US20100242476A1 - Combined heat and power cycle system - Google Patents
Combined heat and power cycle system Download PDFInfo
- Publication number
- US20100242476A1 US20100242476A1 US12/413,920 US41392009A US2010242476A1 US 20100242476 A1 US20100242476 A1 US 20100242476A1 US 41392009 A US41392009 A US 41392009A US 2010242476 A1 US2010242476 A1 US 2010242476A1
- Authority
- US
- United States
- Prior art keywords
- heat
- cycle system
- rankine cycle
- working fluid
- combined
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 239000012530 fluid Substances 0.000 claims abstract description 150
- 238000001704 evaporation Methods 0.000 claims abstract description 11
- 230000008020 evaporation Effects 0.000 claims abstract description 11
- 238000009833 condensation Methods 0.000 claims abstract description 9
- 230000005494 condensation Effects 0.000 claims abstract description 9
- 230000020169 heat generation Effects 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 46
- 238000010438 heat treatment Methods 0.000 claims description 20
- 238000011144 upstream manufacturing Methods 0.000 claims description 7
- 238000002485 combustion reaction Methods 0.000 claims description 6
- 239000003518 caustics Substances 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 238000007710 freezing Methods 0.000 claims description 5
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 claims description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 4
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Thiophene Chemical compound C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 claims description 4
- NVSXSBBVEDNGPY-UHFFFAOYSA-N 1,1,1,2,2-pentafluorobutane Chemical compound CCC(F)(F)C(F)(F)F NVSXSBBVEDNGPY-UHFFFAOYSA-N 0.000 claims description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims description 2
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 2
- 239000001273 butane Substances 0.000 claims description 2
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 claims description 2
- 150000002576 ketones Chemical class 0.000 claims description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 2
- MSSNHSVIGIHOJA-UHFFFAOYSA-N pentafluoropropane Chemical compound FC(F)CC(F)(F)F MSSNHSVIGIHOJA-UHFFFAOYSA-N 0.000 claims description 2
- 229940029560 pentafluoropropane Drugs 0.000 claims description 2
- 229920000570 polyether Polymers 0.000 claims description 2
- 239000001294 propane Substances 0.000 claims description 2
- 229930192474 thiophene Natural products 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 40
- 239000002918 waste heat Substances 0.000 description 13
- 239000000498 cooling water Substances 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 230000005611 electricity Effects 0.000 description 6
- 238000009835 boiling Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000004913 activation Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- -1 ground Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- UORDCDHQRUPPNS-UHFFFAOYSA-N butane;cyclohexane Chemical compound CCCC.C1CCCCC1 UORDCDHQRUPPNS-UHFFFAOYSA-N 0.000 description 1
- ONCPMOQOESCOER-UHFFFAOYSA-N butane;cyclopentane Chemical compound CCCC.C1CCCC1 ONCPMOQOESCOER-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010960 commercial process Methods 0.000 description 1
- CTKNKEYOQPJVFK-UHFFFAOYSA-N cyclohexane;propane Chemical compound CCC.C1CCCCC1 CTKNKEYOQPJVFK-UHFFFAOYSA-N 0.000 description 1
- VGRPDNJRRQMEKA-UHFFFAOYSA-N cyclopentane;1,1,1,2,2-pentafluoropropane Chemical compound C1CCCC1.CC(F)(F)C(F)(F)F VGRPDNJRRQMEKA-UHFFFAOYSA-N 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000010773 plant oil Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/04—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled condensation heat from one cycle heating the fluid in another cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/065—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle the combustion taking place in an internal combustion piston engine, e.g. a diesel engine
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
Definitions
- the embodiments disclosed herein relate generally to the field of a combined heat and power cycle system and, more particularly, to a combined heat and power cycle system for recovering waste heat from a plurality of heat sources having different temperatures for heating purpose and generation of electricity.
- Enormous amounts of waste heat are generated by a wide variety of industrial and commercial processes and operations.
- Example sources of waste heat include heat from space heating assemblies, steam boilers, engines, and cooling systems.
- waste heat is low grade, such as waste heat having a temperature of heat below 840 degrees Fahrenheit, for example, conventional heat recovery systems do not operate with sufficient efficiency to make recovery of energy cost-effective. The net result is that vast quantities of waste heat are simply dumped into the atmosphere, ground, or water.
- Some power generation systems provide better reliability and off-grid operation with alternate fuels such as biogas or landfill gas, with examples being gas turbines and combustion engines such as microturbines and reciprocating engines.
- Combustion engines may be used to generate electricity using fuels such as gasoline, natural gas, biogas, plant oil, and diesel fuel.
- fuels such as gasoline, natural gas, biogas, plant oil, and diesel fuel.
- atmospheric emissions such as nitrogen oxides and particulates may be emitted.
- a fundamental rankine cycle typically includes a turbo generator, an evaporator/boiler, a condenser, and a liquid pump.
- a fundamental rankine cycle typically includes a turbo generator, an evaporator/boiler, a condenser, and a liquid pump.
- single cycle system or two-cycle systems are used in heat recovery applications with waste heat sources of different temperature levels.
- Single-cycle configurations collect heat from the different waste heat locations in a serial arrangement of heat exchangers with an intermediate heating fluid.
- the hot heat source heats a high-boiling point liquid in a top loop
- the cold heat source heats a low-boiling point liquid in a separate bottom loop.
- a cascaded organic rankine cycle system for utilization of waste heat includes a pair of organic rankine cycle systems. The cycles are combined, and the respective organic working fluids are chosen such that the organic working fluid of the first organic rankine cycle is condensed at a condensation temperature that is above the boiling point of the organic working fluid of the second organic cycle.
- a combined heat and power cycle system including at least two integrated rankine cycle systems.
- the combined heat and power cycle system includes a heat generation system comprising at least two separate heat sources having different temperatures.
- the combined heat and power cycle system includes a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid.
- the first rankine system is configured to remove heat from the first heat source.
- a second rankine cycle system is coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid.
- the at least one second heat source includes a lower temperature heat source than the first heat source.
- the second rankine cycle system is configured to remove heat from the at least one second heat source.
- the first and second working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system.
- At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof.
- the first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
- a combined heat and power cycle system including at least two integrated organic rankine cycle system.
- the combined heat and power cycle system includes a combustion engine having an engine exhaust unit; and at least another heat source selected from a group comprising an oil heat exchanger, engine jacket, water jacket heat exchanger, lower temperature intercooler, higher temperature intercooler, or combinations thereof.
- the combined heat and power cycle system includes a first organic rankine cycle system coupled to the engine exhaust unit and configured to circulate a first organic working fluid.
- a second organic rankine cycle system is coupled to at least one other heat source selected from the group comprising the oil heat exchanger, engine jacket, water jacket heat exchanger, lower temperature intercooler, higher temperature intercooler, or combinations thereof, and configured to circulate a second organic working fluid.
- the one heat source includes a lower temperature heat source than at least one other heat source.
- the second organic rankine cycle system is configured to remove heat from the at least one other heat source.
- the first and second organic working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first organic working fluid in the first organic rankine cycle system and evaporation of the second organic working fluid in the second organic rankine cycle system.
- At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof.
- the first working fluid, second working fluid, or combinations thereof, are circulatable in heat exchange relationship with the third fluid through the at least one heat exchanger for heating the the third fluid.
- a combined heat and power cycle system including at least two integrated rankine cycle systems.
- the combined heat and power cycle system includes a heat generation system comprising at least two separate heat sources having different temperatures.
- the combined heat and power cycle system includes a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid.
- the first rankine system is configured to remove heat from the first heat source.
- a second rankine cycle system is coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid.
- the at least one second heat source includes a lower temperature heat source than the first heat source.
- the second rankine cycle system is configured to remove heat from the at least one second heat source.
- the first and second working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system.
- the second rankine cycle is configured to partially evaporate the second working fluid before entering the cascaded heat exchange unit.
- At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof.
- the first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
- FIG. 1 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with an exemplary embodiment disclosed herein;
- FIG. 2 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with another exemplary embodiment disclosed herein;
- FIG. 3 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with yet another exemplary embodiment disclosed herein;
- FIG. 4 is a diagrammatical representation of a bottom cycle of a combined heat and power cycle system in accordance with an exemplary embodiment disclosed herein;
- FIG. 5 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with yet another exemplary embodiment disclosed herein;
- FIG. 6 is a diagrammatical representation of a bottom cycle of a combined heat and power cycle system in accordance with an exemplary embodiment disclosed herein;
- FIG. 7 is a diagrammatical representation of a bottom cycle of a combined heat and power cycle system in accordance with an exemplary embodiment disclosed herein.
- embodiments of the present invention provide a combined heat and power cycle system having at least two integrated rankine cycle systems coupled to at least two separate heat sources respectively having different temperatures.
- the first rankine cycle system is coupled to a first heat source and configured to circulate a first working fluid.
- the second rankine cycle system is coupled to at least one second heat source and configured to circulate a second working fluid.
- the second heat source includes a lower temperature heat source than the first heat source.
- the combined heat and power cycle system also includes a cascaded heat exchange unit.
- the first and second working fluids are circulated in heat exchange relationship for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system.
- the combined heat and power cycle system includes one or more heat exchangers disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof for heating a third fluid to be used for a particular locality.
- the third fluid comprises water, water mixed with anti-corrosive agent, or water mixed with anti-freezing agent.
- the definition of the term “or” for the purpose of the following discussion and the appended claims is intended to be an inclusive “or.” That is, the term “or” is not intended to differentiate between two mutually exclusive alternatives. Rather, the term “or” when employed as a conjunction between two elements is defined as including one element by itself, the other element itself, and combinations and permutations of the elements.
- a discussion or recitation employing the terminology “A” or “B” includes: “A” by itself, “B” by itself, and any combination thereof, such as “AB” and “BA.”
- the present discussion relates to exemplary embodiments, and the appended claims should not be limited to the embodiments discussed.
- the illustrated combined heat and power cycle system 10 includes a first organic rankine cycle system 12 (top cycle) and a second organic rankine cycle system 14 (bottom cycle).
- a first organic working fluid is circulated through the first organic rankine cycle system 12 .
- the first organic working fluid may include cyclohexane, cyclopentane, thiophene, ketones, aromatics, or combinations thereof.
- the first organic rankine cycle system 12 includes an evaporator 16 coupled to a first heat source 18 , for example an exhaust unit of a heat generation system 19 (for example, an engine).
- the temperature of the exhaust unit of the engine may be in the temperature range of 400 to 500 degrees Celsius.
- the evaporator 16 receives heat from the exhaust gas generated from the first heat source 18 and generates a first organic working fluid vapor.
- the first organic working fluid vapor is passed through a first expander 20 to drive a first generator unit 22 .
- the first organic working fluid vapor at a relatively lower pressure and lower temperature is passed through the cascaded heat exchange unit 24 .
- the first organic working fluid vapor is condensed into a liquid, which is then pumped via a pump 26 to the evaporator 16 . The cycle may then be repeated.
- the binary fluid may include cyclohexane-propane, cyclohexane-butane, cyclopentane-butane, or cyclopentane-pentafluoropropane, for example.
- Cascaded heat exchange unit 24 may be coupled to any one or more of a plurality of second heat sources such as an intercooler 28 , an oil heat exchanger 30 , and a cooling water jacket heat exchanger 32 being coupled either in series or parallel. Such second heat sources are also typically coupled to the engine. It should be noted herein that the second heat source includes a lower temperature heat source than the first heat source.
- first and second heat sources may include other multiple low-grade heat sources such as gas turbines with intercoolers.
- the cascaded heat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor.
- the second organic working fluid vapor is passed through a second expander 34 to drive a second generator unit 36 .
- the first expander 20 and the second expander 34 are coupled to a single generator unit.
- neither of the first and second organic working fluids are expanded below the atmospheric pressure, and the boiling point temperature of the first organic working fluid is below the average temperature of the second heat source.
- the second organic working fluid vapor at lower pressure and lower temperature is passed through a condenser 38 .
- the second organic working fluid vapor is condensed into a liquid, which is then pumped via a pump 40 to the second heat sources.
- the second organic working fluid is pumped sequentially via the intercooler 28 , the oil heat exchanger 30 , and the cooling water jacket heat exchanger 32 . The cycle may then be repeated.
- the cascaded organic rankine cycle system facilitates heat recovery over a temperature range that is too large for a single organic rankine cycle system to accommodate efficiently.
- the intercooler 28 , the oil heat exchanger 30 , and the cooling water jacket heat exchanger 32 are coupled along a single cooling loop in which the second organic working fluid is heated and partially evaporated.
- the illustrated layout of the second heat sources facilitates effective heat removal from the plurality of lower temperature engine heat sources. This increases the effectiveness of the cooling systems and provides effective conversion of waste heat into electricity.
- the heat generation system may include a gas turbine system. Steam may be circulated through the top cycle and the second organic working fluid may be circulated through the bottom cycle. Steam is condensed and passed in heat exchange relationship with the second organic working fluid through the cascaded heat exchange unit 24 .
- one or more first heat exchangers 41 are disposed at a location 42 between the intercooler 28 and the oil heat exchanger 30 , or at a location 44 between the oil heat exchanger 30 and the cooling water jacket heat exchanger 32 , or at a location 46 between the cooling water jacket heat exchanger 32 and the cascaded heat exchange unit 24 of the second organic rankine cycle system 14 .
- the first heat exchanger 41 may also be disposed at a location 48 between the cascaded heat exchange unit 24 and the second expander 34 , or at a location 50 between the expander 34 and the condenser 38 .
- the second organic working fluid is circulated in heat exchange relationship with water, or water mixed with anti-corrosive agent, or water mixed with anti-freezing agent (third fluid) through the first heat exchanger 41 , for heating the water, for example water supplied to a particular locality.
- One or more second heat exchangers 52 are disposed at a location 54 between the evaporator 16 and first expander 20 , or at a location 56 between the first expander 20 and the cascaded heat exchange unit 24 of the first organic rankine cycle system 12 .
- the first organic working fluid is circulated in heat exchange relationship with water through the second heat exchanger 52 , for heating the water.
- valves may be provided to the first and second rankine cycle systems 12 , 14 to divert the flow of the first and second organic working fluid through the second and first heat exchangers 52 , 41 respectively. It should be noted herein that even though water is mentioned, other fluids are also envisaged.
- both the heat exchangers 41 , 52 may be operated. When more heat is needed for heating the water, heat is extracted from the engine cooling system and transferred to the second organic working fluid. Heat is then extracted from the second organic working fluid via the first heat exchanger 41 for heating the water. Also, heat may be extracted from the first organic fluid via the second heat exchanger 52 for heating the water.
- either one of heat exchangers 41 , 52 may be active. During summer season, neither of the heat exchangers 41 , 52 are active.
- the second organic rankine cycle system 14 may not be used to generate power. In certain other embodiments, when the first heat exchanger 41 disposed at a location 50 downstream of the expander 34 is in active state, the second organic rankine cycle system 14 may be used to generate power.
- the illustrated combined heat and power cycle system 10 includes the first organic rankine cycle system 12 and the second organic rankine cycle system 14 .
- the first organic rankine cycle system 12 includes the evaporator 16 coupled to the first heat source 18 , i.e. the exhaust unit of the engine, via a thermal oil heat exchanger 58 .
- the thermal oil heat exchanger 58 is a shell and tube type heat exchanger. The thermal oil heat exchanger 58 is used to heat thermal oil to a relatively higher temperature using exhaust gas of the engine.
- the evaporator 16 receives heat from the thermal oil and generates a first organic working fluid vapor.
- the thermal oil is then pumped back from the evaporator 16 to the thermal oil heat exchanger 58 using a pump 60 .
- the cascaded heat exchange unit 24 is coupled to a plurality of second heat sources such as the intercooler 28 , the oil heat exchanger 30 , and an engine jacket 62 via a partial evaporator 64 .
- the partial evaporator 64 receives heat from a cooling water loop that collects heat from the oil heat exchanger 30 , the engine jacket 62 , and the intercooler 28 and generates a partially evaporated second organic working fluid two-phase stream.
- the second organic working fluid stream is passed through the cascaded heat exchange unit 24 for complete evaporation or even superheating of the second organic working fluid.
- the fluid in the cooling water loop is pumped via a pump 66 to the oil heat exchanger 30 , before being supplied to the engine jacket, 62 , and the intercooler 28 before it enters the partial evaporator 64 .
- one or more first heat exchangers 41 are disposed at a location 68 between the pump 66 and the oil heat exchanger 30 , or at a location 70 between the oil heat exchanger 30 and the engine jacket 62 , or at a location 72 between the engine jacket 62 and the intercooler 28 , or at a location 74 between the intercooler 28 and the partial evaporator 64 of the second organic rankine cycle system 14 .
- the cooling water is circulated in heat exchange relationship with water to be heated through the first heat exchanger 41 , for heating purpose.
- the first heat exchanger 41 may also be disposed at a location 76 between the partial evaporator 64 and the cascaded heat exchange unit 24 .
- the second organic working fluid is circulated in heat exchange relationship with water through the first heat exchanger 41 .
- One or more second heat exchangers 52 are disposed at a location 78 between the pump 60 and the thermal oil heat exchanger 58 , or at a location 80 between the thermal oil heat exchanger 58 and the evaporator 16 of the first organic rankine cycle system 12 .
- the thermal oil is circulated in heat exchange relationship with water through the second heat exchanger 52 , for heating the water.
- the second rankine cycle system 14 may not be used to generate power.
- the second heat exchanger 52 disposed at any one of the locations 78 , 80 in thermal oil loop is in active state, no heat may be input from the thermal oil loop to the first organic working fluid, and the first organic rankine cycle system 12 may not be used to generate power.
- the cascaded heat exchange unit 24 is coupled to a plurality of second heat sources such as the intercooler 28 , the oil heat exchanger 30 , and the water jacket heat exchanger 32 .
- the second organic working fluid is sequentially passed through the lower temperature intercooler 28 , the oil heat exchanger 30 , and the water jacket heat exchanger 32 before entering the cascading heat exchange unit 24 .
- the second heat sources are used to preheat or partially vaporize the second organic working fluid entering the cascading heat exchange unit.
- the intercooler 28 is a lower temperature intercooler.
- the cascaded heat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor.
- the second organic working fluid vapor is passed through a higher temperature intercooler 82 to the second expander 34 to drive the second generator unit 36 .
- the lower temperature intercooler 28 performs preheating of the second organic working fluid flowing to the cascaded heat exchange unit 24 .
- the higher temperature intercooler 82 provided downstream of the cascaded heat exchange unit 24 is used to heat the second organic working fluid exiting from the cascaded heat exchange unit 24 to a relatively higher temperature, to complete evaporation or to superheat the second organic working fluid.
- the first heat exchanger 41 may be disposed at a location 84 between the cascaded heat exchange unit 24 and the high temperature intercooler 82 , or a location 86 between the high temperature intercooler 82 and the second expander 34 .
- the second organic rankine cycle system 14 may not be used to generate power.
- the second organic rankine cycle system 14 (bottom cycle) of the combined heat and power cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention.
- the cascaded heat exchange unit 24 is coupled to a plurality of second heat sources such as the intercooler 28 , the oil heat exchanger 30 , and the water jacket heat exchanger 32 .
- the second heat sources are used to preheat or partially vaporize the second organic working fluid entering the cascading heat exchange unit 24 .
- the cascaded heat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor.
- the second organic working fluid vapor is passed in heat exchange relationship with the engine exhaust gas (generated from the engine exhaust unit 18 ) via a heat exchanger 94 .
- the heat exchanger 94 provided downstream of the cascaded heat exchange unit 24 is used to heat the second organic working fluid exiting from the cascaded heat exchange unit 24 to a relatively higher temperature, to complete evaporation or to superheat the second organic working fluid.
- the heat exchanger 94 may be provided to the upstream side of the cascaded heat exchange unit 24 .
- the first heat exchanger 41 may be disposed at a location 88 between the cascaded heat exchange unit 24 and the heat exchanger 94 , or a location 90 between the heat exchanger 94 and the second expander 34 .
- the second organic rankine cycle system 14 may still be used to generate power.
- the second organic rankine cycle system 14 may not be used to generate power.
- the first organic rankine cycle system 12 includes the evaporator 16 coupled to the first heat source, i.e. the exhaust unit of the engine, via a thermal oil heat exchanger 58 and an exhaust economizer 92 .
- the thermal oil is then pumped back from the evaporator 16 to the thermal oil heat exchanger 58 using a pump 60 .
- a drying valve 94 is provided between the evaporator 16 and the first expander 20 and is configured to remove traces of moisture from the first organic fluid vapor exiting the evaporator 16 .
- the condensed liquid (i.e. first organic working fluid) from the cascaded heat exchange unit 24 is pumped via the pump 26 to the exhaust economizer 92 . The condensed liquid is heated prior to being supplied to the evaporator 16 .
- the cascaded heat exchange unit 24 is coupled to a plurality of second heat sources such as the lower temperature intercooler 28 , the oil heat exchanger 30 , the water jacket heat exchanger 32 , and the higher temperature intercooler 82 .
- the cascaded heat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor.
- the heat sources disclosed herein may be coupled in series or parallel. The relative positions of the heat sources may also be varied depending upon the requirement.
- the second organic working fluid is passed through the lower temperature intercooler 28 , the oil heat exchanger 30 , the water jacket heat exchanger 32 , and the higher temperature intercooler 82 before entering the cascaded heat exchange unit 24 .
- the first heat exchanger 41 may be disposed at a location 96 between the oil heat exchanger 30 and the water jacket heat exchanger 32 , or a location 98 between the oil heat exchanger 30 and the higher temperature intercooler 82 . In certain embodiments, when the first heat exchanger 41 disposed at any one of the locations 96 , 98 is in active state, the second organic rankine cycle system 14 may not be used to generate power.
- the second organic rankine cycle system 14 (bottom cycle) of the combined heat and power cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention.
- the cascaded heat exchange unit 24 is coupled to a plurality of second heat sources such as the lower temperature intercooler 28 , the oil heat exchanger 30 , the water jacket heat exchanger 32 , the engine jacket 62 , and the higher temperature intercooler 82 .
- a pump 100 is provided to circulate cooling water between the jacket heat exchanger 32 and the engine jacket 62 .
- the second organic working fluid is passed sequentially through the lower temperature intercooler 28 , the oil heat exchanger 30 , the water jacket heat exchanger 32 and the higher temperature intercooler 82 before entering the cascading heat exchange unit 24 .
- the first heat exchanger 41 may be disposed at a location 102 between the pump 100 and the engine jacket 62 , or a location 104 between the engine jacket 62 and the water jacket heat exchanger 32 .
- the first heat exchanger 41 may be disposed at a location 106 between the water jacket heat exchanger 32 and the higher temperature intercooler 82 , or a location 108 between the higher temperature intercooler 82 and the cascaded heat exchange unit 24 .
- the second organic rankine cycle system 14 may not be used to generate power.
- the second organic rankine cycle system 14 (bottom cycle) of the combined heat and power cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention.
- the cascaded heat exchange unit 24 is coupled to a plurality of second heat sources such as the oil heat exchanger 30 , the engine jacket 62 , and the intercooler 28 .
- the cascaded heat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor.
- the intercooler 28 , the oil heat exchanger 30 , and the engine jacket 44 performs preheating or partial vaporization of the second organic working fluid flowing to the cascaded heat exchange unit 24 .
- the first heat exchanger 41 may be disposed at a location 110 between the oil heat exchanger 30 and the engine jacket 62 , or a location 112 between the engine jacket 62 and the intercooler 28 , or a location 114 between the intercooler 28 , and the cascaded heat exchange unit 24 .
- the second organic rankine cycle system 14 may still be used to generate power.
- the activation of the first and second heat exchangers 41 , 52 , and the first and second organic rankine cycle systems 12 , 14 are exemplary embodiments. It should also be noted that the activation criterior may be varied depending the application such as amount of power and heat required. In one embodiment, when power requirement is more and heat requirement is less, both the first and second heat exchangers 41 , 52 may be deactivated and both the first and second rankine cycle systems 12 , 14 are activated to generate power. In another embodiment, either one of the first and second heat exchangers 41 , 52 may be activated, and both the first and second rankine cycle systems 12 , 14 are activated to generate power.
- one of the rankine cycle system may be operated at part-load.
- both the first and second heat exchangers 41 , 52 may be activated and either one of the first and second rankine cycle systems 12 , 14 are activated to generate power. All such permutations and combinations are envisaged. All the embodiments discussed herein facilitate flexible generation of heat and power. When the power requirement is more, less heat is extracted. When power requirement is less, more heat is generated.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
A combined heat and power cycle system includes a heat generation system having at least two separate heat sources having different temperatures. The combined heat and power cycle system includes a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid. A second rankine cycle system is coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid. The first and second working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system. At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof.
Description
- The embodiments disclosed herein relate generally to the field of a combined heat and power cycle system and, more particularly, to a combined heat and power cycle system for recovering waste heat from a plurality of heat sources having different temperatures for heating purpose and generation of electricity.
- Enormous amounts of waste heat are generated by a wide variety of industrial and commercial processes and operations. Example sources of waste heat include heat from space heating assemblies, steam boilers, engines, and cooling systems. When waste heat is low grade, such as waste heat having a temperature of heat below 840 degrees Fahrenheit, for example, conventional heat recovery systems do not operate with sufficient efficiency to make recovery of energy cost-effective. The net result is that vast quantities of waste heat are simply dumped into the atmosphere, ground, or water.
- Some power generation systems provide better reliability and off-grid operation with alternate fuels such as biogas or landfill gas, with examples being gas turbines and combustion engines such as microturbines and reciprocating engines. Combustion engines may be used to generate electricity using fuels such as gasoline, natural gas, biogas, plant oil, and diesel fuel. However, atmospheric emissions such as nitrogen oxides and particulates may be emitted.
- One method to generate electricity from the waste heat of a combustion engine without increasing the output of emissions is to apply a bottoming rankine cycle. A fundamental rankine cycle typically includes a turbo generator, an evaporator/boiler, a condenser, and a liquid pump. In another method to generate electricity from waste heat, single cycle system or two-cycle systems are used in heat recovery applications with waste heat sources of different temperature levels. Single-cycle configurations collect heat from the different waste heat locations in a serial arrangement of heat exchangers with an intermediate heating fluid. In two-cycle configurations, the hot heat source heats a high-boiling point liquid in a top loop, and the cold heat source heats a low-boiling point liquid in a separate bottom loop. In another conventional system provided to generate electricity from waste heat, a cascaded organic rankine cycle system for utilization of waste heat includes a pair of organic rankine cycle systems. The cycles are combined, and the respective organic working fluids are chosen such that the organic working fluid of the first organic rankine cycle is condensed at a condensation temperature that is above the boiling point of the organic working fluid of the second organic cycle.
- Most of the conventional systems discussed above, are used to exclusively produce power. In other words, the conventional systems provide less flexibility in the ratio between power and heat produced.
- There is a need for a combined heat and power cycle system that provides flexibility in the ratio between power and heat produced.
- In accordance with one exemplary embodiment disclosed herein, a combined heat and power cycle system including at least two integrated rankine cycle systems is provided. The combined heat and power cycle system includes a heat generation system comprising at least two separate heat sources having different temperatures. The combined heat and power cycle system includes a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid. The first rankine system is configured to remove heat from the first heat source. A second rankine cycle system is coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid. The at least one second heat source includes a lower temperature heat source than the first heat source. The second rankine cycle system is configured to remove heat from the at least one second heat source. The first and second working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system. At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof. The first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
- In accordance with one exemplary embodiment disclosed herein, a combined heat and power cycle system including at least two integrated organic rankine cycle system is provided. The combined heat and power cycle system includes a combustion engine having an engine exhaust unit; and at least another heat source selected from a group comprising an oil heat exchanger, engine jacket, water jacket heat exchanger, lower temperature intercooler, higher temperature intercooler, or combinations thereof. The combined heat and power cycle system includes a first organic rankine cycle system coupled to the engine exhaust unit and configured to circulate a first organic working fluid. A second organic rankine cycle system is coupled to at least one other heat source selected from the group comprising the oil heat exchanger, engine jacket, water jacket heat exchanger, lower temperature intercooler, higher temperature intercooler, or combinations thereof, and configured to circulate a second organic working fluid. The one heat source includes a lower temperature heat source than at least one other heat source. The second organic rankine cycle system is configured to remove heat from the at least one other heat source. The first and second organic working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first organic working fluid in the first organic rankine cycle system and evaporation of the second organic working fluid in the second organic rankine cycle system. At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof. The first working fluid, second working fluid, or combinations thereof, are circulatable in heat exchange relationship with the third fluid through the at least one heat exchanger for heating the the third fluid.
- In accordance with one exemplary embodiment disclosed herein, a combined heat and power cycle system including at least two integrated rankine cycle systems is provided. The combined heat and power cycle system includes a heat generation system comprising at least two separate heat sources having different temperatures. The combined heat and power cycle system includes a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid. The first rankine system is configured to remove heat from the first heat source. A second rankine cycle system is coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid. The at least one second heat source includes a lower temperature heat source than the first heat source. The second rankine cycle system is configured to remove heat from the at least one second heat source. The first and second working fluids are circulatable in heat exchange relationship through a cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system. The second rankine cycle is configured to partially evaporate the second working fluid before entering the cascaded heat exchange unit. At least one heat exchanger is disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof. The first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
- These and other features, aspects, and advantages of the present invention will become better understood when the following detailed description is read with reference to the accompanying drawings in which like characters represent like parts throughout the drawings, wherein:
-
FIG. 1 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with an exemplary embodiment disclosed herein; -
FIG. 2 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with another exemplary embodiment disclosed herein; -
FIG. 3 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with yet another exemplary embodiment disclosed herein; -
FIG. 4 is a diagrammatical representation of a bottom cycle of a combined heat and power cycle system in accordance with an exemplary embodiment disclosed herein; -
FIG. 5 is a diagrammatical representation of a combined heat and power cycle system having two integrated organic rankine cycle systems in accordance with yet another exemplary embodiment disclosed herein; -
FIG. 6 is a diagrammatical representation of a bottom cycle of a combined heat and power cycle system in accordance with an exemplary embodiment disclosed herein; and -
FIG. 7 is a diagrammatical representation of a bottom cycle of a combined heat and power cycle system in accordance with an exemplary embodiment disclosed herein. - As discussed in detail below, embodiments of the present invention provide a combined heat and power cycle system having at least two integrated rankine cycle systems coupled to at least two separate heat sources respectively having different temperatures. The first rankine cycle system is coupled to a first heat source and configured to circulate a first working fluid. The second rankine cycle system is coupled to at least one second heat source and configured to circulate a second working fluid. The second heat source includes a lower temperature heat source than the first heat source. The combined heat and power cycle system also includes a cascaded heat exchange unit. The first and second working fluids are circulated in heat exchange relationship for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system. In accordance with the exemplary embodiments of the present invention, the combined heat and power cycle system includes one or more heat exchangers disposed at one or more locations in the first rankine cycle system, second rankine cycle system, or combinations thereof for heating a third fluid to be used for a particular locality. In some embodiments, the third fluid comprises water, water mixed with anti-corrosive agent, or water mixed with anti-freezing agent. The provision of additional heat exchangers for heating purpose enables flexible heat extraction and power generation. Although the combined heat and power cycle system in the exemplary embodiments of
FIGS. 1-9 is described with reference to combustion engines, the system is also applicable to other heat generation systems such as gas turbines, geothermal, solar thermal, industrial and residential heat sources, or the like. - As a preliminary matter, the definition of the term “or” for the purpose of the following discussion and the appended claims is intended to be an inclusive “or.” That is, the term “or” is not intended to differentiate between two mutually exclusive alternatives. Rather, the term “or” when employed as a conjunction between two elements is defined as including one element by itself, the other element itself, and combinations and permutations of the elements. For example, a discussion or recitation employing the terminology “A” or “B” includes: “A” by itself, “B” by itself, and any combination thereof, such as “AB” and “BA.” Furthermore, it is of note that the present discussion relates to exemplary embodiments, and the appended claims should not be limited to the embodiments discussed.
- Referring to
FIG. 1 , a combined heat andpower cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention. The illustrated combined heat andpower cycle system 10 includes a first organic rankine cycle system 12 (top cycle) and a second organic rankine cycle system 14 (bottom cycle). A first organic working fluid is circulated through the first organicrankine cycle system 12. The first organic working fluid may include cyclohexane, cyclopentane, thiophene, ketones, aromatics, or combinations thereof. The first organicrankine cycle system 12 includes anevaporator 16 coupled to afirst heat source 18, for example an exhaust unit of a heat generation system 19 (for example, an engine). In one example, the temperature of the exhaust unit of the engine may be in the temperature range of 400 to 500 degrees Celsius. Theevaporator 16 receives heat from the exhaust gas generated from thefirst heat source 18 and generates a first organic working fluid vapor. The first organic working fluid vapor is passed through afirst expander 20 to drive afirst generator unit 22. After passing through thefirst expander 20, the first organic working fluid vapor at a relatively lower pressure and lower temperature is passed through the cascadedheat exchange unit 24. The first organic working fluid vapor is condensed into a liquid, which is then pumped via apump 26 to theevaporator 16. The cycle may then be repeated. - The cascaded
heat exchange unit 24 is used both as a condenser for the first organicrankine cycle system 12 and as an evaporator for the second organicrankine cycle system 14. A second organic working fluid is circulated through the second organicrankine cycle system 14. The second organic working fluid may include propane, butane, pentafluoro-propane, pentafluoro-butane, pentafluoro-polyether, oil, or combinations thereof. It should be noted herein that list of first and second organic working fluids are not inclusive and other organic working fluids applicable to organic rankine cycles are also envisaged. In certain other exemplary embodiments, the first or second organic working fluid includes a binary fluid. The binary fluid may include cyclohexane-propane, cyclohexane-butane, cyclopentane-butane, or cyclopentane-pentafluoropropane, for example. Cascadedheat exchange unit 24 may be coupled to any one or more of a plurality of second heat sources such as anintercooler 28, anoil heat exchanger 30, and a cooling waterjacket heat exchanger 32 being coupled either in series or parallel. Such second heat sources are also typically coupled to the engine. It should be noted herein that the second heat source includes a lower temperature heat source than the first heat source. It should be noted that in other exemplary embodiments, first and second heat sources may include other multiple low-grade heat sources such as gas turbines with intercoolers. The cascadedheat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor. The second organic working fluid vapor is passed through asecond expander 34 to drive asecond generator unit 36. In certain other exemplary embodiments, thefirst expander 20 and thesecond expander 34 are coupled to a single generator unit. - In an exemplary embodiment, neither of the first and second organic working fluids are expanded below the atmospheric pressure, and the boiling point temperature of the first organic working fluid is below the average temperature of the second heat source. After passing through the
second expander 34, the second organic working fluid vapor at lower pressure and lower temperature is passed through acondenser 38. The second organic working fluid vapor is condensed into a liquid, which is then pumped via apump 40 to the second heat sources. In the illustrated embodiment, the second organic working fluid is pumped sequentially via theintercooler 28, theoil heat exchanger 30, and the cooling waterjacket heat exchanger 32. The cycle may then be repeated. - The cascaded organic rankine cycle system facilitates heat recovery over a temperature range that is too large for a single organic rankine cycle system to accommodate efficiently. In one embodiment, the
intercooler 28, theoil heat exchanger 30, and the cooling waterjacket heat exchanger 32 are coupled along a single cooling loop in which the second organic working fluid is heated and partially evaporated. The illustrated layout of the second heat sources facilitates effective heat removal from the plurality of lower temperature engine heat sources. This increases the effectiveness of the cooling systems and provides effective conversion of waste heat into electricity. In another exemplary embodiment of the present invention, the heat generation system may include a gas turbine system. Steam may be circulated through the top cycle and the second organic working fluid may be circulated through the bottom cycle. Steam is condensed and passed in heat exchange relationship with the second organic working fluid through the cascadedheat exchange unit 24. - In the illustrated embodiment, one or more
first heat exchangers 41 are disposed at alocation 42 between theintercooler 28 and theoil heat exchanger 30, or at alocation 44 between theoil heat exchanger 30 and the cooling waterjacket heat exchanger 32, or at alocation 46 between the cooling waterjacket heat exchanger 32 and the cascadedheat exchange unit 24 of the second organicrankine cycle system 14. Thefirst heat exchanger 41 may also be disposed at alocation 48 between the cascadedheat exchange unit 24 and thesecond expander 34, or at alocation 50 between theexpander 34 and thecondenser 38. The second organic working fluid is circulated in heat exchange relationship with water, or water mixed with anti-corrosive agent, or water mixed with anti-freezing agent (third fluid) through thefirst heat exchanger 41, for heating the water, for example water supplied to a particular locality. One or moresecond heat exchangers 52 are disposed at alocation 54 between the evaporator 16 andfirst expander 20, or at alocation 56 between thefirst expander 20 and the cascadedheat exchange unit 24 of the first organicrankine cycle system 12. The first organic working fluid is circulated in heat exchange relationship with water through thesecond heat exchanger 52, for heating the water. In the illustrated embodiment, valves may be provided to the first and second 12, 14 to divert the flow of the first and second organic working fluid through the second andrankine cycle systems 52, 41 respectively. It should be noted herein that even though water is mentioned, other fluids are also envisaged.first heat exchangers - During winter season, both the
41, 52 may be operated. When more heat is needed for heating the water, heat is extracted from the engine cooling system and transferred to the second organic working fluid. Heat is then extracted from the second organic working fluid via theheat exchangers first heat exchanger 41 for heating the water. Also, heat may be extracted from the first organic fluid via thesecond heat exchanger 52 for heating the water. During spring or autumn season, either one of 41, 52 may be active. During summer season, neither of theheat exchangers 41, 52 are active.heat exchangers - In certain embodiments, when the
first heat exchanger 41 disposed at any one of the 42, 44, 46, and 48 upstream of thelocations expander 34 is in active state, the second organicrankine cycle system 14 may not be used to generate power. In certain other embodiments, when thefirst heat exchanger 41 disposed at alocation 50 downstream of theexpander 34 is in active state, the second organicrankine cycle system 14 may be used to generate power. - In some embodiments, when the
second heat exchanger 52 disposed at alocation 54 upstream of theexpander 20 is in active state, the first organicrankine cycle system 12 may not be used to generate power. In certain other embodiments, when thesecond heat exchanger 52 disposed at alocation 56 downstream of theexpander 20 is in active state, the first organicrankine cycle system 12 may be used to generate power. In some embodiments, when thesecond heat exchanger 52 is not active, heat is input from the first organicrankine cycle system 12 to the second organicrankine cycle system 14. All such permutations and combinations are envisaged, thus facilitating higher power to heat ratio flexibility. - Referring to
FIG. 2 , a combined heat andpower cycle system 10 is illustrated in accordance with another exemplary embodiment of the present invention. As discussed above, the illustrated combined heat andpower cycle system 10 includes the first organicrankine cycle system 12 and the second organicrankine cycle system 14. In the illustrated embodiment, the first organicrankine cycle system 12 includes theevaporator 16 coupled to thefirst heat source 18, i.e. the exhaust unit of the engine, via a thermaloil heat exchanger 58. In the illustrated embodiment, the thermaloil heat exchanger 58 is a shell and tube type heat exchanger. The thermaloil heat exchanger 58 is used to heat thermal oil to a relatively higher temperature using exhaust gas of the engine. Theevaporator 16 receives heat from the thermal oil and generates a first organic working fluid vapor. The thermal oil is then pumped back from theevaporator 16 to the thermaloil heat exchanger 58 using apump 60. - In the illustrated embodiment, the cascaded
heat exchange unit 24 is coupled to a plurality of second heat sources such as theintercooler 28, theoil heat exchanger 30, and anengine jacket 62 via apartial evaporator 64. Thepartial evaporator 64 receives heat from a cooling water loop that collects heat from theoil heat exchanger 30, theengine jacket 62, and theintercooler 28 and generates a partially evaporated second organic working fluid two-phase stream. The second organic working fluid stream is passed through the cascadedheat exchange unit 24 for complete evaporation or even superheating of the second organic working fluid. The fluid in the cooling water loop is pumped via apump 66 to theoil heat exchanger 30, before being supplied to the engine jacket, 62, and theintercooler 28 before it enters thepartial evaporator 64. - In the illustrated embodiment, one or more
first heat exchangers 41 are disposed at alocation 68 between thepump 66 and theoil heat exchanger 30, or at alocation 70 between theoil heat exchanger 30 and theengine jacket 62, or at a location 72 between theengine jacket 62 and theintercooler 28, or at alocation 74 between theintercooler 28 and thepartial evaporator 64 of the second organicrankine cycle system 14. The cooling water is circulated in heat exchange relationship with water to be heated through thefirst heat exchanger 41, for heating purpose. In an alternate embodiment, thefirst heat exchanger 41 may also be disposed at alocation 76 between thepartial evaporator 64 and the cascadedheat exchange unit 24. In such an embodiment, the second organic working fluid is circulated in heat exchange relationship with water through thefirst heat exchanger 41. - One or more
second heat exchangers 52 are disposed at alocation 78 between thepump 60 and the thermaloil heat exchanger 58, or at alocation 80 between the thermaloil heat exchanger 58 and theevaporator 16 of the first organicrankine cycle system 12. The thermal oil is circulated in heat exchange relationship with water through thesecond heat exchanger 52, for heating the water. - In certain embodiments, when the
first heat exchanger 41 disposed at any one of the 68, 70, 72, 74 in the cooling loop is in active state, no heat may be input from the cooling loop to the second organic working fluid. In certain other embodiments, when thelocations first heat exchanger 41 disposed at alocation 76 downstream of thepartial evaporator 64 is in active state, the secondrankine cycle system 14 may not be used to generate power. - In some embodiments, when the
second heat exchanger 52 disposed at any one of the 78, 80 in thermal oil loop is in active state, no heat may be input from the thermal oil loop to the first organic working fluid, and the first organiclocations rankine cycle system 12 may not be used to generate power. - Referring to
FIG. 3 , a combined heat andpower cycle system 10 is illustrated in accordance with another exemplary embodiment of the present invention. In the illustrated embodiment, the cascadedheat exchange unit 24 is coupled to a plurality of second heat sources such as theintercooler 28, theoil heat exchanger 30, and the waterjacket heat exchanger 32. In the illustrated embodiment, the second organic working fluid is sequentially passed through thelower temperature intercooler 28, theoil heat exchanger 30, and the waterjacket heat exchanger 32 before entering the cascadingheat exchange unit 24. The second heat sources are used to preheat or partially vaporize the second organic working fluid entering the cascading heat exchange unit. In the illustrated embodiment, theintercooler 28 is a lower temperature intercooler. The cascadedheat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor. The second organic working fluid vapor is passed through ahigher temperature intercooler 82 to thesecond expander 34 to drive thesecond generator unit 36. In the illustrated embodiment, thelower temperature intercooler 28 performs preheating of the second organic working fluid flowing to the cascadedheat exchange unit 24. Thehigher temperature intercooler 82 provided downstream of the cascadedheat exchange unit 24 is used to heat the second organic working fluid exiting from the cascadedheat exchange unit 24 to a relatively higher temperature, to complete evaporation or to superheat the second organic working fluid. - In the illustrated embodiment, the
first heat exchanger 41 may be disposed at alocation 84 between the cascadedheat exchange unit 24 and thehigh temperature intercooler 82, or alocation 86 between thehigh temperature intercooler 82 and thesecond expander 34. In certain embodiments, when thefirst heat exchanger 41 disposed at any one of the 84, 86 upstream of thelocations second expander 34 is in active state, the second organicrankine cycle system 14 may not be used to generate power. - Referring to
FIG. 4 , the second organic rankine cycle system 14 (bottom cycle) of the combined heat andpower cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention. In the illustrated embodiment, the cascadedheat exchange unit 24 is coupled to a plurality of second heat sources such as theintercooler 28, theoil heat exchanger 30, and the waterjacket heat exchanger 32. The second heat sources are used to preheat or partially vaporize the second organic working fluid entering the cascadingheat exchange unit 24. The cascadedheat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor. In the illustrated embodiment, the second organic working fluid vapor is passed in heat exchange relationship with the engine exhaust gas (generated from the engine exhaust unit 18) via aheat exchanger 94. Theheat exchanger 94 provided downstream of the cascadedheat exchange unit 24 is used to heat the second organic working fluid exiting from the cascadedheat exchange unit 24 to a relatively higher temperature, to complete evaporation or to superheat the second organic working fluid. In certain other exemplary embodiments, theheat exchanger 94 may be provided to the upstream side of the cascadedheat exchange unit 24. - In the illustrated embodiment, the
first heat exchanger 41 may be disposed at alocation 88 between the cascadedheat exchange unit 24 and theheat exchanger 94, or alocation 90 between theheat exchanger 94 and thesecond expander 34. In certain embodiments, when thefirst heat exchanger 41 disposed at thelocation 88 upstream of theheat exchanger 94 is in active state, the second organicrankine cycle system 14 may still be used to generate power. In certain other embodiments, when thefirst heat exchanger 41 disposed at thelocation 90 downstream of theheat exchanger 94 is in active state, the second organicrankine cycle system 14 may not be used to generate power. - Referring to
FIG. 5 , a combined heat andpower cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention. In the illustrated embodiment, the first organicrankine cycle system 12 includes theevaporator 16 coupled to the first heat source, i.e. the exhaust unit of the engine, via a thermaloil heat exchanger 58 and anexhaust economizer 92. The thermal oil is then pumped back from theevaporator 16 to the thermaloil heat exchanger 58 using apump 60. A dryingvalve 94 is provided between the evaporator 16 and thefirst expander 20 and is configured to remove traces of moisture from the first organic fluid vapor exiting theevaporator 16. In the illustrated embodiment, the condensed liquid (i.e. first organic working fluid) from the cascadedheat exchange unit 24 is pumped via thepump 26 to theexhaust economizer 92. The condensed liquid is heated prior to being supplied to theevaporator 16. - In the illustrated embodiment, the cascaded
heat exchange unit 24 is coupled to a plurality of second heat sources such as thelower temperature intercooler 28, theoil heat exchanger 30, the waterjacket heat exchanger 32, and thehigher temperature intercooler 82. The cascadedheat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor. The heat sources disclosed herein may be coupled in series or parallel. The relative positions of the heat sources may also be varied depending upon the requirement. In the illustrated embodiment, the second organic working fluid is passed through thelower temperature intercooler 28, theoil heat exchanger 30, the waterjacket heat exchanger 32, and thehigher temperature intercooler 82 before entering the cascadedheat exchange unit 24. - In the illustrated embodiment, the
first heat exchanger 41 may be disposed at alocation 96 between theoil heat exchanger 30 and the waterjacket heat exchanger 32, or alocation 98 between theoil heat exchanger 30 and thehigher temperature intercooler 82. In certain embodiments, when thefirst heat exchanger 41 disposed at any one of the 96, 98 is in active state, the second organiclocations rankine cycle system 14 may not be used to generate power. - Referring to
FIG. 6 , the second organic rankine cycle system 14 (bottom cycle) of the combined heat andpower cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention. The cascadedheat exchange unit 24 is coupled to a plurality of second heat sources such as thelower temperature intercooler 28, theoil heat exchanger 30, the waterjacket heat exchanger 32, theengine jacket 62, and thehigher temperature intercooler 82. Apump 100 is provided to circulate cooling water between thejacket heat exchanger 32 and theengine jacket 62. In the illustrated embodiment, the second organic working fluid is passed sequentially through thelower temperature intercooler 28, theoil heat exchanger 30, the waterjacket heat exchanger 32 and thehigher temperature intercooler 82 before entering the cascadingheat exchange unit 24. - In the illustrated embodiment, the
first heat exchanger 41 may be disposed at alocation 102 between thepump 100 and theengine jacket 62, or alocation 104 between theengine jacket 62 and the waterjacket heat exchanger 32. Alternately, thefirst heat exchanger 41 may be disposed at alocation 106 between the waterjacket heat exchanger 32 and thehigher temperature intercooler 82, or alocation 108 between thehigher temperature intercooler 82 and the cascadedheat exchange unit 24. - In certain embodiments, when the
first heat exchanger 41 disposed at any one of the 102, 104 in the cooling loop is in active state, no heat may be input from the cooling loop to the second organic working fluid and the second organiclocations rankine cycle system 14 may still be used to generate power. In certain other embodiments, when thefirst heat exchanger 41 disposed at any one of the 106, 108 upstream of the cascadedlocations heat exchange unit 24 is in active state, the second organicrankine cycle system 14 may not be used to generate power. - Referring to
FIG. 7 , the second organic rankine cycle system 14 (bottom cycle) of the combined heat andpower cycle system 10 is illustrated in accordance with an exemplary embodiment of the present invention. The cascadedheat exchange unit 24 is coupled to a plurality of second heat sources such as theoil heat exchanger 30, theengine jacket 62, and theintercooler 28. The cascadedheat exchange unit 24 receives heat from the first organic working fluid and generates a second organic working fluid vapor. In the illustrated embodiment, theintercooler 28, theoil heat exchanger 30, and theengine jacket 44 performs preheating or partial vaporization of the second organic working fluid flowing to the cascadedheat exchange unit 24. - In the illustrated embodiment, the
first heat exchanger 41 may be disposed at alocation 110 between theoil heat exchanger 30 and theengine jacket 62, or alocation 112 between theengine jacket 62 and theintercooler 28, or alocation 114 between theintercooler 28, and the cascadedheat exchange unit 24. In certain embodiments, when thefirst heat exchanger 41 disposed at any one of the 110, 112, 114 is in active state, the second organiclocations rankine cycle system 14 may still be used to generate power. - It should be noted herein that with reference to
FIGS. 1-7 , the activation of the first and 41, 52, and the first and second organicsecond heat exchangers 12, 14 are exemplary embodiments. It should also be noted that the activation criterior may be varied depending the application such as amount of power and heat required. In one embodiment, when power requirement is more and heat requirement is less, both the first andrankine cycle systems 41, 52 may be deactivated and both the first and secondsecond heat exchangers 12, 14 are activated to generate power. In another embodiment, either one of the first andrankine cycle systems 41, 52 may be activated, and both the first and secondsecond heat exchangers 12, 14 are activated to generate power. In such a more specific embodiment, one of the rankine cycle system may be operated at part-load. In another embodiment, when the heat requirement is more and power requirement is less, both the first andrankine cycle systems 41, 52 may be activated and either one of the first and secondsecond heat exchangers 12, 14 are activated to generate power. All such permutations and combinations are envisaged. All the embodiments discussed herein facilitate flexible generation of heat and power. When the power requirement is more, less heat is extracted. When power requirement is less, more heat is generated.rankine cycle systems - While only certain features of the invention have been illustrated and described herein, many modifications and changes will occur to those skilled in the art. It is, therefore, to be understood that the appended claims are intended to cover all such modifications and changes as fall within the true spirit of the invention.
Claims (36)
1. A combined heat and power cycle system including at least two integrated rankine cycle systems, the combined heat and power cycle system comprising:
a heat generation system comprising at least two separate heat sources having different temperatures;
a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid; wherein the first rankine system is configured to remove heat from the first heat source;
a second rankine cycle system is coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid, the at least one second heat source comprising a lower temperature heat source than the first heat source, wherein the second rankine cycle system is configured to remove heat from the at least one second heat source; and
a cascaded heat exchange unit, wherein the first and second working fluids are circulatable in heat exchange relationship through the cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system; and
at least one heat exchanger disposed at one or more locations in the first rankine cycle system; second rankine system, or combinations thereof; wherein the first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
2. The combined heat and power cycle system of claim 1 , wherein the third fluid comprises water, or water mixed with anti-corrosive agent, or water mixed with anit-freezing agent.
3. The combined heat and power cycle system of claim 1 , wherein the second working fluid comprises a second organic working fluid.
4. The combined heat and power cycle system of claim 1 , wherein the second organic working fluid comprises propane, butane, pentafluoro-propane, pentafluoro-butane, pentafluoro-polyether, oil, or combinations thereof.
5. The combined heat and power cycle system of claim 1 , wherein the second rankine cycle system comprises a condenser coupled to the at least one second heat source selected from a group comprising an oil heat exchanger, an engine jacket, a water jacket heat exchanger, a lower temperature intercooler, a higher temperature intercooler, or combinations thereof.
6. The combined heat and power cycle system of claim 5 , wherein the one or more locations in the second rankine cycle system comprises one or more locations between the plurality of second heat sources.
7. The combined heat and power cycle system of claim 5 , wherein the one or more locations in the second rankine cycle system comprises a location between the at least one second heat source and the cascaded heat exchange unit.
8. The combined heat and power cycle system of claim 5 , wherein the one or more locations in the second rankine cycle system comprises a location between the cascaded heat exchange unit and an expander.
9. The combined heat and power cycle system of claim 5 , wherein the one or more locations in the second rankine cycle system comprises a location between an expander and the condenser.
10. The combined heat and power cycle system of claim 5 , wherein the lower temperature intercooler and the higher temperature intercooler are provided respectively to an upstream side and a downstream side of the cascaded heat exchange unit.
11. The combined heat and power cycle system of claim 10 , wherein the one or more locations in the second rankine cycle system comprises a location between the cascaded heat exchange unit and the high temperature intercooler.
12. The combined heat and power cycle system of claim 9 , wherein the one or more locations in the second rankine cycle system comprises a location between the high temperature intercooler and an expander.
13. The combined heat and power cycle system of claim 5 , wherein the at least one second heat source is configured to partially evaporate the second working fluid before entering the cascaded heat exchange unit.
14. The combined heat and power cycle system of claim 5 , further comprising a partial evaporator; wherein the condenser is coupled to the oil heat exchanger, the engine jacket, the water jacket heat exchanger, the engine jacket, the lower temperature intercooler, the higher temperature intercooler, or combinations thereof through the partial evaporator configured to partially evaporate the second working fluid before entering the cascaded heat exchange unit.
15. The combined heat and power cycle system of claim 14 , wherein the one or more locations in the second rankine cycle system comprises one or more locations between the partial evaporator and the oil heat exchanger, the engine jacket, the water jacket heat exchanger, the engine jacket, the lower temperature intercooler, the higher temperature intercooler, or combinations thereof.
16. The combined heat and power cycle system of claim 14 , wherein the one or more locations in the second rankine cycle system comprises a location between the partial evaporator and the cascaded heat exchange unit.
17. The combined heat and power cycle system of claim 1 , wherein the second rankine cycle system is configured to remove heat from the first heat source through a third heat exchanger.
18. The combined heat and power cycle system of claim 17 , wherein the one or more locations in the second rankine cycle system comprises a location between the cascaded heat exchange unit and the third heat exchanger.
19. The combined heat and power cycle system of claim 17 , wherein the one or more locations in the second rankine cycle system comprises a location between the third heat exchanger and an expander.
20. The combined heat and power cycle system of claim 1 , wherein the first working fluid comprises steam.
21. The combined heat and power cycle system of claim 1 , wherein the first working fluid comprises a first organic working fluid.
22. The combined heat and power cycle system of claim 1 , wherein the first organic working fluid comprises cyclohexane, cyclopentane, thiophene, ketones, aromatics, or combinations thereof.
23. The combined heat and power cycle system of claim 1 , wherein one or more locations in the first rankine cycle system comprises a location between an evaporator and an expander.
24. The combined heat and power cycle system of claim 1 , wherein one or more locations in the first rankine cycle system comprises a location between an expander and the cascaded heat exchange unit.
25. The combined heat and power cycle system of claim 1 , wherein the at least one heat exchanger is selectively activated and deactivated depending on the amount of heat required for heating the third fluid.
26. The combined heat and power cycle system of claim 1 , wherein the first rankine cycle system and the second rankine cycle system are selectively activated and deactivated depending on the amount of power required.
27. A combined heat and power cycle system including at least two integrated organic rankine cycle systems, the combined heat and power cycle system comprising:
a combustion engine comprising one heat source comprising an engine exhaust unit; and at least one other heat source selected from a group comprising an oil heat exchanger, an engine jacket, a water jacket heat exchanger, a lower temperature intercooler, a higher temperature intercooler, or combinations thereof;
a first organic rankine cycle system coupled to the engine exhaust unit and configured to circulate a first organic working fluid; wherein the first organic rankine system is configured to remove heat from the engine exhaust unit;
a second organic rankine cycle system coupled to the at least one other heat source selected from the group comprising the oil heat exchanger, the engine jacket, the water jacket heat exchanger, the lower temperature intercooler, the higher temperature intercooler, or combinations thereof; and configured to circulate a second organic working fluid, the one heat source comprising a higher temperature heat source than the at least one other heat source, wherein the second organic rankine cycle system is configured to remove heat from the at least one other heat source; and
a cascaded heat exchange unit, wherein the first and second organic working fluids are circulatable in heat exchange relationship through the cascaded heat exchange unit for condensation of the first organic working fluid in the first organic rankine cycle system and evaporation of the second organic working fluid in the second organic rankine cycle system; and
at least one heat exchanger disposed at one or more locations in the first rankine cycle system; second rankine cycle system, or combinations thereof, wherein the first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
28. The combined heat and power cycle system of claim 27 , wherein the third fluid comprises water, or water mixed with anti-corrosive agent, or water mixed with anti-freezing agent.
29. The combined heat and power cycle system of claim 27 , wherein the first organic rankine cycle system further comprises an evaporator coupled to the engine exhaust unit.
30. The combined heat and power cycle system of claim 29 , wherein the evaporator is coupled to the engine exhaust unit through a thermal oil heat exchanger, an exhaust economizer, or combinations thereof.
31. The combined heat and power cycle system of claim 27 , wherein the one or more locations in the first rankine cycle system comprises one or more locations between the evaporator and the thermal oil heat exchanger, the exhaust economizer, or combinations thereof.
32. The combined heat and power cycle system of claim 27 , wherein the second rankine cycle system comprises a condenser coupled to the at least one other heat source selected from the group comprising the oil heat exchanger, the engine jacket, the water jacket heat exchanger, the lower temperature intercooler, the higher temperature intercooler, or combinations thereof.
33. The combined heat and power cycle system of claim 27 , wherein the at least one heat exchanger is selectively activated and deactivated depending on the amount of heat required for heating the third fluid.
34. The combined heat and power cycle system of claim 27 , wherein the first organic rankine cycle system and the second organic rankine cycle system are selectively activated and deactivated depending on the amount of power required.
35. A combined heat and power cycle system including at least two integrated rankine cycle systems, the combined heat and power cycle system comprising:
a heat generation system comprising at least two separate heat sources having different temperatures;
a first rankine cycle system coupled to a first heat source among the at least two separate heat sources and configured to circulate a first working fluid; wherein the first rankine system is configured to remove heat from the first heat source;
a second rankine cycle system coupled to at least one second heat source among the at least two separate heat sources and configured to circulate a second working fluid, the at least one second heat source comprising a lower temperature heat source than the first heat source, wherein the second rankine cycle system is configured to remove heat from the at least one second heat source; and
a cascaded heat exchange unit, wherein the first and second working fluids are circulatable in heat exchange relationship through the cascaded heat exchange unit for condensation of the first working fluid in the first rankine cycle system and evaporation of the second working fluid in the second rankine cycle system; wherein the second rankine cycle is configured to preheat and/or partially evaporate the second working fluid before entering the cascaded heat exchange unit;
at least one heat exchanger disposed at one or more locations in the first rankine cycle system; second rankine cycle system, or combinations thereof; wherein the first working fluid, second working fluid, or combinations thereof are circulatable in heat exchange relationship with a third fluid through the at least one heat exchanger for heating the third fluid.
36. The combined heat and power cycle system of claim 36 , wherein the third fluid comprises water, or water mixed with anit-corrosive agent, or water mixed with anti-freezing agent.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/413,920 US20100242476A1 (en) | 2009-03-30 | 2009-03-30 | Combined heat and power cycle system |
| US12/616,827 US20100242479A1 (en) | 2009-03-30 | 2009-11-12 | Tri-generation system using cascading organic rankine cycle |
| EP10157834.2A EP2423474A3 (en) | 2009-03-30 | 2010-03-25 | Tri-generation system using cascading organic rankine cycle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/413,920 US20100242476A1 (en) | 2009-03-30 | 2009-03-30 | Combined heat and power cycle system |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/616,827 Continuation-In-Part US20100242479A1 (en) | 2009-03-30 | 2009-11-12 | Tri-generation system using cascading organic rankine cycle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20100242476A1 true US20100242476A1 (en) | 2010-09-30 |
Family
ID=42782439
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/413,920 Abandoned US20100242476A1 (en) | 2009-03-30 | 2009-03-30 | Combined heat and power cycle system |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US20100242476A1 (en) |
Cited By (33)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110072820A1 (en) * | 2009-09-30 | 2011-03-31 | General Electric Company | Heat engine and method for operating the same |
| DE202011109771U1 (en) | 2011-02-10 | 2012-03-21 | Voith Patent Gmbh | Stationary power plant, in particular gas power plant, for power generation |
| WO2012054049A1 (en) * | 2010-10-22 | 2012-04-26 | General Electric Company | Heat engine and method for operating the same |
| CN102454441A (en) * | 2010-10-29 | 2012-05-16 | 通用电气公司 | Rankine cycle integrated with absorption chiller |
| JP2012163093A (en) * | 2010-11-19 | 2012-08-30 | General Electric Co <Ge> | Rankine cycle integrated with organic rankine cycle and absorption chiller cycle |
| US20120279220A1 (en) * | 2011-05-02 | 2012-11-08 | Harris Corporation | Hybrid imbedded combined cycle |
| US8650879B2 (en) | 2011-04-20 | 2014-02-18 | General Electric Company | Integration of waste heat from charge air cooling into a cascaded organic rankine cycle system |
| EP2733339A1 (en) * | 2012-11-20 | 2014-05-21 | IAV GmbH Ingenieurgesellschaft Auto und Verkehr | Device for utilisation of the waste heat of an internal combustion engine |
| US20140352306A1 (en) * | 2013-05-30 | 2014-12-04 | General Electric Company | System and method of waste heat recovery |
| US8997490B2 (en) | 2012-02-02 | 2015-04-07 | Electratherm, Inc. | Heat utilization in ORC systems |
| US9038389B2 (en) | 2012-06-26 | 2015-05-26 | Harris Corporation | Hybrid thermal cycle with independent refrigeration loop |
| US9297387B2 (en) | 2013-04-09 | 2016-03-29 | Harris Corporation | System and method of controlling wrapping flow in a fluid working apparatus |
| US9303533B2 (en) | 2013-12-23 | 2016-04-05 | Harris Corporation | Mixing assembly and method for combining at least two working fluids |
| US9303514B2 (en) | 2013-04-09 | 2016-04-05 | Harris Corporation | System and method of utilizing a housing to control wrapping flow in a fluid working apparatus |
| CN105569754A (en) * | 2014-09-26 | 2016-05-11 | 余义刚 | A method of using ambient heat energy to do work externally and a system for doing work with ambient heat energy |
| US9574563B2 (en) | 2013-04-09 | 2017-02-21 | Harris Corporation | System and method of wrapping flow in a fluid working apparatus |
| US20170058714A1 (en) * | 2015-08-24 | 2017-03-02 | Saudi Arabian Oil Company | Power Generation from Waste Heat in Integrated Crude Oil Refining and Aromatics Facilities |
| US9670836B2 (en) * | 2013-07-09 | 2017-06-06 | Volkswagen Aktiengesellschaft | Drive unit for a motor vehicle |
| US9725652B2 (en) | 2015-08-24 | 2017-08-08 | Saudi Arabian Oil Company | Delayed coking plant combined heating and power generation |
| US9745871B2 (en) | 2015-08-24 | 2017-08-29 | Saudi Arabian Oil Company | Kalina cycle based conversion of gas processing plant waste heat into power |
| US9803507B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation using independent dual organic Rankine cycles from waste heat systems in diesel hydrotreating-hydrocracking and continuous-catalytic-cracking-aromatics facilities |
| US9803513B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated aromatics, crude distillation, and naphtha block facilities |
| US9803511B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation using independent dual organic rankine cycles from waste heat systems in diesel hydrotreating-hydrocracking and atmospheric distillation-naphtha hydrotreating-aromatics facilities |
| US9803505B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated aromatics and naphtha block facilities |
| US9803506B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated crude oil hydrocracking and aromatics facilities |
| US9803508B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated crude oil diesel hydrotreating and aromatics facilities |
| US9816401B2 (en) | 2015-08-24 | 2017-11-14 | Saudi Arabian Oil Company | Modified Goswami cycle based conversion of gas processing plant waste heat into power and cooling |
| US20190234343A1 (en) * | 2018-01-30 | 2019-08-01 | International Engine Intellectual Property Company, Llc. | Organic rankine cycle waste heat recovery system having two loops |
| US10472992B2 (en) | 2013-09-05 | 2019-11-12 | Enviro Power LLC | On-demand steam generator and control system |
| US10598049B2 (en) | 2017-10-03 | 2020-03-24 | Enviro Power, Inc. | Evaporator with integrated heat recovery |
| US10862370B2 (en) * | 2018-03-01 | 2020-12-08 | Takaitsu Kobayashi | Working medium property difference power generation system and working medium property difference power generation method that uses the power generation system |
| US11204190B2 (en) | 2017-10-03 | 2021-12-21 | Enviro Power, Inc. | Evaporator with integrated heat recovery |
| US11261760B2 (en) | 2013-09-05 | 2022-03-01 | Enviro Power, Inc. | On-demand vapor generator and control system |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3943719A (en) * | 1975-02-26 | 1976-03-16 | Terry Lynn E | Hydride-dehydride power system and methods |
| US4033135A (en) * | 1975-02-07 | 1977-07-05 | Sulzer Brothers Limited | Plant and process for vaporizing and heating liquid natural gas |
| US4050252A (en) * | 1976-01-23 | 1977-09-27 | Hitachi Shipbuilding & Engineering Co., Ltd. | Ocean nuclear power equipment |
| US4070862A (en) * | 1976-09-24 | 1978-01-31 | E. I. Du Pont De Nemours And Company | Cascaded two-fluid rotary closed Rankine cycle engine |
| US4407131A (en) * | 1980-08-13 | 1983-10-04 | Battelle Development Corporation | Cogeneration energy balancing system |
| US4422298A (en) * | 1977-12-29 | 1983-12-27 | Reikichi Nozawa | Liquefied natural gas-freon electricity generation system |
| US4444015A (en) * | 1981-01-27 | 1984-04-24 | Chiyoda Chemical Engineering & Construction Co., Ltd. | Method for recovering power according to a cascaded Rankine cycle by gasifying liquefied natural gas and utilizing the cold potential |
| US4760705A (en) * | 1983-05-31 | 1988-08-02 | Ormat Turbines Ltd. | Rankine cycle power plant with improved organic working fluid |
| US5497624A (en) * | 1988-12-02 | 1996-03-12 | Ormat, Inc. | Method of and apparatus for producing power using steam |
| US6167706B1 (en) * | 1996-01-31 | 2001-01-02 | Ormat Industries Ltd. | Externally fired combined cycle gas turbine |
| US20030005696A1 (en) * | 2000-10-18 | 2003-01-09 | Wilson Benjamin Raymond | Internal combustion engine energy extraction devices |
| US20030213246A1 (en) * | 2002-05-15 | 2003-11-20 | Coll John Gordon | Process and device for controlling the thermal and electrical output of integrated micro combined heat and power generation systems |
| US20030213245A1 (en) * | 2002-05-15 | 2003-11-20 | Yates Jan B. | Organic rankine cycle micro combined heat and power system |
| US6960839B2 (en) * | 2000-07-17 | 2005-11-01 | Ormat Technologies, Inc. | Method of and apparatus for producing power from a heat source |
| US20080168772A1 (en) * | 2005-03-29 | 2008-07-17 | Utc Power, Llc | Cascaded Organic Rankine Cycles for Waste Heat Utilization |
| US20090000299A1 (en) * | 2007-06-29 | 2009-01-01 | General Electric Company | System and method for recovering waste heat |
-
2009
- 2009-03-30 US US12/413,920 patent/US20100242476A1/en not_active Abandoned
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4033135A (en) * | 1975-02-07 | 1977-07-05 | Sulzer Brothers Limited | Plant and process for vaporizing and heating liquid natural gas |
| US3943719A (en) * | 1975-02-26 | 1976-03-16 | Terry Lynn E | Hydride-dehydride power system and methods |
| US4050252A (en) * | 1976-01-23 | 1977-09-27 | Hitachi Shipbuilding & Engineering Co., Ltd. | Ocean nuclear power equipment |
| US4070862A (en) * | 1976-09-24 | 1978-01-31 | E. I. Du Pont De Nemours And Company | Cascaded two-fluid rotary closed Rankine cycle engine |
| US4422298A (en) * | 1977-12-29 | 1983-12-27 | Reikichi Nozawa | Liquefied natural gas-freon electricity generation system |
| US4407131A (en) * | 1980-08-13 | 1983-10-04 | Battelle Development Corporation | Cogeneration energy balancing system |
| US4444015A (en) * | 1981-01-27 | 1984-04-24 | Chiyoda Chemical Engineering & Construction Co., Ltd. | Method for recovering power according to a cascaded Rankine cycle by gasifying liquefied natural gas and utilizing the cold potential |
| US4760705A (en) * | 1983-05-31 | 1988-08-02 | Ormat Turbines Ltd. | Rankine cycle power plant with improved organic working fluid |
| US5497624A (en) * | 1988-12-02 | 1996-03-12 | Ormat, Inc. | Method of and apparatus for producing power using steam |
| US6167706B1 (en) * | 1996-01-31 | 2001-01-02 | Ormat Industries Ltd. | Externally fired combined cycle gas turbine |
| US6960839B2 (en) * | 2000-07-17 | 2005-11-01 | Ormat Technologies, Inc. | Method of and apparatus for producing power from a heat source |
| US20030005696A1 (en) * | 2000-10-18 | 2003-01-09 | Wilson Benjamin Raymond | Internal combustion engine energy extraction devices |
| US20030213246A1 (en) * | 2002-05-15 | 2003-11-20 | Coll John Gordon | Process and device for controlling the thermal and electrical output of integrated micro combined heat and power generation systems |
| US20030213245A1 (en) * | 2002-05-15 | 2003-11-20 | Yates Jan B. | Organic rankine cycle micro combined heat and power system |
| US20080168772A1 (en) * | 2005-03-29 | 2008-07-17 | Utc Power, Llc | Cascaded Organic Rankine Cycles for Waste Heat Utilization |
| US20090000299A1 (en) * | 2007-06-29 | 2009-01-01 | General Electric Company | System and method for recovering waste heat |
Cited By (75)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8459030B2 (en) | 2009-09-30 | 2013-06-11 | General Electric Company | Heat engine and method for operating the same |
| US20110072820A1 (en) * | 2009-09-30 | 2011-03-31 | General Electric Company | Heat engine and method for operating the same |
| WO2012054049A1 (en) * | 2010-10-22 | 2012-04-26 | General Electric Company | Heat engine and method for operating the same |
| CN102454441A (en) * | 2010-10-29 | 2012-05-16 | 通用电气公司 | Rankine cycle integrated with absorption chiller |
| JP2012163093A (en) * | 2010-11-19 | 2012-08-30 | General Electric Co <Ge> | Rankine cycle integrated with organic rankine cycle and absorption chiller cycle |
| DE202011109771U1 (en) | 2011-02-10 | 2012-03-21 | Voith Patent Gmbh | Stationary power plant, in particular gas power plant, for power generation |
| DE102011010974A1 (en) * | 2011-02-10 | 2012-08-16 | Voith Patent Gmbh | Stationary power plant, in particular gas power plant, for power generation |
| US9030034B2 (en) | 2011-02-10 | 2015-05-12 | Steamdrive Gmbh | Stationary power plant, in particular a gas power plant, for generating electricity |
| US8650879B2 (en) | 2011-04-20 | 2014-02-18 | General Electric Company | Integration of waste heat from charge air cooling into a cascaded organic rankine cycle system |
| US8991181B2 (en) * | 2011-05-02 | 2015-03-31 | Harris Corporation | Hybrid imbedded combined cycle |
| US20120279220A1 (en) * | 2011-05-02 | 2012-11-08 | Harris Corporation | Hybrid imbedded combined cycle |
| US8997490B2 (en) | 2012-02-02 | 2015-04-07 | Electratherm, Inc. | Heat utilization in ORC systems |
| US9038389B2 (en) | 2012-06-26 | 2015-05-26 | Harris Corporation | Hybrid thermal cycle with independent refrigeration loop |
| EP2733339A1 (en) * | 2012-11-20 | 2014-05-21 | IAV GmbH Ingenieurgesellschaft Auto und Verkehr | Device for utilisation of the waste heat of an internal combustion engine |
| US9297387B2 (en) | 2013-04-09 | 2016-03-29 | Harris Corporation | System and method of controlling wrapping flow in a fluid working apparatus |
| US9303514B2 (en) | 2013-04-09 | 2016-04-05 | Harris Corporation | System and method of utilizing a housing to control wrapping flow in a fluid working apparatus |
| US9574563B2 (en) | 2013-04-09 | 2017-02-21 | Harris Corporation | System and method of wrapping flow in a fluid working apparatus |
| US20140352306A1 (en) * | 2013-05-30 | 2014-12-04 | General Electric Company | System and method of waste heat recovery |
| US9593597B2 (en) * | 2013-05-30 | 2017-03-14 | General Electric Company | System and method of waste heat recovery |
| US9670836B2 (en) * | 2013-07-09 | 2017-06-06 | Volkswagen Aktiengesellschaft | Drive unit for a motor vehicle |
| US11261760B2 (en) | 2013-09-05 | 2022-03-01 | Enviro Power, Inc. | On-demand vapor generator and control system |
| US10472992B2 (en) | 2013-09-05 | 2019-11-12 | Enviro Power LLC | On-demand steam generator and control system |
| US9303533B2 (en) | 2013-12-23 | 2016-04-05 | Harris Corporation | Mixing assembly and method for combining at least two working fluids |
| CN105569754A (en) * | 2014-09-26 | 2016-05-11 | 余义刚 | A method of using ambient heat energy to do work externally and a system for doing work with ambient heat energy |
| US9828885B2 (en) | 2015-08-24 | 2017-11-28 | Saudi Arabian Oil Company | Modified Goswami cycle based conversion of gas processing plant waste heat into power and cooling with flexibility |
| US10125640B2 (en) | 2015-08-24 | 2018-11-13 | Saudi Arabian Oil Company | Modified goswami cycle based conversion of gas processing plant waste heat into power and cooling with flexibility |
| US9803509B2 (en) * | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated crude oil refining and aromatics facilities |
| US9803507B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation using independent dual organic Rankine cycles from waste heat systems in diesel hydrotreating-hydrocracking and continuous-catalytic-cracking-aromatics facilities |
| US9803513B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated aromatics, crude distillation, and naphtha block facilities |
| US9803511B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation using independent dual organic rankine cycles from waste heat systems in diesel hydrotreating-hydrocracking and atmospheric distillation-naphtha hydrotreating-aromatics facilities |
| US9803505B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated aromatics and naphtha block facilities |
| US9803506B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated crude oil hydrocracking and aromatics facilities |
| US9803930B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated hydrocracking and diesel hydrotreating facilities |
| US9803508B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated crude oil diesel hydrotreating and aromatics facilities |
| US9816759B2 (en) | 2015-08-24 | 2017-11-14 | Saudi Arabian Oil Company | Power generation using independent triple organic rankine cycles from waste heat in integrated crude oil refining and aromatics facilities |
| US9816401B2 (en) | 2015-08-24 | 2017-11-14 | Saudi Arabian Oil Company | Modified Goswami cycle based conversion of gas processing plant waste heat into power and cooling |
| US9745871B2 (en) | 2015-08-24 | 2017-08-29 | Saudi Arabian Oil Company | Kalina cycle based conversion of gas processing plant waste heat into power |
| US9845995B2 (en) | 2015-08-24 | 2017-12-19 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US9845996B2 (en) | 2015-08-24 | 2017-12-19 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US9851153B2 (en) | 2015-08-24 | 2017-12-26 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US9869209B2 (en) | 2015-08-24 | 2018-01-16 | Saudi Arabian Oil Company | Kalina cycle based conversion of gas processing plant waste heat into power |
| US9879918B2 (en) | 2015-08-24 | 2018-01-30 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US9891004B2 (en) | 2015-08-24 | 2018-02-13 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US9915477B2 (en) | 2015-08-24 | 2018-03-13 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US10113448B2 (en) | 2015-08-24 | 2018-10-30 | Saudi Arabian Oil Company | Organic Rankine cycle based conversion of gas processing plant waste heat into power |
| US10113805B2 (en) | 2015-08-24 | 2018-10-30 | Saudi Arabian Oil Company | Systems for recovery and re-use of waste energy in hydrocracking-based configuration for integrated crude oil refining and aromatics complex |
| US10119764B2 (en) | 2015-08-24 | 2018-11-06 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US10125639B2 (en) | 2015-08-24 | 2018-11-13 | Saudi Arabian Oil Company | Organic Rankine cycle based conversion of gas processing plant waste heat into power and cooling |
| US10126067B2 (en) | 2015-08-24 | 2018-11-13 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US9803145B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated crude oil refining, aromatics, and utilities facilities |
| US10174640B1 (en) | 2015-08-24 | 2019-01-08 | Saudi Arabian Oil Company | Modified Goswami cycle based conversion of gas processing plant waste heat into power and cooling with flexibility |
| US10227899B2 (en) | 2015-08-24 | 2019-03-12 | Saudi Arabian Oil Company | Organic rankine cycle based conversion of gas processing plant waste heat into power and cooling |
| US10301977B2 (en) | 2015-08-24 | 2019-05-28 | Saudi Arabian Oil Company | Kalina cycle based conversion of gas processing plant waste heat into power |
| US20170058714A1 (en) * | 2015-08-24 | 2017-03-02 | Saudi Arabian Oil Company | Power Generation from Waste Heat in Integrated Crude Oil Refining and Aromatics Facilities |
| US10385275B2 (en) | 2015-08-24 | 2019-08-20 | Saudi Arabian Oil Company | Delayed coking plant combined heating and power generation |
| US10429135B2 (en) | 2015-08-24 | 2019-10-01 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US10436517B2 (en) | 2015-08-24 | 2019-10-08 | Saudi Arabian Oil Company | Systems for recovery and re-use of waste energy in hydrocracking-based configuration for integrated crude oil refining and aromatics complex |
| US10443946B2 (en) | 2015-08-24 | 2019-10-15 | Saudi Arabian Oil Company | Systems for recovery and re-use of waste energy in crude oil refining and aromatics complex |
| US9725652B2 (en) | 2015-08-24 | 2017-08-08 | Saudi Arabian Oil Company | Delayed coking plant combined heating and power generation |
| US10480352B2 (en) | 2015-08-24 | 2019-11-19 | Saudi Arabian Oil Company | Organic Rankine cycle based conversion of gas processing plant waste heat into power and cooling |
| US10480864B2 (en) | 2015-08-24 | 2019-11-19 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US10502495B2 (en) | 2015-08-24 | 2019-12-10 | Saudi Arabian Oil Company | Systems for recovery and re-use of waste energy in crude oil refining facility and aromatics complex |
| US10502494B2 (en) | 2015-08-24 | 2019-12-10 | Saudi Arabian Oil Company | Systems for recovery and re-use of waste energy in crude oil refining facility and aromatics complex through simultaneous intra-plant integration and plants' thermal coupling |
| US10577981B2 (en) | 2015-08-24 | 2020-03-03 | Saudi Arabian Oil Company | Modified Goswami cycle based conversion of gas processing plant waste heat into power and cooling |
| US11073050B2 (en) | 2015-08-24 | 2021-07-27 | Saudi Arabian Oil Company | Kalina cycle based conversion of gas processing plant waste heat into power |
| US10767932B2 (en) | 2015-08-24 | 2020-09-08 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US10801785B2 (en) | 2015-08-24 | 2020-10-13 | Saudi Arabian Oil Company | Recovery and re-use of waste energy in industrial facilities |
| US10995636B2 (en) | 2015-08-24 | 2021-05-04 | Saudi Arabian Oil Company | Organic Rankine cycle based conversion of gas processing plant waste heat into power |
| US10927305B2 (en) | 2015-08-24 | 2021-02-23 | Saudi Arabian Oil Company | Delayed coking plant combined heating and power generation |
| US10961460B2 (en) | 2015-08-24 | 2021-03-30 | Saudi Arabian Oil Company | Delayed coking plant combined heating and power generation |
| US10961873B2 (en) | 2015-08-24 | 2021-03-30 | Saudi Arabian Oil Company | Power generation from waste energy in industrial facilities |
| US10598049B2 (en) | 2017-10-03 | 2020-03-24 | Enviro Power, Inc. | Evaporator with integrated heat recovery |
| US11204190B2 (en) | 2017-10-03 | 2021-12-21 | Enviro Power, Inc. | Evaporator with integrated heat recovery |
| US20190234343A1 (en) * | 2018-01-30 | 2019-08-01 | International Engine Intellectual Property Company, Llc. | Organic rankine cycle waste heat recovery system having two loops |
| US10862370B2 (en) * | 2018-03-01 | 2020-12-08 | Takaitsu Kobayashi | Working medium property difference power generation system and working medium property difference power generation method that uses the power generation system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20100242476A1 (en) | Combined heat and power cycle system | |
| US8561405B2 (en) | System and method for recovering waste heat | |
| US20100326076A1 (en) | Optimized system for recovering waste heat | |
| US20100319346A1 (en) | System for recovering waste heat | |
| US20100146974A1 (en) | System for recovering waste heat | |
| US8302399B1 (en) | Organic rankine cycle systems using waste heat from charge air cooling | |
| US20100242479A1 (en) | Tri-generation system using cascading organic rankine cycle | |
| JP5567961B2 (en) | Double reheat Rankine cycle system and method | |
| CN101248253B (en) | Cascade Organic Rankine Cycle Using Waste Heat | |
| US8650879B2 (en) | Integration of waste heat from charge air cooling into a cascaded organic rankine cycle system | |
| EP2834477B1 (en) | System and method for recovery of waste heat from dual heat sources | |
| US20110083437A1 (en) | Rankine cycle system | |
| CN104895630A (en) | Different evaporation temperature based multistage organic Rankine cycle (ORC) power generation system | |
| Kim et al. | Thermodynamic analysis of a dual loop cycle coupled with a marine gas turbine for waste heat recovery system using low global warming potential working fluids | |
| KR20070116106A (en) | Cascaded Organic Rankine Cycle to Use Waste Heat |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: GENERAL ELECTRIC COMPANY, NEW YORK Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:AST, GABOR;FREY, THOMAS JOHANNES;HUCK, PIERRE SEBASTIEN;AND OTHERS;REEL/FRAME:022469/0221 Effective date: 20090330 |
|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |