwischenmittelwärmetauschers 83 gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird.

With regard to the working medium circuit C, in particular, in contrast to the procedure in 20 the process step S83b is carried out after the process step S5:

• S83b: The working fluid is cooled and condensed, in particular by means of the second intermediate fluid heat exchanger 83, whereby thermal energy is extracted from the working fluid located in the working fluid circuit C.

27 shows a schematic representation of an arrangement 126 according to the invention for converting energy from an electrode coating system 1 with two intermediate circuits Ba, Bb for direct evaporation and condensation of the working medium and with use of the refrigerant flow E in an intermediate circuit Bb.

To illustrate the arrangement 126 according to the invention in 27 is made with reference to 26 Unless otherwise indicated, reference is made analogously to the above description in full.

The arrangement in 27 differs from that in 26 in particular in that the arrangement 126 further comprises a second coolant heat exchanger 92, which is assigned to the second intermediate circuit Bb. The second coolant heat exchanger 92 is cooled in particular by means of the refrigerant flow E and is intended to transfer at least part of the thermal energy from the second intermediate circuit Bb to the refrigerant flow E. The second coolant heat exchanger 92 can function in a similar manner to the coolant heat exchanger 63, wherein reference is made at this point to the above description of the coolant heat exchanger 63.

27a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 27 .

To illustrate the method according to the invention in 27a is made with reference to 26a Unless otherwise indicated, reference is made analogously to the above description in full.

• S92a: Mindestens ein Teil der aus dem zweiten Zwischenmittelkreis Bb stammenden Wärmeenergie wird in den Kältemittelstrom E eingekoppelt.
• S92e: Das Zwischenmittel wird gekühlt, wobei Wärmeenergie aus dem im zweiten Zwischenmittelkreis Bb befindlichen Zwischenmittel ausgekoppelt wird.

Deviating from the procedure in 26a are used in the process 27a The following procedural steps are carried out:

• S92a: At least part of the heat energy originating from the second intermediate circuit Bb is coupled into the refrigerant flow E.
• S92e: The intermediate medium is cooled, whereby heat energy is extracted from the intermediate medium located in the second intermediate medium circuit Bb.

28 shows a schematic representation of an arrangement 127 according to the invention for converting energy from an electrode coating system 1 with two intermediate circuits Ba, Bb for the direct evaporation and condensation of the working medium and with use of the refrigerant flow E in one intermediate circuit Bb and the waste heat of the refrigeration machine 6 in another intermediate circuit Ba.

To illustrate the arrangement 127 according to the invention in 28 is made with reference to 27 Unless otherwise indicated, reference is made analogously to the above description in full.

The arrangement in 28 differs from that in 27 In particular, the arrangement 127 further comprises a first intermediate medium preheater 93 for heating the intermediate medium circulating in the first intermediate medium circuit Ba. The waste heat from the refrigeration machine 6 is fed to the first intermediate medium preheater 93, in which at least a portion of the waste heat can be coupled into the first intermediate medium circuit Ba. At least a portion of the waste heat from the refrigeration machine 6 can thus be usefully recycled by preheating the first intermediate medium flow Ba therewith before it is fed to the first cooling device 21.

28a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 28 .

To illustrate the method according to the invention in 28a is made with reference to 27a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from the procedure in 27a is used in the process in 28a with respect to the first intermediate center circle Ba, method step S93 is carried out after method step S9c.

S93: At least part of the heat energy extracted from the refrigeration machine 6 is coupled into the first intermediate circuit Ba as refrigeration machine heat flow F.

29 shows a schematic representation of an arrangement 128 according to the invention for converting energy from an electrode coating system 1 with two intermediate circuits Ba, Bb for direct evaporation and condensation of the working medium and with use of the cooling water flow D in an intermediate circuit Bb.

To illustrate the arrangement 128 according to the invention in 29 is made with reference to 26 Unless otherwise indicated, reference is made analogously to the above description in full.

The arrangement in 29 differs from that in 26 in particular in that the arrangement 128 further comprises a second coolant heat exchanger 92, which is assigned to the second intermediate center circuit Bb. The second coolant heat exchanger 92 is cooled in particular by means of the cooling water flow D and is intended to transfer at least part of the thermal energy from the second intermediate center circuit Bb to the cooling water flow D. The second coolant heat exchanger 92 can function in a similar manner to the coolant heat exchanger 63, wherein reference is made at this point to the above description of the coolant heat exchanger 63.

29a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 29 .

To illustrate the method according to the invention in 29a is made with reference to 27a Unless otherwise indicated, reference is made analogously to the above description in full.

• S92c: Mindestens ein Teil der aus dem zweiten Zwischenmittelkreis Bb stammenden Wärmeenergie wird in den Kühlwasserstrom D eingekoppelt.
• S92e: Das Zwischenmittel wird gekühlt, wobei Wärmeenergie aus dem im zweiten Zwischenmittelkreis Bb befindlichen Zwischenmittel ausgekoppelt wird.

Deviating from the procedure in 26a are used in the process 29a The following procedural steps are carried out:

• S92c: At least part of the thermal energy originating from the second intermediate circuit Bb is coupled into the cooling water flow D.
• S92e: The intermediate medium is cooled, whereby heat energy is extracted from the intermediate medium located in the second intermediate medium circuit Bb.

30 shows a schematic representation of an arrangement 129 according to the invention for converting energy from an electrode coating system 1 with two intermediate circuits Ba, Bb for direct evaporation and condensation of the working medium and with use of the cooling water flow D in one intermediate circuit Bb and the waste heat of the refrigeration machine 6 in another intermediate circuit Ba.

To illustrate the arrangement 129 according to the invention in 30 is made with reference to 29 Unless otherwise indicated, reference is made analogously to the above description in full.

The arrangement in 30 differs from that in 29 in particular in that the arrangement 129 further comprises the first intermediate medium preheater 93 for heating the intermediate medium circulating in the first intermediate medium circuit Ba. The waste heat of the refrigeration machine 6 is guided to the first intermediate medium preheater 93, in which at least a portion of the waste heat can be coupled into the first intermediate medium circuit Ba. At least a portion of the waste heat of the refrigeration machine 6 can thus be used for recycling by first intermediate medium stream Ba is preheated therewith before it is led to the first cooling device 21.

30a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 30 .

To illustrate the method according to the invention in 30a is made with reference to 29a Unless otherwise indicated, reference is made analogously to the above description in full.

Deviating from the procedure in 29a is used in the process in 30a with respect to the first intermediate center circle Ba, method step S93 is carried out after method step S9c.

S93: At least part of the heat energy extracted from the refrigeration machine 6 is coupled into the first intermediate circuit Ba as refrigeration machine heat flow F.

31 shows a schematic representation of an arrangement 130 according to the invention for converting energy from an electrode coating system 1 with two intermediate circuits Ba, Bb for direct evaporation and condensation of the working medium and with use of the waste heat of the refrigeration machine 6 in an intermediate circuit Ba.

To illustrate the arrangement 130 according to the invention in 31 is made with reference to 26 Unless otherwise indicated, reference is made analogously to the above description in full.

The arrangement in 31 differs from that in 26 in particular in that the arrangement 130 further comprises the first intermediate medium preheater 93 for heating the intermediate medium circulating in the first intermediate medium circuit Ba. The waste heat from the refrigeration machine 6 is fed to the first intermediate medium preheater 93, in which at least a portion of the waste heat can be coupled into the first intermediate medium circuit Ba. At least a portion of the waste heat from the refrigeration machine 6 can thus be usefully recycled by preheating the first intermediate medium flow Ba therewith before it is fed to the first cooling device 21.

31a shows a schematic representation of a method according to the invention, preferably for implementation in an arrangement according to 31 .

To illustrate the method according to the invention in 31a is made with reference to 26a Unless otherwise indicated, reference is made analogously to the above description in its entirety. 26a Deviating procedural steps correspond to those in 30a illustrated process steps with respect to the first intermediate center circle Ba. Reference is made to the above description.

List of reference symbols

A

Prozessgasstrom

B

Zwischenmittelkreis

Ba

erster Zwischenmittelkreis

Bb

zweiter Zwischenmittelkreis

B1

erste Zwischenmittelleitung

B2

zweite Zwischenmittelleitung

B3

dritte Zwischenmittelleitung

C

Arbeitsmittelkreis

C1

erste Arbeitsmittelleitung

C2

zweite Arbeitsmittelleitung

C3

dritte Arbeitsmittelleitung

D

Kühlwasserstrom

E

Kältemittelstrom

F

Wärmefluss aus der Kältemaschine

1

Elektrodenbeschichtungsanlage

1a

Elektrodenbeschichtungsprozess

2

Prozessgaskondensator

3

Gebläse

5

Wärmekraftmaschine

5i

Einlass der Wärmekraftmaschine

5ii

Auslass der Wärmekraftmaschine

6

Kältemaschine

7

Arbeitsmittelpumpe

8

Luftwärmetauscher

9

Arbeitsmittelverdampfer

9i

Zwischenmitteleinlass des Arbeitsmittelverdampfers

9ii

Zwischenmittelauslass des Arbeitsmittelverdampfers

9iii

Arbeitsmitteleinlass des Arbeitsmittelverdampfers

9iv

Arbeitsmittelauslass des Arbeitsmittelverdampfers

21

erster Kühlapparat

21i

Arbeitsmitteleinlass des Prozessgaskondensators

21ii

Arbeitsmittelauslass des Prozessgaskondensators

21iii

Zwischenmitteleinlass des Prozessgaskondensators

21iv

Zwischenmittelauslass des Prozessgaskondensators

22

zweiter Kühlapparat

23

dritter Kühlapparat

24

Prozessgasheizvorrichtung

24i

Arbeitsmitteleinlass der Prozessgasheizvorrichtung

24ii

Arbeitsmittelauslass der Prozessgasheizvorrichtung

24iii

Zwischenmitteleinlass der Prozessgasheizvorrichtung

24iv

Zwischenmittelauslass der Prozessgasheizvorrichtung

25

Prozessgaseinlass

26

Prozessgasauslass

51

Generator

53

Stromnetz

63

Kühlmittelwärmetauscher

64

Zwischenmittel-Vorheizer

66

Arbeitsmittel-Vorheizer

68

Zwischenmittelwärmetauscher

69

Arbeitsmittelvorkühler

68iii

Arbeitsmitteleinlass des Zwischenmittelwärmetauschers

68iv

Arbeitsmittelauslass des Zwischenmittelwärmetauschers 68

71

Zwischenmittelpumpe

81

Arbeitsmittelkühler

82

Luftkühler

83

zweiter Zwischenmittelwärmetauscher

83i

Arbeitsmitteleinlass des zweiten Zwischenmittelwärmetauschers

83ii

Arbeitsmittelauslass des zweiten Zwischenmittelwärmetauschers

83iii

Zwischenmitteleinlass des zweiten Zwischenmittelwärmetauschers

83iv

Zwischenmittelauslass des zweiten Zwischenmittelwärmetauschers

92

zweiter Kühlmittelwärmetauscher

93

erster Zwischenmittel-Vorheizer

100 - 130

Anordnungen zur Umwandlung von Energie aus einem Industrieprozess

Verfahrensschritte

S1

Elektrodenbeschichtungsprozess

S2

Kondensationsschritt

S4

Kühlwasser wird zu einer zweiten Kühlstufe geführt.

S5

Umwandlung von Wärmeenergie in mechanische Energie

S6

Der Kältemittelstrom wird gekühlt

S8

Wärmeenergie wird aus dem Arbeitsmittel ausgekoppelt und in eine Umgebung abgeführt

S9a

Wärmeenergie wird zur Verdampfung des Arbeitsmittels aus dem Zwischenmittelkreis B ausgekoppelt.

S9b

Wärmeenergie wird zur Verdampfung des Arbeitsmittels in den Arbeitsmittelkreis C eingekoppelt.

S9c

Wärmeenergie wird zur Verdampfung des Arbeitsmittels aus dem ersten Zwischenmittelkreis Ba ausgekoppelt.

S11

Kühlwasser wird in eine Umgebung geführt

S21a

Wärmeenergie wird in einer ersten Kühlstufe S21a aus dem Prozessgasstrom A ausgekoppelt.

S21b

Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt in den Arbeitsmittelkreis C eingekoppelt. Das im Arbeitsmittelkreis C befindliche Arbeitsmittel wird erhitzt und verdampft.

S21c

Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt in den Zwischenmittelkreis B eingekoppelt.

S21d

Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt auf ein im ersten Zwischenmittelkreis Ba strömendes Zwischenmittel eingekoppelt.

S22a

Das Prozessgas wird in einer zweiten Kühlstufe abgekühlt. Wärmeenergie wird aus dem Prozessgasstrom A ausgekoppelt.

S22b

Wärmeenergie wird in den Kühlwasserstrom D eingekoppelt.

S23a

Das Prozessgas wird in einer dritten Kühlstufe abgekühlt. Wärmeenergie wird aus dem Prozessgasstrom A ausgekoppelt.

S23b

Wärmeenergie wird in den Kältemittelstrom E eingekoppelt.

S24a

Das Prozessgas wird aufgeheizt. Wärmeenergie wird in den Prozessgasstrom A eingekoppelt.

S24b

Das Arbeitsmittel wird gekühlt und dabei mindestens ein Teil der im Arbeitsmittel aufweisenden Wärmeenergie ausgekoppelt. Das Arbeitsmittel wird beim Kühlvorgang kondensiert.

S24c

Das Arbeitsmittel wird gekühlt und dabei mindestens ein Teil der im Arbeitsmittel aufweisenden Wärmeenergie ausgekoppelt.

S24d

Wärmeenergie wird zum Aufheizen des Prozessgasstroms A aus dem Zwischenmittelkreis B ausgekoppelt.

S24e

Mindestens ein Teil der aus dem Prozessgasstrom A ausgekoppelte Wärmeenergie wird direkt auf ein im zweiten Zwischenmittelkreis Bb strömendes Zwischenmittel eingekoppelt.

S51

Umwandlung von mechanischer Energie in elektrische Energie

S53

Abführen elektrischer Energie aus der Anordnung

S63a

Wärmeenergie wird in den Kältemittelstrom E eingekoppelt.

S63b

Das Arbeitsmittel wird gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird.

S63c

Wärmeenergie wird in den Kühlwasserstrom D eingekoppelt.

S63e

Das Zwischenmittel wird gekühlt, wobei Wärmeenergie aus dem im Zwischenmittelkreis B befindlichen Zwischenmittel ausgekoppelt wird.

S64

Wärmeenergie wird als Kältemaschine-Wärmefluss F in den Zwischenmittelkreis B eingekoppelt.

S66

Wärmeenergie wird als Kältemaschine-Wärmefluss F in den Arbeitsmittelkreis C eingekoppelt.

S68a

Wärmeenergie wird mithilfe des Zwischenmittelwärmetauschers 68 in das Zwischenmittel eingekoppelt.

S68b

Wärmeenergie wird mithilfe des Zwischenmittelwärmetauschers 68 aus dem Arbeitsmittel ausgekoppelt.

S69a

Wärmeenergie wird mithilfe des Arbeitsmittelvorkühlers 69 in das Zwischenmittel eingekoppelt.

S69b

Wärmeenergie wird mithilfe des Arbeitsmittelvorkühlers 69 aus dem Arbeitsmittel ausgekoppelt.

S81

Kühlen des Arbeitsmittels

S83a

Wärmeenergie wird auf das im zweiten Zwischenmittelkreis Bb befindliche Zwischenmittel übertragen.

S83b

Das Arbeitsmittel wird insbesondere mithilfe des zweiten Zwischenmittelwärmetauschers 83 gekühlt und kondensiert, wobei Wärmeenergie aus dem im Arbeitsmittelkreis C befindlichen Arbeitsmittel ausgekoppelt wird.

S92a

Mindestens ein Teil der aus dem zweiten Zwischenmittelkreis Bb stammenden Wärmeenergie wird in den Kältemittelstrom E eingekoppelt.

S92c

Mindestens ein Teil der aus dem zweiten Zwischenmittelkreis Bb stammenden Wärmeenergie wird in den Kühlwasserstrom D eingekoppelt.

S92e

Das Zwischenmittel wird gekühlt, wobei Wärmeenergie aus dem im zweiten Zwischenmittelkreis Bb befindlichen Zwischenmittel ausgekoppelt wird.

S93

Wärmeenergie wird als Kältemaschine-Wärmefluss F in den ersten Zwischenmittelkreis Ba eingekoppelt.

A

Process gas flow

B

Intermediate circle

Ba

first intermediate circle

Bb

second intermediate center circle

B1

first intermediate line

B2

second intermediate line

B3

third intermediate line

C

Work equipment circuit

C1

first work equipment line

C2

second work equipment line

C3

third work equipment line

D

Cooling water flow

E

Refrigerant flow

F

Heat flow from the chiller

1

Electrode coating system

1a

Electrode coating process

2

Process gas condenser

3

fan

5

heat engine

5i

Inlet of the heat engine

5ii

Outlet of the heat engine

6

refrigeration machine

7

Working fluid pump

8

Air heat exchanger

9

Working fluid evaporator

9i

Intermediate medium inlet of the working medium evaporator

9ii

Intermediate medium outlet of the working medium evaporator

9iii

Working fluid inlet of the working fluid evaporator

9iv

Working fluid outlet of the working fluid evaporator

21

first cooling device

21i

Working fluid inlet of the process gas condenser

21ii

Working fluid outlet of the process gas condenser

21iii

Intermediate inlet of the process gas condenser

21iv

Intermediate outlet of the process gas condenser

22

second cooling device

23

third cooling device

24

Process gas heating device

24i

Working fluid inlet of the process gas heating device

24ii

Working fluid outlet of the process gas heating device

24iii

Intermediate inlet of the process gas heater

24iv

Intermediate outlet of the process gas heating device

25

Process gas inlet

26

Process gas outlet

51

generator

53

power grid

63

Coolant heat exchanger

64

Intermediate preheater

66

Work equipment preheater

68

Intermediate heat exchanger

69

Working fluid pre-cooler

68iii

Working fluid inlet of the intermediate heat exchanger

68iv

Working fluid outlet of the intermediate heat exchanger 68

71

Intermediate pump

81

Working fluid cooler

82

air cooler

83

second intermediate heat exchanger

83i

Working fluid inlet of the second intermediate heat exchanger

83ii

Working fluid outlet of the second intermediate heat exchanger

83iii

Intermediate medium inlet of the second intermediate medium heat exchanger

83iv

Intermediate medium outlet of the second intermediary heat exchanger

92

second coolant heat exchanger

93

first intermediate preheater

100 - 130

Arrangements for converting energy from an industrial process

Procedural steps

S1

Electrode coating process

S2

Condensation step

S4

Cooling water is fed to a second cooling stage.

S5

Conversion of thermal energy into mechanical energy

S6

The refrigerant flow is cooled

S8

Heat energy is extracted from the working medium and dissipated into the environment

S9a

Thermal energy is extracted from the intermediate circuit B to evaporate the working fluid.

S9b

Thermal energy is coupled into the working fluid circuit C to evaporate the working fluid.

S9c

Thermal energy is extracted from the first intermediate circuit Ba to evaporate the working fluid.

S11

Cooling water is fed into an environment

S21a

Thermal energy is extracted from the process gas stream A in a first cooling stage S21a.

S21b

At least part of the thermal energy extracted from the process gas stream A is directly coupled into the working fluid circuit C. The working fluid in the working fluid circuit C is heated and evaporated.

S21c

At least part of the heat energy extracted from the process gas stream A is directly coupled into the intermediate circuit B.

S21d

At least part of the thermal energy extracted from the process gas stream A is directly coupled to an intermediate medium flowing in the first intermediate medium circuit Ba.

S22a

The process gas is cooled in a second cooling stage. Thermal energy is extracted from process gas stream A.

S22b

Thermal energy is coupled into the cooling water flow D.

S23a

The process gas is cooled in a third cooling stage. Thermal energy is extracted from process gas stream A.

S23b

Thermal energy is coupled into the refrigerant flow E.

S24a

The process gas is heated. Thermal energy is coupled into process gas stream A.

S24b

The working fluid is cooled, and at least a portion of the thermal energy contained in the working fluid is extracted. The working fluid is condensed during the cooling process.

S24c

The working fluid is cooled and at least part of the thermal energy contained in the working fluid is extracted.

S24d

Thermal energy is extracted from the intermediate circuit B to heat the process gas stream A.

S24e

At least part of the thermal energy extracted from the process gas stream A is directly coupled to an intermediate medium flowing in the second intermediate medium circuit Bb.

S51

Conversion of mechanical energy into electrical energy

S53

Dissipation of electrical energy from the arrangement

S63a

Thermal energy is coupled into the refrigerant flow E.

S63b

The working fluid is cooled and condensed, whereby heat energy is extracted from the working fluid in the working fluid circuit C.

S63c

Thermal energy is coupled into the cooling water flow D.

S63e

The intermediate medium is cooled, whereby heat energy is extracted from the intermediate medium located in the intermediate medium circuit B.

S64

Thermal energy is coupled into the intermediate circuit B as a refrigeration machine heat flow F.

S66

Thermal energy is coupled into the working fluid circuit C as a refrigeration machine heat flow F.

S68a

Thermal energy is coupled into the intermediate medium using the intermediate medium heat exchanger 68.

S68b

Thermal energy is extracted from the working fluid using the intermediate heat exchanger 68.

S69a

Thermal energy is coupled into the intermediate medium using the working medium pre-cooler 69.

S69b

Thermal energy is extracted from the working fluid using the working fluid pre-cooler 69.

S81

Cooling the working fluid

S83a

Heat energy is transferred to the intermediate medium located in the second intermediate medium circuit Bb.

S83b

The working fluid is cooled and condensed in particular by means of the second intermediate fluid heat exchanger 83, whereby thermal energy is extracted from the working fluid located in the working fluid circuit C.

S92a

At least part of the heat energy originating from the second intermediate circuit Bb is coupled into the refrigerant flow E.

S92c

At least part of the thermal energy originating from the second intermediate circuit Bb is coupled into the cooling water flow D.

S92e

The intermediate medium is cooled, whereby heat energy is extracted from the intermediate medium located in the second intermediate medium circuit Bb.

S93

Thermal energy is coupled into the first intermediate circuit Ba as a refrigeration machine heat flow F.

QUOTES CONTAINED IN THE DESCRIPTION

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Cited patent literature

• CA 2214542A1 [0005]

Claims (17)

An arrangement (100-130) for converting energy from a process gas stream (A) originating from an industrial plant (1), comprising: - a process gas cooling device, in particular a process gas condenser (2), with which process gas cooling device or process gas condenser (2) at least a portion of the process gas stream (A) can be cooled or condensed, wherein thermal energy can be extracted from the process gas stream (A); - a working fluid circuit (C) for transporting at least a portion of the thermal energy extracted from the process gas stream (A), which can be injected into a working fluid; - a heat engine (5) arranged in the working fluid circuit (C), with which at least a portion of the thermal energy injected into the working fluid can be converted into mechanical energy. Arrangement (100-130) according to Claim 1 with a working medium condenser arranged in the working medium circuit (C) downstream of the heat engine, by means of which the working medium can be condensed, whereby heat energy can be extracted from the working medium. Arrangement (100-130) according to one of the preceding claims, wherein a process gas heating device (24) for heating at least a portion of the process gas stream (A) is arranged downstream of the process gas cooling device, in particular the process gas condenser (2), by means of which process gas heating device (24) thermal energy can be coupled into the process gas stream (A). Arrangement (100-130) according to one of the preceding claims, wherein the working fluid circuit (C) comprises: - a first working fluid line (C1) to the heat engine (A), by means of which the working fluid can be fed to an inlet of the heat engine; - a second working fluid line (C2), by means of which the working fluid can be discharged from an outlet of the heat engine (5); - a third working fluid line (C3), by means of which the working fluid can be fed to a working fluid inlet (9iii, 21i) of a working fluid heating device (9, 21, 66), in particular for evaporating the working fluid. Arrangement (100-130) according to one of the preceding claims, comprising a working fluid evaporator (9) for evaporating working fluid, wherein thermal energy can be transferred from an intermediate medium to the working fluid using the working fluid evaporator (9); at least one intermediate medium circuit (B, Ba, Bb) comprising: - a first intermediate medium line (B1) to the working medium evaporator (9), by means of which first intermediate medium line (B1) an intermediate medium can be fed to an intermediate medium inlet (9ii) of the working medium evaporator (9) for supplying intermediate medium, wherein the thermal energy extracted from the process gas stream (A) can be transported to the working medium evaporator (9) with the aid of the intermediate medium, and/or - a second intermediate medium line (B2) to the process gas heating device (24), by means of which second intermediate medium line (B2) an intermediate medium can be fed to an intermediate medium inlet (24iii) of the process gas heating device (24) for supplying intermediate medium, wherein at least part of the thermal energy from the intermediate medium can be transferred to the process gas stream (A) via the process gas heating device (24). Arrangement (100-130) according to one of the preceding claims, wherein the process gas cooling device, in particular the process gas condenser (2), has at least two cooling devices (21, 22, 23) arranged one behind the other for cooling at least a portion of the process gas flow, each of which is intended for a cooling stage, wherein - a front cooling device (21) is intended to transfer at least a portion of the thermal energy from the process gas flow to the working fluid for expansion in the heat engine and thereby cool at least a portion of the process gas flow; - a rear cooling device (22, 23) arranged downstream of the front cooling device (21) is intended to transfer at least part of the thermal energy from the process gas flow (A) to a coolant flow (D, E) and in the process to cool, in particular to condense, at least part of the process gas flow (A), wherein the coolant flow (D, E) is further intended to absorb thermal energy at a point (63, 92) in an intermediate circuit (B, Ba, Bb) and/or in the working medium circuit (C). Arrangement (100-130) according to Claim 6 with a refrigeration machine (6) for cooling the coolant flow (D, E), wherein at least a part of the thermal energy, in particular that which is coupled from the coolant flow (D, E) into the refrigeration machine (6), can be coupled out of the refrigeration machine (6) for coupling into the process gas flow (A) and/or into an intermediate circuit (B, Ba, Bb) and/or into the working medium circuit (C). Arrangement (100-130) according to Claim 6 or 7 , wherein the process gas cooling device, in particular the process gas condenser (2): - has three cooling devices (21, 22, 23) arranged one behind the other for cooling at least a portion of the process gas stream (A), wherein ◯ the first cooling device (21) can be flowed through by an intermediate medium located in an intermediate medium circuit (B), wherein the thermal energy originating from at least a portion of the process gas stream (A) can be transferred to the intermediate medium for re-coupling into the process gas stream (A), ◯ the second cooling device (22) can be flowed through by a first coolant, in particular a cooling water (D), wherein thermal energy from the process gas stream (A) can be transferred to the first coolant, ◯ the third cooling device (23) can be flowed through by a second cooled coolant, in particular a refrigerant (E), which is cooled by means of a refrigeration machine (6), wherein thermal energy from the process gas stream (A) can be transferred to the second coolant, in which arrangement (100-130) - which is arranged in an intermediate medium circuit (B, Ba) located intermediate means can flow through a working medium evaporator (9) for evaporating the working medium, wherein at least part of the thermal energy in the working medium can be converted into electrical energy via the heat engine (5) and the generator (51), - a process gas heating device (24) arranged downstream of the process gas cooling device, in particular of the process gas condenser (2), can be flowed through by the intermediate means located in an intermediate means circuit (B, Bb), wherein thermal energy can be coupled into the process gas stream (A). Arrangement (100-130) according to one of the preceding claims with a generator (51) which can be coupled or is coupled to the heat engine (5) for generating electrical energy. Method for converting energy from a process gas stream (A) originating from an industrial process (S1), in which method at least a portion of the process gas stream (A) is exposed to or subjected to a cooling step, in particular a condensation step (S2), wherein at least a portion of the thermal energy from the process gas stream (A) is transferred to a working medium for conversion in a heat engine (5) which is arranged in a working medium circuit (C). Procedure according to Claim 10 , in which process the working medium is condensed downstream of the conversion in the heat engine (5), whereby heat energy is extracted from the working medium. Method according to one of the preceding claims, in which thermal energy from the working medium is transferred to the process gas during a heating process of the process gas stream (A). Method according to one of the preceding claims, comprising at least one intermediate medium circuit (B, Ba, Bb) which can be coupled to the process gas stream (A) and/or to the working medium circuit (C) in a heat-conducting or heat-transferring manner, in which the following method steps are carried out: a. During cooling of the process gas stream (A), thermal energy is transferred directly to an intermediate medium located in the intermediate medium circuit (B, Ba, Bb), flowing or circulating; b. At least a portion of the thermal energy transferred from the process gas to the intermediate medium is transferred directly to the working medium located in the working medium circuit (C) upstream of the conversion in the heat engine (5), whereby the working medium is evaporated; c. The evaporated working medium is fed to the heat engine (5). A method according to any one of the preceding claims, in which the following method steps are carried out: a. During cooling of the process gas stream (A), thermal energy is transferred directly to a working fluid, whereby the working fluid is vaporized; b. The vaporized working fluid is fed to the heat engine (5); c. During heating of the process gas stream (A), thermal energy is transferred directly to the process gas, whereby the working fluid is condensed in the working fluid circuit (C) downstream of the heat engine (5) during the heat transfer to the process gas (A). Method according to one of the preceding claims, wherein the cooling step, in particular the condensation step (S2) of the process gas stream (A), comprises at least two consecutive cooling stages (S21a, S22a, S23a), in which method the following method steps are carried out: a. Thermal energy from the process gas stream (A) is transferred to a working medium in a front cooling stage (S21a); b. In a rear cooling stage (S22a, S23a) arranged downstream of the front cooling stage (S21a), thermal energy from the process gas stream (A) is transferred to a coolant located in a coolant stream (D, E); c. Thermal energy from the working medium is transferred to the coolant located in a coolant stream (D, E) at a point in the working medium circuit (C) downstream of the conversion in the heat engine (5). Procedure according to Claim 15 , in which the following method steps are carried out: a. a coolant is cooled in a coolant flow (D, E) with the aid of a refrigeration machine (6), wherein thermal energy is extracted from the coolant into the refrigeration machine (6); b. the coolant is guided to the rear cooling stage (S22a, S23a) of the process gas flow (A); c. downstream of the rear cooling stage (S22a, S23a) of the process gas flow (A), thermal energy from the working fluid is absorbed by the coolant in the coolant flow (D, E), wherein the working fluid in the working fluid circuit (C) is cooled and condensed, and/or d. in the working fluid circuit (C), the thermal energy previously extracted into the refrigeration machine (6) is transferred to an intermediate medium or to the working fluid for coupling into the process gas flow (A) and/or for coupling into the working fluid circuit (C). Use of the arrangement (100-130) according to one of the Claims 1 until 9 or the procedure under one of the Claims 10 until 16 for converting energy from a process gas stream (A), in particular from a circulating or recirculating air of a dryer for treating process gas of a dryer, in particular from the process gas of a production plant (1) for producing electrodes of a battery and/or a device for separating or recovering at least one solvent from the process gas of a production plant (1).

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