CN203518328U - Compressed gas distribution type energy system using rare gas as working media - Google Patents
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Abstract
Description
技术领域 technical field
本实用新型涉及储能技术与分布式供能技术领域,具体的说,是一种以压缩空气储能技术为基础,利用稀有气体的跨临界特性实现以供热、冷为主,供电为辅的分布式能源系统。 The utility model relates to the field of energy storage technology and distributed energy supply technology. Specifically, it is based on compressed air energy storage technology and utilizes the transcritical characteristics of rare gases to realize heating and cooling as main and power supply as auxiliary. distributed energy system. the
背景技术 Background technique
电、热、冷是维持人类社会发展和进步的三种重要的能量形式。一般而言,电能是人类社会最核心的能源,同时也是供应量最为充足的能量形式,电能不仅可以直接供应用户,还可以利用其他装置转化为热能或者冷能。而随着人类生活水平的提高,人类对生活舒适度的要求升高,因此对热和冷的需求急剧增加。虽然电能可转化为热能或冷能,但该过程造成的能量品位的降低造成了能源的严重浪费。因此,优先考虑满足用户的热能和冷能需求是未来分布式供能系统能源利用的一项重要目标。 Electricity, heat, and cold are three important forms of energy that maintain the development and progress of human society. Generally speaking, electric energy is the core energy source of human society, and it is also the form of energy with the most abundant supply. Electric energy can not only be directly supplied to users, but also be converted into heat or cold energy by using other devices. With the improvement of human living standards, human beings have higher requirements for living comfort, so the demand for heat and cold has increased dramatically. Although electric energy can be converted into heat energy or cold energy, the reduction of energy grade caused by this process has caused serious waste of energy. Therefore, giving priority to satisfying users' heating and cooling needs is an important goal of energy utilization in future distributed energy supply systems. the
压缩空气储能技术是上世纪五六十年代发展起来的一种以燃气轮机技术为基础的能量存储技术,目前已被一些学者发掘出其用于分布式供能领域的潜力。主要的方法是将空气进行压缩,利用化石燃料加热压缩空气完成膨胀做功发电,透平机出口温度较高的空气(400-600K)分别进行制冷和供热。该方式有效利用了透平机出口空气的废热,减少了能量的浪费,提高了系统的整体效率。但其对化石燃料的利用也不可避免地造成了环境污染问题。因此,如何减少或避免储能系统对化石能源的利用而实现冷热电联供也是储能技术未来发展的一个重要方向。 Compressed air energy storage technology is an energy storage technology based on gas turbine technology developed in the 1950s and 1960s. It has been discovered by some scholars for its potential in the field of distributed energy supply. The main method is to compress the air, use fossil fuels to heat the compressed air to complete expansion and power generation, and the air with a higher temperature (400-600K) at the outlet of the turbine is used for cooling and heating respectively. This method effectively utilizes the waste heat of the outlet air of the turbine, reduces energy waste, and improves the overall efficiency of the system. However, the use of fossil fuels inevitably causes environmental pollution. Therefore, how to reduce or avoid the use of fossil energy by the energy storage system and realize the combined cooling, heating and power supply is also an important direction for the future development of energy storage technology. the
在传统的压缩空气储能技术中,压气机对空气进行压缩时会产生过程 热,但该部分热量一般都被冷却水带走而浪费掉;若将压力较高,温度较低的空气进行膨胀,不仅可以得到一定的电量输出,同时膨胀机出口空气温度较低,理论上可用于制冷。因此压缩空气储能技术存在不利用化石燃料而实现冷热电联供的可能性。不过,对于压缩空气储能技术的介质——空气而言,其来源方便,储量充足,且有一定的可压缩性,但由于其密度较小,临界压力、温度较高,当需要压缩至较高压力时会造成透平机械的设计复杂化和困难化,而在未达到超临界状态下需要的存储容积亦较大,因此造成储能系统设计困难、成本较高。同时由于空气内部组分复杂,在以低温状态下进行膨胀制冷时容易出现液化和组分分离情况,影响系统的运行安全,这是以空气为存储介质进行冷热电联供的压缩空气储能系统面临的主要问题。因此,如果储能技术能以密度较大,且容易实现超临界状态的纯气体为工质,就可以避免上述问题的发生。 In the traditional compressed air energy storage technology, when the compressor compresses the air, it will generate process heat, but this part of the heat is generally taken away by the cooling water and wasted; if the air with higher pressure and lower temperature is expanded , not only can get a certain power output, but at the same time the outlet air temperature of the expander is low, which can be used for refrigeration in theory. Therefore, compressed air energy storage technology has the possibility of realizing cogeneration of cooling, heating and power without using fossil fuels. However, for the medium of compressed air energy storage technology—air, its source is convenient, its reserves are sufficient, and it has certain compressibility. However, due to its low density, high critical pressure and high temperature, when it needs to be compressed to When the pressure is high, the design of the turbomachinery will be complicated and difficult, and the storage volume required under the supercritical state is also large, so the design of the energy storage system is difficult and the cost is high. At the same time, due to the complex internal components of the air, liquefaction and component separation are prone to occur when expansion refrigeration is performed at low temperature, which affects the operation safety of the system. This is a compressed air energy storage system that uses air as the storage medium for combined cooling, heating and power supply. The main problem facing the system. Therefore, if the energy storage technology can use pure gas with high density and easy to achieve supercritical state as the working medium, the above problems can be avoided. the
以稀有气体为代表的惰性气体是满足上述要求的一种工质选择。稀有气体一般利用空气分离技术作为副产物从空气中分离,在常温和常压下稀有气体均无色、无味、无臭,化学性质几乎都是惰性的,其临界参数如表1中所示。可以看出,稀有气体的临界压力较小,当压缩至60atm且温度为环境温度时,稀有气体即可变为超临界状态,其密度也比同状态下的压缩空气大几十倍至几百倍,同时兼有气体和液体的双重特性,具有更好的流动性和传输特性。考虑到稀有气体的上述优秀的物理和化学特性,当以压缩空气储能技术为基础,以任意一种稀有气体为存储介质时,不仅可以利用稀有气体的高密度特性降低如透平机械、换热器、储气罐等系统核心部件的设计难度,减小储能系统的存储规模,大大降低系统的研发成本与维护成本,还也可以避免低温空气膨胀造成的空气液化和组分分离问题进一步增强系统的安全性和可操作性。 Inert gases represented by rare gases are a choice of working fluids to meet the above requirements. Rare gases are generally separated from the air as a by-product by air separation technology. Rare gases are colorless, tasteless, and odorless at normal temperature and pressure, and are almost inert in chemical properties. Their critical parameters are shown in Table 1. It can be seen that the critical pressure of the rare gas is small. When compressed to 60 atm and the temperature is the ambient temperature, the rare gas can become a supercritical state, and its density is tens to hundreds of times higher than that of compressed air in the same state. times, it has the dual characteristics of gas and liquid, and has better fluidity and transmission characteristics. Considering the above-mentioned excellent physical and chemical properties of rare gases, when any kind of rare gas is used as the storage medium based on compressed air energy storage technology, not only can the high-density characteristics of rare gases be used to reduce the The design difficulty of the core components of the system such as heaters and gas storage tanks reduces the storage scale of the energy storage system, greatly reduces the research and development costs and maintenance costs of the system, and can also avoid the problems of air liquefaction and component separation caused by low-temperature air expansion. Enhance system security and operability. the
表1惰性气体临界参数 Table 1 Critical parameters of inert gas
综上,本系统针对上述问题,实现以压缩空气储能技术为基础,利用稀有气体的跨临界特性实现以供热、冷为主,供电为辅的分布式能源系统。 To sum up, in view of the above problems, this system realizes a distributed energy system based on compressed air energy storage technology and using the transcritical characteristics of rare gases to provide heat and cold as the main and power supply as the auxiliary. the
发明内容 Contents of the invention
本实用新型涉及一种以任意一种稀有气体为存储介质的压缩气体分布式能源系统,分别利用稀有气体的压缩过程和膨胀过程完成热量存储和冷量存储,并输出一定电量,解决用户对热、冷、电的需求,同时系统不需要使用化石燃料,不产生温室气体及硫化物、氮化物等污染性气体。 The utility model relates to a compressed gas distributed energy system using any rare gas as a storage medium, which uses the compression process and expansion process of the rare gas to complete heat storage and cold storage respectively, and outputs a certain amount of electricity to solve the user's problem of heat , cooling, and electricity requirements, and the system does not need to use fossil fuels, and does not produce greenhouse gases, sulfides, nitrides and other polluting gases. the
本实用新型为解决其技术问题所采取的技术方案是: The technical scheme that the utility model takes for solving its technical problem is:
一种以稀有气体为存储介质的压缩气体分布式能源系统,包括:稀有气体供应单元、稀有气体压缩储能单元、稀有气体膨胀释能单元、载热介质循环回路,其特征在于, A compressed gas distributed energy system using a rare gas as a storage medium, including: a rare gas supply unit, a rare gas compression energy storage unit, a rare gas expansion energy release unit, and a heat-carrying medium circulation loop, characterized in that,
所述稀有气体供应单元包括常压稀有气体存储器; The rare gas supply unit includes a normal pressure rare gas storage;
所述稀有气体压缩储能单元包括低压级压气机、中压级压气机、高压级压气机及高压气体储气罐,其中, The rare gas compression energy storage unit includes a low-pressure compressor, a medium-pressure compressor, a high-pressure compressor and a high-pressure gas storage tank, wherein,
--所述低压级压气机的进气口通过管路与所述常压稀有气体存储器的出气 口连通,所述低压级压气机产生的高压气体穿过低压级冷却器的热流体侧后,一部分经带有压缩端低压级开关阀的气体管路通入所述高压气体储气罐,另一部分经带有压缩端低压级速启/速关阀的气体管路通入所述中压级压气机的进气口; --The air inlet of the low-pressure stage compressor communicates with the gas outlet of the atmospheric pressure rare gas storage through a pipeline, and after the high-pressure gas produced by the low-pressure stage compressor passes through the thermal fluid side of the low-pressure stage cooler, One part is led into the high-pressure gas storage tank through the gas pipeline with the low-pressure stage switch valve at the compression end, and the other part is led into the medium-pressure stage through the gas pipeline with the low-pressure stage quick-open/quick-off valve at the compression end. Air intake of the compressor;
--所述中压级压气机产生的高压气体穿过中压级冷却器的热流体侧后,一部分经带有压缩端中压级开关阀的气体管路通入所述高压气体储气罐,另一部分经带有压缩端中压级速启/速关阀的气体管路通入所述高压级压气机的进气口; --After the high-pressure gas produced by the medium-pressure compressor passes through the hot fluid side of the medium-pressure cooler, part of it passes through the gas pipeline with the medium-pressure switch valve at the compression end and enters the high-pressure gas storage tank , the other part leads to the air inlet of the high-pressure compressor through a gas pipeline with a medium-pressure quick-opening/quick-closing valve at the compression end;
--所述高压级压气机产生的高压气体穿过高压级冷却器的热流体侧后,经带有压缩端高压级开关阀的气体管路通入所述高压气体储气罐; --After the high-pressure gas produced by the high-pressure compressor passes through the hot fluid side of the high-pressure cooler, it is passed into the high-pressure gas storage tank through a gas pipeline with a high-pressure switch valve at the compression end;
所述稀有气体膨胀释能单元包括高压级膨胀机、中压级膨胀机及低压级膨胀机,其中, The rare gas expansion energy release unit includes a high-pressure expander, a medium-pressure expander and a low-pressure expander, wherein,
--所述高压气体储气罐储存的高压气体,一部分经设有膨胀端高压级开关阀的气体管路通入高压级换热器的冷流体侧后通入所述高压级膨胀机,另一部分经设有膨胀端高压级速启/速关阀的气体管路通入所述高压级膨胀机; --A part of the high-pressure gas stored in the high-pressure gas storage tank is passed into the cold fluid side of the high-pressure heat exchanger through the gas pipeline provided with a high-pressure switch valve at the expansion end, and then passed into the high-pressure expander; A part of the gas pipeline is provided with a high-pressure stage quick-opening/quick-closing valve at the expansion end and enters the high-pressure stage expander;
--所述高压级膨胀机膨胀后的气体,一部分经带有膨胀端中压级开关阀的气体管路通入储冷罐,另一部分经带有膨胀端中压级速启/速关阀的气体管路通入中压级换热器的冷流体侧后进入所述中压级膨胀机, --A part of the gas expanded by the high-pressure expander enters the cold storage tank through a gas pipeline with a medium-pressure on-off valve at the expansion end, and the other part passes through a medium-pressure quick-open/quick-off valve with an expansion end The gas pipeline of the medium pressure stage enters the cold fluid side of the medium pressure heat exchanger and then enters the medium pressure stage expander,
--所述中压级膨胀机膨胀后的气体,一部分经带有膨胀端低压级开关阀的气体管路通入储冷罐,另一部分经带有膨胀端低压级速启/速关阀的气体管路通入低压级换热器的冷流体侧后进入所述低压级膨胀机, --A part of the gas expanded by the medium-pressure expander enters the cold storage tank through the gas pipeline with the low-pressure on-off valve at the expansion end, and the other part passes through the gas pipeline with the low-pressure quick-open/quick-off valve at the expansion end The gas pipeline leads to the cold fluid side of the low-pressure stage heat exchanger and then enters the low-pressure stage expander,
--所述低压级膨胀机膨胀后的气体通过储冷罐后流入常压稀有气体存储器; --The gas expanded by the low-pressure stage expander flows into the normal-pressure rare gas storage after passing through the cold storage tank;
所述载热介质循环回路包括载热介质供应罐、储热罐,所述载热介质供应罐中的载热介质经管路分别通入低压级冷却器、中压级冷却器、高压级冷却器的冷流体侧后进入所述储热罐,所述储热罐中的载热介质经管路分别通入高压 级换热器、中压级换热器、低压级换热器的热流体侧后进入所述载热介质供应罐。 The heat-carrying medium circulation loop includes a heat-carrying medium supply tank and a heat storage tank, and the heat-carrying medium in the heat-carrying medium supply tank is respectively fed into the low-pressure stage cooler, the medium-pressure stage cooler, and the high-pressure stage cooler through pipelines. The cold fluid side of the heat storage tank enters the heat storage tank, and the heat transfer medium in the heat storage tank is respectively passed through the pipeline to the hot fluid side of the high-pressure heat exchanger, medium-pressure heat exchanger, and low-pressure heat exchanger. Enter the heat transfer medium supply tank. the
进一步地,所述载热介质供应罐通过一共同的低温载热介质供应管路将载热介质分送至低压级冷却器、中压级冷却器、高压级冷却器的冷流体侧,位于所述低压级冷却器和中压级冷却器之间的供应管路上设有中压级冷却器开关阀,位于所述中压级冷却器和高压级冷却器之间的供应管路上设有高压级冷却器开关阀。 Further, the heat-carrying medium supply tank distributes the heat-carrying medium to the cold fluid side of the low-pressure stage cooler, the medium-pressure stage cooler, and the high-pressure stage cooler through a common low-temperature heat-carrying medium supply pipeline, and is located at the A medium-pressure stage cooler switch valve is provided on the supply pipeline between the low-pressure stage cooler and the medium-pressure stage cooler, and a high-pressure stage is provided on the supply pipeline between the medium-pressure stage cooler and the high-pressure stage cooler. Cooler switch valve. the
进一步地,所述储热罐通过一共同的高温载热介质供应管路将载热介质分送至高压级换热器、中压级换热器、低压级换热器的热流体侧,所述供应管路上串接有高压级换热器开关阀、中压级换热器开关阀、低压级换热器开关阀,其中,所述高压级换热器开关阀设置在所述储热罐和高压级换热器之间的供应管路上,所述中压级换热器开关阀设置在所述高压级换热器和中压级换热器之间的供应管路上,所述低压级换热器开关阀设置在所述中压级换热器和低压级换热器之间的供应管路上。 Further, the heat storage tank distributes the heat-carrying medium to the hot fluid side of the high-pressure stage heat exchanger, the medium-pressure stage heat exchanger, and the low-pressure stage heat exchanger through a common high-temperature heat-carrying medium supply pipeline, so The supply pipeline is connected in series with a high-pressure heat exchanger on-off valve, a medium-pressure heat exchanger on-off valve, and a low-pressure heat exchanger on-off valve, wherein the high-pressure heat exchanger on-off valve is arranged in the heat storage tank On the supply pipeline between the high-pressure stage heat exchanger and the high-pressure stage heat exchanger, the medium-pressure stage heat exchanger switch valve is set on the supply pipeline between the high-pressure stage heat exchanger and the medium-pressure stage heat exchanger, and the low-pressure stage A heat exchanger switch valve is provided on the supply line between the medium-pressure stage heat exchanger and the low-pressure stage heat exchanger. the
进一步地,所述储热罐用以向用热单元供应热量,所述用热单元包括通过管路依次连接的热用户、用热端载热介质供应罐、用热端开关阀,其中,热用户和用热端开关阀之间的用热管路上设有穿过所述储热罐部分的用热换热部件。 Further, the heat storage tank is used to supply heat to the heat-using unit, and the heat-using unit includes heat users connected in sequence through pipelines, a heat-carrying medium supply tank at the heat-using end, and a switch valve at the heat-using end. The heat utilization and heat exchange components passing through the heat storage tank are arranged on the heat utilization pipeline between the user and the heat utilization end switch valve. the
进一步地,所述用热单元还包括用热端控制系统,用以控制调节用热端开关阀的开度和热用户的用热量。 Further, the heat consumption unit also includes a heat consumption end control system, which is used to control the opening degree of the on-off valve of the heat consumption end and the heat consumption of heat users. the
进一步地,所述低压级冷却器的热流体侧出口处的管路上设有压缩端低压级止回阀。 Further, a low-pressure stage check valve at the compression end is provided on the pipeline at the hot fluid side outlet of the low-pressure stage cooler. the
进一步地,所述中压级冷却器的热流体侧出口处的管路上设有压缩端中压级止回阀。 Further, an intermediate pressure check valve at the compression end is provided on the pipeline at the hot fluid side outlet of the intermediate pressure cooler. the
进一步地,所述高压级冷却器的热流体侧出口处的管路上设有压缩端高压级止回阀。 Further, a high pressure stage check valve at the compression end is provided on the pipeline at the hot fluid side outlet of the high pressure stage cooler. the
进一步地,所述高压气体储气罐的进气口处的管路上设有安全阀。 Further, a safety valve is provided on the pipeline at the air inlet of the high-pressure gas storage tank. the
进一步地,所述高压气体储气罐的出气口处的管路上设有膨胀端高压级止回阀。 Further, a high-pressure check valve at the expansion end is provided on the pipeline at the gas outlet of the high-pressure gas storage tank. the
进一步地,所述高压级膨胀机的出气口处的管路上设有膨胀端中压级止回阀。 Further, a middle-pressure check valve at the expansion end is provided on the pipeline at the gas outlet of the high-pressure expander. the
进一步地,所述中压级膨胀机的出气口处的管路上设有膨胀端低压级止回阀。 Further, a low-pressure check valve at the expansion end is provided on the pipeline at the gas outlet of the medium-pressure expander. the
进一步地,所述储冷罐和稀有气体存储器之间的气体管路上设有减压阀,和/或过滤器,和/或干燥器。 Further, the gas pipeline between the cold storage tank and the rare gas storage is provided with a pressure reducing valve, and/or a filter, and/or a dryer. the
进一步地,所述低压级压气机、中压级压气机、高压级压气机分别由低压级电动机、中压级电动机、高压级电动机驱动。 Further, the low-pressure stage compressor, the medium-pressure stage compressor, and the high-pressure stage compressor are respectively driven by a low-voltage stage electric motor, a medium-pressure stage electric motor, and a high-pressure stage electric motor. the
进一步地,所述高压级膨胀机、中压级膨胀机、低压级膨胀机分别驱动高压级发电机、中压级发电机、低压级发电机。 Further, the high-pressure stage expander, the medium-pressure stage expander, and the low-pressure stage expander respectively drive the high-voltage stage generator, the medium-pressure stage generator, and the low-pressure stage generator. the
进一步地,所述稀有气体存储器和稀有气体膨胀释能单元间的气体管路上设有储冷罐,所述储冷罐用以向用冷单元供应冷量。 Further, a cold storage tank is provided on the gas pipeline between the rare gas storage and the rare gas expansion and energy release unit, and the cold storage tank is used to supply cold energy to the cooling unit. the
进一步地,所述用冷单元包括通过管路依次连接的用冷端载冷介质供应罐、用冷端开关阀、冷用户,其中,用冷端开关阀和冷用户之间的用冷管路上设有穿过所述储冷罐部分的用冷换热部件。 Further, the cooling unit includes a cooling medium supply tank at the cold end, an on-off valve at the cold end, and a cold user connected in sequence through pipelines, wherein the on-off pipeline between the on-off valve at the cold end and the cold user There is a cold heat exchange component passing through the cold storage tank part. the
进一步地,所述用冷单元还包括用冷端控制系统,用以控制调节用冷端开关阀的开度和冷用户的用冷量。 Further, the cooling unit also includes a cold end control system, which is used to control the opening degree of the on-off valve of the cold end for adjustment and the cooling capacity of the cold user. the
本实用新型的一种可能的具体操作过程为: A kind of possible specific operation process of the present utility model is:
常压稀有气体存储器中存储的常压状态稀有气体,进入低压级压气机进 行压缩,低压级压气机由低压级电动机带动,电动机的电能可来自风能等可再生能源。稀有气体经低压级压气机压缩后,压力升高,温度升高,进入低压级冷却器进行热量交换,降低温度,同时载热介质供应罐提供的介质进入低压级换热器中收集热量,存储于储热罐中。 The rare gas in the normal pressure state stored in the normal pressure rare gas storage enters the low-pressure stage compressor for compression. The low-pressure stage compressor is driven by the low-pressure stage motor, and the electric energy of the motor can come from renewable energy sources such as wind energy. After the rare gas is compressed by the low-pressure stage compressor, the pressure increases and the temperature rises, and enters the low-pressure stage cooler for heat exchange and lowers the temperature. At the same time, the medium provided by the heat transfer medium supply tank enters the low-pressure stage heat exchanger to collect heat and store it. in the heat storage tank. the
若储热罐中热量可满足使用,则压缩端低压级开关阀打开,压缩端低压级速启/速关阀关闭,稀有气体依次通过压缩端低压级止回阀、压缩端低压级开关阀、安全阀进入高压气体储气罐;若储热罐中热量需要继续补充,则压缩端低压级开关阀关闭,压缩端低压级速启/速关阀打开,稀有气体依次通过压缩端低压级止回阀、压缩端低压级速启/速关阀进入中压级压气机,中压级压气机由中压级电动机带动。中压级压气机出口稀有气体进入中压级换热器完成热量交换,温度降低,同时中压级换热器开关阀打开,载热介质供应罐提供的介质进入中压级换热器中收集热量,并存储于储热罐中。 If the heat in the heat storage tank is sufficient, the on-off valve of the low-pressure stage at the compression end is opened, the quick-open/quick-off valve at the low-pressure stage at the compression end is closed, and the rare gas passes through the low-pressure check valve at the compression end, the on-off valve at the low-pressure stage at the compression end, The safety valve enters the high-pressure gas storage tank; if the heat in the heat storage tank needs to be replenished, the on-off valve of the low-pressure stage at the compression end is closed, the quick-opening/quick-closing valve of the low-pressure stage at the compression end is opened, and rare gases pass through the low-pressure stage check valve at the compression end in turn. The valve and the low-pressure stage quick-opening/quick-closing valve at the compression end enter the medium-pressure compressor, which is driven by the medium-pressure motor. The rare gas at the outlet of the medium-pressure compressor enters the medium-pressure heat exchanger to complete heat exchange, and the temperature drops. At the same time, the switch valve of the medium-pressure heat exchanger is opened, and the medium provided by the heat-carrying medium supply tank enters the medium-pressure heat exchanger for collection. heat and store it in a heat storage tank. the
若储热罐中热量可满足使用,则压缩端中压级开关阀打开,压缩端中压级速启/速关阀关闭,稀有气体依次通过压缩端中压级止回阀、压缩端中压级开关阀、安全阀进入高压气体储气罐;若储热罐中热量需要继续补充,则压缩端中压级开关阀关闭,压缩端中压级速启/速关阀打开,稀有气体依次通过压缩端中压级止回阀、压缩端中压级速启/速关阀进入高压级压气机,高压级压气机由高压级电动机带动。高压级压气机出口稀有气体进入高压级换热器完成热量交换,温度降低,同时高压级换热器开关阀打开,载热介质供应罐提供的介质进入高压级换热器中收集热量,并存储于储热罐中。 If the heat in the heat storage tank is sufficient for use, the medium-pressure on-off valve at the compression end opens, the medium-pressure quick-open/quick-off valve at the compression end closes, and the rare gas passes through the medium-pressure check valve at the compression end and the medium-pressure valve at the compression end in turn. The stage switch valve and safety valve enter the high-pressure gas storage tank; if the heat in the heat storage tank needs to be replenished, the medium-pressure stage switch valve at the compression end is closed, the medium-pressure stage quick-opening/quick-closing valve at the compression end is opened, and rare gases pass through in turn. The medium-pressure stage check valve at the compression end and the medium-pressure stage quick-opening/quick-closing valve at the compression end enter the high-pressure stage compressor, which is driven by the high-pressure stage electric motor. The rare gas at the outlet of the high-pressure stage compressor enters the high-pressure stage heat exchanger to complete heat exchange, and the temperature drops. in the heat storage tank. the
经高压级压气机压缩后,压缩端高压级开关阀打开,稀有气体依次通过压缩端高压级止回阀、压缩端高压级开关阀、安全阀进入高压气体储气罐进行存储。至此,提供给系统的电能转化为稀有气体的压力能和储热罐中的热能。 After being compressed by the high-pressure stage compressor, the high-pressure stage switch valve at the compression end is opened, and the rare gas enters the high-pressure gas storage tank through the high-pressure check valve at the compression end, the high-pressure stage switch valve at the compression end, and the safety valve in turn for storage. So far, the electric energy supplied to the system is converted into the pressure energy of the rare gas and the heat energy in the heat storage tank. the
当热用户需要热量时,用热端控制系统进行负荷需求调控,用热端开关阀打开,用热端载热介质供应罐提供载热介质,经由储热罐吸收热量后送入热用户完成热量供应,降温后的介质返回用热端载热介质供应罐。 When the heat user needs heat, use the hot end control system to regulate the load demand, open the hot end switch valve, use the hot end heat transfer medium supply tank to provide heat transfer medium, absorb heat through the heat storage tank and send it to the heat user to complete the heat Supply, the cooled medium returns to the supply tank for the heat transfer medium at the hot end. the
在对外做功及制取冷量阶段,系统可根据用户端对冷量和电量的需求有选择性回收储热罐中的存储热量值。 In the stage of doing external work and producing cooling capacity, the system can selectively recover the stored heat value in the heat storage tank according to the user's demand for cooling capacity and electricity. the
当电量需求较小或其他方式获得的电能供应充足时,高压级换热器开关阀关闭,膨胀端高压级开关阀关闭,膨胀端高压级速启/速关阀打开,高压气体储气罐释放的稀有气体依次通过膨胀端高压级止回阀、膨胀端高压级速启/速关阀进入高压级膨胀机,推动高压级膨胀机对外做功,高压级膨胀机通过转轴带动高压级发电机对外发电。 When the power demand is small or the power supply obtained by other methods is sufficient, the on-off valve of the high-pressure stage heat exchanger is closed, the on-off valve of the high-pressure stage on the expansion end is closed, the high-pressure stage quick-open/quick-off valve on the expansion end is opened, and the high-pressure gas storage tank is released. The rare gas enters the high-pressure expander sequentially through the high-pressure check valve at the expansion end and the high-pressure quick-open/quick-off valve at the expansion end, pushing the high-pressure expander to do work externally, and the high-pressure expander drives the high-pressure generator to generate electricity externally through the rotating shaft . the
若高压级膨胀机出口气体温度足够低,则膨胀端中压级速启/速关阀关闭,膨胀端中压级开关阀打开,高压级膨胀机出口气体依次通过膨胀端中压级止回阀、膨胀端中压级开关阀进入储冷罐;若高压级膨胀机出口气体温度不够低,则膨胀端中压级速启/速关阀打开,膨胀端中压级开关阀关闭,高压级膨胀机出口气体依次通过膨胀端中压级止回阀、膨胀端中压级速启/速关阀、中压级换热器进入中压级膨胀机,推动中压级膨胀机对外做功,中压级膨胀机通过转轴带动中压级发电机对外发电。 If the gas temperature at the outlet of the high-pressure expander is low enough, the medium-pressure quick-opening/quick-closing valve at the expansion end is closed, the medium-pressure on-off valve at the expansion end is opened, and the gas at the outlet of the high-pressure expander passes through the medium-pressure check valve at the expansion end in turn. 1. The medium-pressure stage switch valve at the expansion end enters the cold storage tank; if the outlet gas temperature of the high-pressure stage expander is not low enough, the medium-pressure stage quick-opening/quick-closing valve at the expansion end opens, the medium-pressure stage switch valve at the expansion end closes, and the high-pressure stage expands The gas at the outlet of the machine enters the medium-pressure expander through the medium-pressure check valve at the expansion end, the medium-pressure quick-opening/quick-closing valve at the expansion end, and the medium-pressure heat exchanger to push the medium-pressure expander to do work. The stage expander drives the medium-voltage stage generator to generate electricity through the rotating shaft. the
若中压级膨胀机出口气体温度足够低,则膨胀端低压级速启/速关阀关闭,膨胀端低压级开关阀打开,中压级膨胀机出口气体依次通过膨胀端低压级止回阀、膨胀端低压级开关阀进入储冷罐;若中压级膨胀机出口气体温度不够低,则膨胀端低压级速启/速关阀打开,膨胀端低压级开关阀关闭,中压级膨胀机出口气体依次通过膨胀端低压级止回阀、膨胀端低压级速启/速关阀、低压级换热器进入低压级膨胀机,推动低压级膨胀机对外做功,低压级膨胀机通过转轴带动低压级发电机对外发电。低压级膨胀机出口气体将进 入储冷罐降温,再依次经过减压阀、过滤器、干燥器返回到常压稀有气体存储器。 If the gas temperature at the outlet of the medium-pressure expander is low enough, the low-pressure stage quick-opening/quick-closing valve at the expansion end is closed, the low-pressure stage switch valve at the expansion end is opened, and the gas at the outlet of the medium-pressure expander passes through the low-pressure check valve at the expansion end, The on-off valve of the low-pressure stage at the expansion end enters the cold storage tank; if the gas temperature at the outlet of the medium-pressure expander is not low enough, the quick-open/quick-off valve of the low-pressure stage at the expansion end opens, the on-off valve of the low-pressure stage at the expansion end closes, and the outlet of the medium-pressure expander The gas enters the low-pressure expander sequentially through the low-pressure check valve at the expansion end, the low-pressure quick-open/quick valve at the expansion end, and the low-pressure heat exchanger, pushing the low-pressure expander to do work externally, and the low-pressure expander drives the low-pressure expander through the shaft. The generator generates electricity externally. The gas at the outlet of the low-pressure stage expander will enter the cold storage tank to cool down, and then return to the normal pressure rare gas storage through the pressure reducing valve, filter and dryer in sequence. the
当冷用户需要冷量时,用冷端控制系统进行负荷需求调控,用冷端开关阀打开,用冷端载冷介质供应罐提供载冷介质,经由储冷罐吸收冷量后送入冷用户完成冷量供应,升温后的介质返回用冷端载冷介质供应罐。 When the cold user needs cooling capacity, the cold end control system is used to regulate the load demand, the cold end switch valve is used to open, and the cold end cold medium supply tank is used to provide the cold medium, and the cold energy is absorbed by the cold storage tank and then sent to the cold user. After the cold supply is completed, the heated medium returns to the cold end carrying cold medium supply tank. the
当电量需求偏大、冷量需求较小且其他方式获得的电能供应不足时,高压级换热器开关阀打开,膨胀端高压级开关阀打开,膨胀端高压级速启/速关阀关闭,高压气体储气罐释放的稀有气体依次通过膨胀端高压级止回阀、膨胀端高压级开关阀进入高压级换热器完成升温,储热罐供应的载热介质通过高压级换热器开关阀进入高压级换热器完成与稀有气体的热量交换,随后返回载热介质供应罐。升温后的稀有气体进入高压级膨胀机,推动高压级膨胀机对外做功,高压级膨胀机通过转轴带动高压级发电机对外发电。 When the power demand is too large, the cooling capacity demand is small and the power supply obtained by other methods is insufficient, the switch valve of the high-pressure stage heat exchanger is opened, the high-pressure stage switch valve of the expansion end is opened, and the high-pressure stage quick-opening/quick-closing valve of the expansion end is closed. The rare gas released from the high-pressure gas storage tank enters the high-pressure heat exchanger through the high-pressure check valve at the expansion end and the high-pressure switch valve at the expansion end to complete the temperature rise, and the heat medium supplied by the heat storage tank passes through the high-pressure heat exchanger switch valve. Enter the high-pressure stage heat exchanger to complete the heat exchange with the rare gas, and then return to the heat transfer medium supply tank. The heated rare gas enters the high-pressure expander to drive the high-pressure expander to do work, and the high-pressure expander drives the high-voltage generator to generate electricity through the rotating shaft. the
若不需要继续补充电力供应,则膨胀端中压级速启/速关阀关闭,膨胀端中压级开关阀打开,高压级膨胀机出口气体依次通过膨胀端中压级止回阀、膨胀端中压级开关阀进入储冷罐完成冷量存储;若需要继续补充电力供应,则膨胀端中压级速启/速关阀打开,膨胀端中压级开关阀关闭,高压级膨胀机出口气体依次通过膨胀端中压级止回阀、膨胀端中压级速启/速关阀进入中压级换热器完成升温,此时中压级换热器开关阀打开,储热罐供应的载热介质通过高压级换热器开关阀、中压级换热器开关阀后进入中压级换热器完成与稀有气体的热量交换,随后返回载热介质供应罐。升温后的稀有气体进入中压级膨胀机,推动中压级膨胀机对外做功,中压级膨胀机通过转轴带动中压级发电机对外发电。 If there is no need to continue to supplement the power supply, the medium-pressure stage quick-opening/quick-closing valve at the expansion end is closed, the medium-pressure stage switch valve at the expansion end is opened, and the gas at the outlet of the high-pressure expander passes through the medium-pressure check valve at the expansion end, the expansion end The on-off valve of the medium-pressure stage enters the cold storage tank to complete the storage of cold energy; if it is necessary to continue to supplement the power supply, the quick-open/quick-off valve of the medium-pressure stage at the expansion end is opened, the on-off valve of the medium-pressure stage at the expansion end is closed, and the gas at the outlet of the high-pressure expander The medium-pressure stage check valve at the expansion end and the medium-pressure stage quick-opening/quick-closing valve at the expansion end enter the medium-pressure stage heat exchanger in turn to complete the temperature rise. The heat medium passes through the switch valve of the high-pressure heat exchanger and the switch valve of the medium-pressure heat exchanger, enters the medium-pressure heat exchanger to complete the heat exchange with the rare gas, and then returns to the heat-carrying medium supply tank. The heated rare gas enters the medium-pressure expander to push the medium-pressure expander to do work, and the medium-pressure expander drives the medium-voltage generator to generate electricity through the shaft. the
若不需要继续补充电力供应,则膨胀端低压级速启/速关阀关闭,膨胀端低压级开关阀打开,中压级膨胀机出口气体依次通过膨胀端低压级止回 阀、膨胀端低压级开关阀进入储冷罐完成冷量存储;若需要继续补充电力供应,则膨胀端低压级速启/速关阀打开,膨胀端低压级开关阀关闭,中压级膨胀机出口气体依次通过膨胀端低压级止回阀、膨胀端低压级速启/速关阀进入低压级换热器完成升温,此时低压级换热器开关阀打开,储热罐供应的载热介质通过高压级换热器开关阀、中压级换热器开关阀、低压级换热器开关阀后进入低压级换热器完成与稀有气体的热量交换,随后返回载热介质供应罐。升温后的稀有气体进入低压级膨胀机,推动低压级膨胀机对外做功,低压级膨胀机通过转轴带动低压级发电机对外发电。低压级膨胀机出口气体经过储冷罐降温后,再依次经过减压阀、过滤器、干燥器返回到常压稀有气体存储器。 If there is no need to continue to supplement the power supply, the low-pressure stage quick-opening/quick-closing valve at the expansion end is closed, the low-pressure stage switch valve at the expansion end is opened, and the gas at the outlet of the medium-pressure expander passes through the low-pressure check valve at the expansion end and the low-pressure stage at the expansion end. The switch valve enters the cold storage tank to complete the cold storage; if it is necessary to continue to supplement the power supply, the low-pressure stage quick-opening/quick-closing valve at the expansion end opens, the low-pressure stage switch valve at the expansion end closes, and the outlet gas of the medium-pressure expander passes through the expansion end in turn The low-pressure stage check valve and the low-pressure stage quick-opening/quick-closing valve at the expansion end enter the low-pressure stage heat exchanger to complete the temperature rise. At this time, the switch valve of the low-pressure stage heat exchanger is opened, and the heat transfer medium supplied by the heat storage tank passes through the high-pressure stage heat exchanger. After the on-off valve, the on-off valve of the medium-pressure heat exchanger, and the on-off valve of the low-pressure heat exchanger, it enters the low-pressure heat exchanger to complete the heat exchange with the rare gas, and then returns to the heat-carrying medium supply tank. The heated rare gas enters the low-pressure stage expander to drive the low-pressure stage expander to do work externally, and the low-pressure stage expander drives the low-pressure stage generator to generate electricity externally through the rotating shaft. The gas at the outlet of the low-pressure stage expander is cooled by the cold storage tank, and then returns to the normal-pressure rare gas storage through the pressure reducing valve, filter, and dryer in sequence. the
综上,在储能过程,该系统可利用每级压气机进气之前的开关阀和速启/速关阀控制压缩的级数,以控制气体的最终压力和热量的存储量,存储的热量值可根据热用户的需求有选择性分配给热用户及返还给高压气体;在释能过程,该系统可根据用户对电量和冷量的需求量,利用每级膨胀机进气之前的开关阀和速启/速关阀控制膨胀和再热的级数,完成冷量和电量的供应。考虑到由其他方式获得电力供应的方便性,释能过程可减少储热器中热量对高压气体的返还,系统以冷量供应为主,电力供应为辅,而该方式亦可保证热用户的用热量。 To sum up, in the process of energy storage, the system can use the on-off valve and the quick-start/quick-off valve before the intake of each stage compressor to control the number of stages of compression, so as to control the final pressure of the gas and the amount of heat stored. The value can be selectively allocated to heat users and returned to high-pressure gas according to the needs of heat users; in the process of energy release, the system can use the switch valve before the intake of each stage expander according to the user's demand for electricity and cooling capacity And quick opening/quick closing valves control the expansion and reheating stages to complete the supply of cooling capacity and electricity. Considering the convenience of obtaining power supply by other means, the energy release process can reduce the return of heat in the heat storage to the high-pressure gas. The system is mainly based on cold supply and supplemented by power supply. Use heat. the
本实用新型的优点及有益效果是: Advantage and beneficial effect of the present utility model are:
1、本实用新型以稀有气体代替空气作为储能技术的存储介质,利用稀有气体低临界压力、低临界温度的特点,在储能到释能阶段完成稀有气体的气态-超临界状态-气态的变化过程,相对于以空气为介质的储能系统,超临界状态下的稀有气体的存储体积更小,降低了系统成本,且纯气体为工质可保证系统运行的稳定性和安全性。 1. The utility model uses rare gas instead of air as the storage medium of energy storage technology, utilizes the characteristics of low critical pressure and low critical temperature of rare gas, and completes the gaseous state-supercritical state-gaseous state of rare gas during the energy storage to energy release stage In the process of change, compared with the energy storage system with air as the medium, the storage volume of the rare gas in the supercritical state is smaller, which reduces the system cost, and the pure gas as the working medium can ensure the stability and safety of the system operation. the
2、本实用新型以稀有气体为压缩气体储能系统的工作介质,借助其密 度较高的特点,相比采用压缩和膨胀空气造成的储能系统整体结构复杂、设计困难、成本较高等问题,以稀有气体为工作介质可以明显降低系统核心部件如透平机械、换热器、储气罐的设计难点,缩小系统规模,进而大大降低系统成本。 2. The utility model uses rare gas as the working medium of the compressed gas energy storage system. With the help of its high density, compared with the energy storage system caused by compressed and expanded air, the overall structure is complicated, the design is difficult, and the cost is high. , using rare gas as the working medium can significantly reduce the design difficulties of core components of the system such as turbomachinery, heat exchangers, and gas storage tanks, reduce the scale of the system, and greatly reduce the cost of the system. the
3、本实用新型可根据热、电、冷的需求,尤其是热和冷的需求量控制系统运行方式改变热和冷的供应量,减少热和冷量供应与需求之间不匹配情况的发生,避免能量的浪费;也可在用户对能量需求较小时完成热和冷的存储,实现未来时间里冷和热的即时供应。 3. The utility model can change the supply of heat and cold according to the demand of heat, electricity and cold, especially the operation mode of the demand control system of heat and cold, so as to reduce the occurrence of mismatch between the supply and demand of heat and cold , to avoid energy waste; it can also complete heat and cold storage when the user's energy demand is small, and realize the instant supply of cold and heat in the future. the
4、本实用新型可以富余电力为能量来源,也可以风能等可再生能源为系统的电力来源,并可以太阳能为系统辅助供热,保证系统的热、电、冷的供应。整个系统在运转工程中不产生任何污染环境的物质,可与热电厂联合使用,亦可用于孤岛、独立建筑或小区,是名副其实的环保、节能系统。 4. The utility model can use surplus electric power as the energy source, or renewable energy such as wind energy as the power source of the system, and can use solar energy as the auxiliary heating for the system to ensure the supply of heat, electricity and cold for the system. The whole system does not produce any substances that pollute the environment during the operation of the project. It can be used in conjunction with thermal power plants, and can also be used in isolated islands, independent buildings or communities. It is a veritable environmental protection and energy-saving system. the
附图说明 Description of drawings
图1本实用新型的以稀有气体为工质的压缩气体分布式能源系统示意图。 Fig. 1 is a schematic diagram of a compressed gas distributed energy system using rare gas as a working medium of the utility model. the
具体实施方式 Detailed ways
为使本储能系统的目的、技术方案及优点更加清楚明白,以下参照附图并举实施例,对本实用新型进一步详细说明。 In order to make the purpose, technical solution and advantages of the energy storage system clearer, the utility model will be further described in detail below with reference to the accompanying drawings and examples. the
如图1所示,本实用新型的以稀有气体为工质的压缩气体分布式能源系统,由常压稀有气体存储器1,低压级压气机2,中压级压气机3,高压级压气机4,低压级电动机5,中压级电动机6,高压级电动机7,低压级冷却器8,中压级冷却器9,高压级冷却器10,压缩端低压级止回阀11,压缩端中压级止回阀12,压缩端高压级止回阀13,压缩端低压级开关阀14,压缩端中压级开关阀15,压 缩端高压级开关阀16,压缩端低压级速启/速关阀17,压缩端中压级速启/速关阀18,中压级冷却器开关阀19,高压级冷却器开关阀20,安全阀21,高压气体储气罐22,载热介质供应罐23,储热罐24,用热端控制系统25,用热端载热介质供应罐26,用热端开关阀27,热用户28,膨胀端高压级止回阀29,膨胀端中压级止回阀30,膨胀端低压级止回阀31,膨胀端高压级开关阀32,膨胀端中压级开关阀33,膨胀端低压级开关阀34,膨胀端高压级速启/速关阀35,膨胀端中压级速启/速关阀36,膨胀端低压级速启/速关阀37,高压级换热器38,中压级换热器39,低压级换热器40,高压级膨胀机41,中压级膨胀机42,低压级膨胀机43,高压级发电机44,中压级发电机45,低压级发电机46,高压级换热器开关阀47,中压级换热器开关阀48,低压级换热器开关阀49,储冷罐50,用冷端控制系统51,用冷端开关阀52,用冷端载冷介质供应罐53,冷用户54,减压阀55,过滤器56,干燥器57等组成,具体操作过程为:
As shown in Figure 1, the compressed gas distributed energy system using rare gas as the working medium of the utility model consists of a normal pressure rare gas storage 1, a low-pressure compressor 2, a medium-pressure compressor 3, and a high-pressure compressor 4 , low-voltage stage motor 5, medium-
常压稀有气体存储器1中存储的常压状态稀有气体,进入低压级压气机2进行压缩,低压级压气机2由低压级电动机5带动,电动机5的电能可来自风能等可再生能源。稀有气体经低压级压气机2压缩后,压力升高,温度升高,进入低压级冷却器8进行热量交换,降低温度,同时载热介质供应罐23提供的介质进入低压级换热器8中收集热量,存储于储热罐24中。
The rare gas stored in the normal-pressure rare gas storage 1 enters the low-pressure compressor 2 for compression. The low-pressure compressor 2 is driven by the low-pressure motor 5, and the electric energy of the motor 5 can come from renewable energy sources such as wind energy. After the rare gas is compressed by the low-pressure stage compressor 2, the pressure rises and the temperature rises, and enters the low-pressure stage cooler 8 for heat exchange and lowers the temperature. At the same time, the medium provided by the heat-carrying
若储热罐24中热量可满足使用,则压缩端低压级开关阀14打开,压缩端低压级速启/速关阀17关闭,稀有气体依次通过压缩端低压级止回阀11、压缩端低压级开关阀14、安全阀21进入高压气体储气罐22;若储热罐24中热量需要继续补充,则压缩端低压级开关阀14关闭,压缩端低压级速启/速关阀17打开,稀有气体依次通过压缩端低压级止回阀11、压缩端低压级速启/速关阀17进入中压级压气机3,中压级压气机3由中压级电动机6带动。中压级压气机3出口稀有气体进入中压级换热器9完成热量交换,温度降 低,同时中压级换热器开关阀19打开,载热介质供应罐23提供的介质进入中压级换热器9中收集热量,并存储于储热罐24中。
If the heat in the
若储热罐24中热量可满足使用,则压缩端中压级开关阀15打开,压缩端中压级速启/速关阀18关闭,稀有气体依次通过压缩端中压级止回阀12、压缩端中压级开关阀15、安全阀21进入高压气体储气罐22;若储热罐24中热量需要继续补充,则压缩端中压级开关阀15关闭,压缩端中压级速启/速关阀18打开,稀有气体依次通过压缩端中压级止回阀12、压缩端中压级速启/速关阀18进入高压级压气机4,高压级压气机4由高压级电动机7带动。高压级压气机4出口稀有气体进入高压级换热器10完成热量交换,温度降低,同时高压级换热器开关阀20打开,载热介质供应罐23提供的介质进入高压级换热器10中收集热量,并存储于储热罐24中。
If the heat in the
经高压级压气机4压缩后,压缩端高压级开关阀16打开,稀有气体依次通过压缩端高压级止回阀13、压缩端高压级开关阀16、安全阀21进入高压气体储气罐22进行存储。至此,提供给系统的电能转化为稀有气体的压力能和储热罐24中的热能。
After being compressed by the high-pressure compressor 4, the high-pressure switch valve 16 at the compression end is opened, and the rare gas enters the high-pressure
当热用户28需要热量时,用热端控制系统25进行负荷需求调控,用热端开关阀27打开,用热端载热介质供应罐26提供载热介质,经由储热罐24吸收热量后送入热用户28完成热量供应,降温后的介质返回用热端载热介质供应罐26。
When the heat user 28 needs heat, the hot
在对外做功及制取冷量阶段,系统可根据用户端对冷量和电量的需求有选择性回收储热罐24中的存储热量值。
In the stage of doing external work and producing cooling capacity, the system can selectively recover the stored heat value in the
当电量需求较小或其他方式获得的电能供应充足时,高压级换热器开关阀47关闭,膨胀端高压级开关阀32关闭,膨胀端高压级速启/速关阀35打开,高压气体储气罐22释放的稀有气体依次通过膨胀端高压级止回阀29、 膨胀端高压级速启/速关阀35进入高压级膨胀机41,推动高压级膨胀机41对外做功,高压级膨胀机41通过转轴带动高压级发电机44对外发电。
When the demand for electricity is small or the supply of electric energy obtained by other means is sufficient, the on-off
若高压级膨胀机41出口气体温度足够低,则膨胀端中压级速启/速关阀36关闭,膨胀端中压级开关阀33打开,高压级膨胀机41出口气体依次通过膨胀端中压级止回阀30、膨胀端中压级开关阀33进入储冷罐50;若高压级膨胀机41出口气体温度不够低,则膨胀端中压级速启/速关阀36打开,膨胀端中压级开关阀33关闭,高压级膨胀机41出口气体依次通过膨胀端中压级止回阀30、膨胀端中压级速启/速关阀36、中压级换热器39进入中压级膨胀机42,推动中压级膨胀机42对外做功,中压级膨胀机42通过转轴带动中压级发电机45对外发电。
If the gas temperature at the outlet of the high-
若中压级膨胀机42出口气体温度足够低,则膨胀端低压级速启/速关阀37关闭,膨胀端低压级开关阀34打开,中压级膨胀机42出口气体依次通过膨胀端低压级止回阀31、膨胀端低压级开关阀34进入储冷罐50;若中压级膨胀机42出口气体温度不够低,则膨胀端低压级速启/速关阀37打开,膨胀端低压级开关阀34关闭,中压级膨胀机42出口气体依次通过膨胀端低压级止回阀31、膨胀端低压级速启/速关阀37、低压级换热器40进入低压级膨胀机43,推动低压级膨胀机46对外做功,低压级膨胀机43通过转轴带动低压级发电机46对外发电。低压级膨胀机43出口气体将进入储冷罐50降温,再依次经过减压阀55、过滤器56、干燥器57返回到常压稀有气体存储器1。
If the gas temperature at the outlet of the medium-pressure expander 42 is low enough, the low-pressure stage quick-opening/quick-closing valve 37 at the expansion end is closed, the low-pressure stage switch valve 34 at the expansion end is opened, and the gas at the outlet of the medium-pressure expander 42 passes through the low-pressure stage at the expansion end in turn. The
当冷用户54需要冷量时,用冷端控制系统51进行负荷需求调控,用冷端开关阀52打开,用冷端载冷介质供应罐53提供载冷介质,经由储冷罐50吸收冷量后送入冷用户54完成冷量供应,升温后的介质返回用冷端载冷介质供应罐53。
When the
当电量需求偏大、冷量需求较小且其他方式获得的电能供应不足时,高 压级换热器开关阀47打开,膨胀端高压级开关阀32打开,膨胀端高压级速启/速关阀35关闭,高压气体储气罐22释放的稀有气体依次通过膨胀端高压级止回阀29、膨胀端高压级开关阀32进入高压级换热器38完成升温,储热罐24供应的载热介质通过高压级换热器开关阀47进入高压级换热器38完成与稀有气体的热量交换,随后返回载热介质供应罐23。升温后的稀有气体进入高压级膨胀机41,推动高压级膨胀机41对外做功,高压级膨胀机41通过转轴带动高压级发电机44对外发电。
When the power demand is relatively large, the cooling demand is small, and the power supply obtained by other methods is insufficient, the
若不需要继续补充电力供应,则膨胀端中压级速启/速关阀36关闭,膨胀端中压级开关阀33打开,高压级膨胀机41出口气体依次通过膨胀端中压级止回阀30、膨胀端中压级开关阀33进入储冷罐50完成冷量存储;若需要继续补充电力供应,则膨胀端中压级速启/速关阀36打开,膨胀端中压级开关阀33关闭,高压级膨胀机41出口气体依次通过膨胀端中压级止回阀30、膨胀端中压级速启/速关阀36进入中压级换热器39完成升温,此时中压级换热器开关阀48打开,储热罐24供应的载热介质通过高压级换热器开关阀47、中压级换热器开关阀48后进入中压级换热器39完成与稀有气体的热量交换,随后返回载热介质供应罐23。升温后的稀有气体进入中压级膨胀机42,推动中压级膨胀机42对外做功,中压级膨胀机42通过转轴带动中压级发电机45对外发电。
If there is no need to continue to supplement the power supply, the medium-pressure stage quick-opening/quick-closing
若不需要继续补充电力供应,则膨胀端低压级速启/速关阀37关闭,膨胀端低压级开关阀34打开,中压级膨胀机42出口气体依次通过膨胀端低压级止回阀31、膨胀端低压级开关阀34进入储冷罐50完成冷量存储;若需要继续补充电力供应,则膨胀端低压级速启/速关阀37打开,膨胀端低压级开关阀34关闭,中压级膨胀机42出口气体依次通过膨胀端低压级止回阀31、膨胀端低压级速启/速关阀37进入低压级换热器40完成升温,此时低压级换 热器开关阀49打开,储热罐24供应的载热介质通过高压级换热器开关阀47、中压级换热器开关阀48、低压级换热器开关阀49后进入低压级换热器40完成与稀有气体的热量交换,随后返回载热介质供应罐23。升温后的稀有气体进入低压级膨胀机43,推动低压级膨胀机43对外做功,低压级膨胀机43通过转轴带动低压级发电机46对外发电。低压级膨胀机43出口气体经过储冷罐50降温后,再依次经过减压阀55、过滤器56、干燥器57返回到常压稀有气体存储器1。
If there is no need to continue to supplement the power supply, the low-pressure stage quick-open/quick-off valve 37 at the expansion end is closed, the low-pressure stage switch valve 34 at the expansion end is opened, and the gas at the outlet of the medium-pressure expander 42 passes through the low-
综上,在储能过程,该系统可利用每级压气机进气之前的开关阀和速启/速关阀控制压缩的级数,以控制气体的最终压力和热量的存储量,存储的热量值可根据热用户的需求有选择性分配给热用户及返还给高压气体;在释能过程,该系统可根据用户对电量和冷量的需求量,利用每级膨胀机进气之前的开关阀和速启/速关阀控制膨胀和再热的级数,完成冷量和电量的供应。考虑到由其他方式获得电力供应的方便性,释能过程可减少储热器中热量对高压气体的返还,系统以冷量供应为主,电力供应为辅,而该方式亦可保证热用户的用热量。 To sum up, in the process of energy storage, the system can use the on-off valve and the quick-start/quick-off valve before the intake of each stage compressor to control the number of stages of compression, so as to control the final pressure of the gas and the amount of heat stored. The value can be selectively allocated to heat users and returned to high-pressure gas according to the needs of heat users; in the process of energy release, the system can use the switch valve before the intake of each stage expander according to the user's demand for electricity and cooling capacity And quick opening/quick closing valves control the expansion and reheating stages to complete the supply of cooling capacity and electricity. Considering the convenience of obtaining power supply by other means, the energy release process can reduce the return of heat in the heat storage to the high-pressure gas. The system is mainly based on cold supply and supplemented by power supply. Use heat. the
以上所述仅为本实用新型的较佳实施例而已,并不用以限制本实用新型,凡在本实用新型的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本实用新型的范围之内。 The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modifications, equivalent replacements, improvements, etc. within the spirit and principles of the present utility model shall include Within the scope of the present utility model. the
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106437885A (en) * | 2016-11-29 | 2017-02-22 | 中国科学院理化技术研究所 | Compressed air energy storage system |
| CN108386235A (en) * | 2018-04-18 | 2018-08-10 | 贵州电网有限责任公司 | A kind of compressed-air energy storage accumulation of heat heat regenerative system |
| CN110446839A (en) * | 2017-03-29 | 2019-11-12 | 株式会社神户制钢所 | Compressed air energy storage power generation device |
| CN112901460A (en) * | 2021-02-01 | 2021-06-04 | 国网江苏省电力有限公司镇江供电分公司 | Compressed air energy storage system of degree of depth energy supply |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106437885A (en) * | 2016-11-29 | 2017-02-22 | 中国科学院理化技术研究所 | Compressed air energy storage system |
| CN106437885B (en) * | 2016-11-29 | 2018-04-17 | 中国科学院理化技术研究所 | Compressed air energy storage system |
| CN110446839A (en) * | 2017-03-29 | 2019-11-12 | 株式会社神户制钢所 | Compressed air energy storage power generation device |
| CN108386235A (en) * | 2018-04-18 | 2018-08-10 | 贵州电网有限责任公司 | A kind of compressed-air energy storage accumulation of heat heat regenerative system |
| CN112901460A (en) * | 2021-02-01 | 2021-06-04 | 国网江苏省电力有限公司镇江供电分公司 | Compressed air energy storage system of degree of depth energy supply |
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