CN208205498U - A kind of absorption soil source heat pump system of twin-stage of fume afterheat driving - Google Patents
A kind of absorption soil source heat pump system of twin-stage of fume afterheat driving Download PDFInfo
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- CN208205498U CN208205498U CN201721885387.9U CN201721885387U CN208205498U CN 208205498 U CN208205498 U CN 208205498U CN 201721885387 U CN201721885387 U CN 201721885387U CN 208205498 U CN208205498 U CN 208205498U
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 29
- 239000002689 soil Substances 0.000 title claims abstract description 25
- 239000003517 fume Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 134
- 238000010438 heat treatment Methods 0.000 claims abstract description 63
- 239000002918 waste heat Substances 0.000 claims abstract description 52
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000003546 flue gas Substances 0.000 claims abstract description 46
- 239000000779 smoke Substances 0.000 claims abstract description 28
- 238000001816 cooling Methods 0.000 claims abstract description 25
- 238000005057 refrigeration Methods 0.000 claims abstract description 22
- 239000006096 absorbing agent Substances 0.000 claims description 23
- 239000000446 fuel Substances 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 239000008400 supply water Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 230000008878 coupling Effects 0.000 abstract description 6
- 238000010168 coupling process Methods 0.000 abstract description 6
- 238000005859 coupling reaction Methods 0.000 abstract description 6
- 230000000295 complement effect Effects 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 4
- 239000003507 refrigerant Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
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- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
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- Sorption Type Refrigeration Machines (AREA)
Abstract
本实用新型提供一种烟气余热驱动的双级吸收式土壤源热泵系统,包括烟气余热利用子系统、吸热式热泵子系统、土壤源利用子系统;土壤源利用子系统包括浅层地热能换热装置;吸热式热泵子系统包括制热机和制冷机;制热机接收烟气余热利用子系统的排烟和经过浅层地热能换热装置换热后的循环水对进入制热机的用户供暖循环水的回水进行加热后,作为用户供暖循环水的给水输出;制冷机接收烟气余热利用子系统的排烟进行热‑冷交换后,对进入制冷机的用户制冷循环的回水进行冷却后,作为用户制冷循环水的给水输出。本实用新型通过多能互补耦合,既可灵活调节浅层地热能源的利用量,又能保证用户的用能需求,提高了可再生能源的供能稳定性,减小了余热浪费和热污染。
The utility model provides a two-stage absorption soil source heat pump system driven by flue gas waste heat, which includes a flue gas waste heat utilization subsystem, a heat absorption heat pump subsystem, and a soil source utilization subsystem; the soil source utilization subsystem includes a shallow ground Thermal energy heat exchange device; the heat absorption heat pump subsystem includes a heating machine and a refrigerator; the heating machine receives the smoke exhaust from the flue gas waste heat utilization subsystem and the circulating water after heat exchange through the shallow geothermal energy heat exchange device enters the heating machine. After heating, the return water of the user heating circulating water is output as the feed water of the user heating circulating water; after the refrigerator receives the waste heat of the flue gas and utilizes the exhaust smoke of the subsystem for heat-cold exchange, the return water of the user refrigeration cycle entering the refrigerator is After cooling, it is output as the feed water of the user's refrigeration cycle water. Through multi-energy complementary coupling, the utility model can not only flexibly adjust the utilization of shallow geothermal energy, but also ensure the energy demand of users, improve the energy supply stability of renewable energy, and reduce waste heat waste and thermal pollution.
Description
技术领域technical field
本实用新型涉及低品位余热利用技术领域,特别是涉及一种烟气余热驱动的双级吸收式土壤源热泵系统。The utility model relates to the technical field of low-grade waste heat utilization, in particular to a two-stage absorption soil source heat pump system driven by flue gas waste heat.
背景技术Background technique
能源和环境问题是制约经济社会可持续发展的两大突出问题。分布式能源系统通常是以可再生能源和清洁燃料为能源,布置在需求侧附近,直接面向用户,按需供应多种能量的绿色综合供能系统。可再生能源具有能流密度低、分布较为分散、规模较小的特点,常规能源利用方式难以对其高效利用,因此,研究以清洁化石燃料和可再生能源互为补充的新型分布式供能系统意义重大。Energy and environmental issues are two prominent issues restricting sustainable economic and social development. Distributed energy systems are usually based on renewable energy and clean fuels, arranged near the demand side, directly facing users, and supplying a variety of energy on demand. Green comprehensive energy supply system. Renewable energy has the characteristics of low energy flow density, relatively dispersed distribution, and small scale. Conventional energy utilization methods are difficult to efficiently utilize it. Therefore, research on new distributed energy supply systems that complement each other with clean fossil fuels and renewable energy Significant.
地表浅层是一个巨大的太阳能集热器,收集了47%的太阳能,土壤源是近乎无限的可再生能源,也是清洁能源。单独的土壤源利用方案受土壤性能影响较大,如何实现浅层地热能源和燃气分布式能源的高效耦合成为本领域技术人员亟待解决的实际技术问题。The shallow layer of the ground is a huge solar collector, which collects 47% of the solar energy, and the soil source is a nearly unlimited renewable energy source, which is also a clean energy source. A single soil source utilization scheme is greatly affected by soil properties. How to realize the efficient coupling of shallow geothermal energy and gas distributed energy has become a practical technical problem to be solved urgently by those skilled in the art.
实用新型内容Utility model content
本实用新型解决的技术问题:The technical problem that the utility model solves:
本实用新型提供了一种烟气余热驱动的双级吸收式土壤源热泵系统,实现浅层地热能源和燃气分布式能源的高效耦合。The utility model provides a two-stage absorption soil source heat pump system driven by waste heat of flue gas, which realizes efficient coupling of shallow geothermal energy and gas distributed energy.
本实用新型采用的技术方案:The technical scheme that the utility model adopts:
一种烟气余热驱动的双级吸收式土壤源热泵系统,包括:A two-stage absorption ground source heat pump system driven by flue gas waste heat, including:
提供排烟的烟气余热利用子系统;获取烟气余热利用子系统的排烟的吸热式热泵子系统;与吸热式热泵子系统连通进行换热的土壤源利用子系统;The flue gas waste heat utilization subsystem that provides smoke exhaust; the heat absorption heat pump subsystem that obtains the smoke exhaust of the flue gas waste heat utilization subsystem; the soil source utilization subsystem that communicates with the heat absorption heat pump subsystem for heat exchange;
所述土壤源利用子系统包括对地热和吸热式热泵子系统进行换热的浅层地热能换热装置5;The soil source utilization subsystem includes a shallow geothermal energy heat exchange device 5 for exchanging heat with the geothermal and heat-absorbing heat pump subsystems;
所述吸热式热泵子系统包括制热机3和制冷机4;The endothermic heat pump subsystem includes a heating machine 3 and a refrigerator 4;
制热机3接收烟气余热利用子系统的排烟和经过浅层地热能换热装置5换热后的循环水对进入制热机3的用户供暖循环水的回水进行加热后,作为用户供暖循环水的给水输出,同时将经过换热冷却的浅层地热能换热装置5的循环水重新送入到浅层地热能换热装置5进行换热升温;The heating machine 3 receives the smoke exhaust from the flue gas waste heat utilization subsystem and the circulating water after heat exchange by the shallow geothermal energy heat exchange device 5. After heating the return water of the user heating circulating water entering the heating machine 3, it is used as the user heating cycle The water supply is output, and at the same time, the circulating water of the shallow geothermal energy heat exchange device 5 that has been cooled by heat exchange is re-sent to the shallow geothermal energy heat exchange device 5 for heat exchange and temperature rise;
制冷机4接收烟气余热利用子系统的排烟进行热-冷交换后,对进入制冷机4的用户制冷循环的回水进行冷却后,作为用户制冷循环水的给水输出;同时,冷却过程中产生的热量将经过浅层地热能换热装置5的循环水进行加热后,重新送入到浅层地热能换热装置5进行换热降温。Refrigerator 4 receives the waste heat of flue gas and utilizes the exhaust smoke of the subsystem for heat-cold exchange, and then cools the return water of the user's refrigeration cycle entering into the refrigerator 4, and outputs it as the feed water of the user's refrigeration cycle water; at the same time, during the cooling process The generated heat will be heated by the circulating water of the shallow geothermal energy heat exchange device 5, and then re-sent to the shallow geothermal energy heat exchange device 5 for heat exchange and cooling.
进一步,所述土壤源利用子系统还包括U型地埋管装置6,U型地埋管装置6的管道内的介质进入到浅层地热能换热装置5进行换热后,重新进入到U型地埋管装置6中。Further, the soil source utilization subsystem also includes a U-shaped buried pipe device 6, and the medium in the pipeline of the U-shaped buried pipe device 6 enters the shallow geothermal energy heat exchange device 5 for heat exchange, and then re-enters the U-shaped buried pipe device 6. Type buried pipe device 6.
进一步,所述吸热式热泵子系统的制热机3为第一类增热型吸收式热泵,包括发生器ⅠGH、冷凝器ⅠCH、蒸发器ⅠEH、吸收器ⅠAH;发生器ⅠGH的进气口接收烟气余热利用子系统的排烟,发生器ⅠGH出气口的排烟排入大气;蒸发器ⅠEH的入水口连接浅层地热能换热装置5的循环水出水,蒸发器EH的出水口连接浅层地热能换热装置5的循环水进水;吸收器ⅠAH的入水口连接用户供暖循环水的回水,冷凝器ⅠCH的出水口连接用户供暖循环水的给水;Further, the heating machine 3 of the endothermic heat pump subsystem is a first-type heat-increasing absorption heat pump, including a generator IGH , a condenser ICH, an evaporator IEH , and an absorber IAH ; the generator IGH The air inlet of the evaporator receives the smoke exhaust from the waste heat utilization subsystem of the flue gas, and the exhaust smoke from the outlet of the generator IG H is discharged into the atmosphere; the water inlet of the evaporator IE H is connected to the circulating water outlet of the shallow geothermal energy heat exchange device 5, and evaporates The water outlet of EH is connected to the circulating water inlet of shallow geothermal energy heat exchange device 5; the water inlet of absorber IA H is connected to the return water of user heating circulating water, and the water outlet of condenser ICH is connected to the user’s heating circulating water water supply;
所述吸热式热泵子系统的制冷机4为吸收式制冷装置,包括发生器ⅡGC、冷凝器ⅡCC、蒸发器ⅡEC、吸收器ⅡAC;发生器ⅡGC的进气口接收烟气余热利用子系统的排烟,发生器ⅡGC出气口的排烟排入大气;蒸发器ⅡEC的入水口连接用户制冷循环水的回水,蒸发器ⅡEC的出水口连接用户制冷循环水的给水,吸收器ⅡAH的入水口连接浅层地热能换热装置5的循环水出水,冷凝器ⅡCH的出水口连接浅层地热能换热装置5的循环水进水。The refrigerator 4 of the endothermic heat pump subsystem is an absorption refrigeration device, including a generator IIGC , a condenser IICC , an evaporator IIEC , and an absorber IIAC ; the air inlet of the generator IIGC receives flue gas The smoke exhaust from the waste heat utilization subsystem and the exhaust smoke from the outlet of the generator IIGC are discharged into the atmosphere; the water inlet of the evaporator IIEC is connected to the return water of the user's refrigeration circulation water, and the water outlet of the evaporator IIEC is connected to the user's refrigeration circulation water For water supply, the water inlet of the absorber ⅡA H is connected to the circulating water outlet of the shallow geothermal energy heat exchange device 5, and the water outlet of the condenser ⅡCH H is connected to the circulating water inlet of the shallow geothermal energy heat exchange device 5.
进一步,所述烟气余热利用子系统与制热机3的发生器ⅠGH进气口连通的管道上设置有阀ⅠVG1,所述蒸发器ⅠEH的出水口与浅层地热能换热装置5的循环水进水口连通的管道上设置有阀ⅢVH2,所述浅层地热能换热装置5的循环水出水口与蒸发器ⅠEH的进水口连通的管道上设置有阀ⅤVH1;Further, a valve IV G1 is set on the pipe connecting the flue gas waste heat utilization subsystem with the inlet of the generator IG H of the heating machine 3, and the water outlet of the evaporator IE H is connected to the shallow geothermal energy heat exchange device 5 A valve IIIV H2 is set on the pipeline connected to the circulating water inlet of the shallow geothermal energy heat exchange device 5, and a valve VV H1 is set on the pipeline connected to the water inlet of the evaporator IE H between the circulating water outlet of the shallow geothermal energy heat exchange device 5;
所述烟气余热利用子系统与制冷机4的发生器ⅡGC进气口连通的管道上设置有阀ⅡVG2;所述冷凝器ⅡCC的出水口与浅层地热能换热装置5的循环水进水口之间的管道上设置有阀ⅣVC2,所述浅层地热能换热装置5的循环水出水口与吸收器ⅡAC的进水口连通的管道上设置有阀ⅥVC1; A valve IIV G2 is set on the pipe connecting the flue gas waste heat utilization subsystem with the air inlet of the generator IIGC of the refrigerator 4; A valve IVV C2 is provided on the pipeline between the water inlets, and a valve VIV C1 is provided on the pipeline connecting the circulating water outlet of the shallow geothermal energy heat exchange device 5 with the water inlet of the absorber IIAC;
在制热机3工作时,阀ⅠVG1、阀ⅢVH2、阀ⅤVH1开启,阀ⅡVG2、阀ⅣVC2、阀ⅥVC1关闭;When the heating machine 3 is working, valve IV G1 , valve III V H2 and valve V V H1 are opened, and valve II V G2 , valve IV V C2 and valve VI V C1 are closed;
在制冷机4工作时,阀ⅡVG2、阀ⅣVC2、阀ⅥVC1开启,阀ⅠVG1、阀ⅢVH2、阀ⅤVH1关闭。When the refrigerator 4 is working, the valves IIVG2, IVVC2 and VIVC1 are opened, and the valves IVG1, IIIVH2 and VVH1 are closed.
进一步,所述烟气余热利用子系统包括依次连接的燃料动力转换装置1和余热制冷供热装置2,所述燃料动力转换装置1为内燃机组;所述余热制冷供热装置2为烟气热水型吸收式热泵。Further, the flue gas waste heat utilization subsystem includes a sequentially connected fuel power conversion device 1 and a waste heat cooling and heating device 2, the fuel power conversion device 1 is an internal combustion unit; the waste heat cooling and heating device 2 is a flue gas heating Water type absorption heat pump.
本实用新型的有益效果:The beneficial effects of the utility model:
(1)利用吸收式热泵技术实现了低品位烟气余热和浅层地热能源的高效回收和利用,实现了燃气冷热电三联供技术和土壤源热泵技术的耦合,提高了可再生能源供能稳定性,减小了余热浪费和热污染;(1) The use of absorption heat pump technology realizes the efficient recovery and utilization of low-grade flue gas waste heat and shallow geothermal energy, realizes the coupling of gas-fired combined cooling, heating and power technology and soil source heat pump technology, and improves the energy supply of renewable energy Stability, reducing waste heat waste and thermal pollution;
(2)吸收式热泵以烟气为驱动热源,吸收式热泵能耗小于电驱动土壤源热泵,提高了多能互补系统综合能源利用率。(2) The absorption heat pump uses flue gas as the driving heat source, and the energy consumption of the absorption heat pump is less than that of the electric-driven soil source heat pump, which improves the comprehensive energy utilization rate of the multi-energy complementary system.
(3)通过多能互补耦合,既可灵活调节浅层地热能源的利用量,又能保证用户的用能需求,维持土壤中的能量平衡,实现可再生能源的持续利用。(3) Through multi-energy complementary coupling, it can not only flexibly adjust the utilization of shallow geothermal energy, but also ensure the energy demand of users, maintain the energy balance in the soil, and realize the sustainable utilization of renewable energy.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
其中,1-燃料动力转换装置;2-余热制冷供热装置;3-制热机;4-制冷机;5-浅层地热能换热装置;6-U型地埋管装置;Among them, 1-fuel power conversion device; 2-waste heat cooling and heating device; 3-heating machine; 4-refrigerating machine; 5-shallow geothermal energy heat exchange device; 6-U-shaped buried pipe device;
S1、S2、S3、S4、S5、S6为烟气;S1, S2, S3, S4, S5, S6 are flue gas;
W1、W2、W3、W4、W5、W6为浅层地热能换热器循环水;W1, W2, W3, W4, W5, and W6 are circulating water for shallow geothermal energy heat exchangers;
D1、D2为U型地埋管循环水;D1 and D2 are U-shaped buried pipe circulating water;
L1、L2、L3、L4为用户空调循环水;L1, L2, L3, and L4 are circulating water for user air conditioners;
VG1、VG2、VC1、VC2、VH1、VH2为阀门。VG1, VG2, VC1, VC2, VH1, VH2 are valves.
具体实施方式Detailed ways
下面结合附图和具体实施方式对本实用新型作进一步详细说明。The utility model is described in further detail below in conjunction with accompanying drawing and specific embodiment.
本实用新型实施例公开了一种烟气余热驱动的双级吸收式土壤源热泵系统,实现了燃气冷热电三联供技术和土壤源热泵技术的互补耦合,提高了可再生能源供能稳定性,减小了余热浪费和热污染。The embodiment of the utility model discloses a two-stage absorption soil source heat pump system driven by flue gas waste heat, which realizes the complementary coupling of gas cooling, heating and power triple supply technology and soil source heat pump technology, and improves the energy supply stability of renewable energy , reducing waste heat waste and thermal pollution.
下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清除、完整地描述,显然,所描述的实施例仅仅是本实用新型的一部分实施例,而不是全部实施例。基于本实用新型的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其它实施例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all implementations. example. Based on the embodiments of the present utility model, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of the present utility model.
具体来说,如图1所示,本实用新型提供一种烟气余热驱动的双级吸收式土壤源热泵系统,包括烟气余热利用子系统,该烟气余热利用子系统使用燃气冷热电三联供系统提供排烟S2作为吸热式热泵子系统的驱动热源;排烟S2进入到吸热式热泵子系统进行加热,同时还包括与吸热式热泵子系统连通进行换热的土壤源利用子系统。Specifically, as shown in Figure 1, the utility model provides a two-stage absorption soil source heat pump system driven by flue gas waste heat, including a flue gas waste heat utilization subsystem, and the flue gas waste heat utilization subsystem uses gas cooling and heating power The triple supply system provides exhaust smoke S2 as the driving heat source of the heat-absorbing heat pump subsystem; the exhaust smoke S2 enters the heat-absorbing heat pump subsystem for heating, and also includes the use of soil sources connected to the heat-absorbing heat pump subsystem for heat exchange subsystem.
其中,土壤源利用子系统包括对地下热和地上的吸热式热泵子系统进行换热的浅层地热能换热装置5,还包括埋在地下的U型地埋管装置6,其中,U型地埋管装置6的U型管内的介质D1(如循环热水)进入到浅层地热能换热装置5进行换热,换热后的介质D2返回U型管内。浅层地热能换热装置5内部可设置换热管,该换热管与U型地埋管装置6的介质管道连通,还与吸热式热泵子系统连通。Among them, the soil source utilization subsystem includes a shallow geothermal energy heat exchange device 5 for exchanging heat between the underground heat and the above-ground heat-absorbing heat pump subsystem, and also includes a U-shaped underground pipe device 6 buried underground, where U The medium D1 (such as circulating hot water) in the U-shaped pipe of the buried pipe device 6 enters the shallow geothermal energy heat exchange device 5 for heat exchange, and the medium D2 after heat exchange returns to the U-shaped pipe. A heat exchange tube can be arranged inside the shallow geothermal energy heat exchange device 5, and the heat exchange tube communicates with the medium pipeline of the U-shaped underground pipe device 6 and also communicates with the endothermic heat pump subsystem.
吸热式热泵子系统包括制热机3和制冷机4,制热机3用于对用户供暖循环水进行加热后对用户进行供暖,制冷机4用于对用户制冷循环水冷却后对用户进行制冷,其中,用户供暖循环水和用户制冷循环水可采用同一条循环管道,在不同的季节连接制热机3或者制冷机4,实现制热或者制冷。制热机3以排烟S2作为驱动热源,以浅层地热能换热装置5的循环水W5作为低温热源实现供热,而制冷机4则以排烟S2作为高温热源,以浅层地热能换热装置5的循环水W2作为冷却水实现供冷。The endothermic heat pump subsystem includes a heating machine 3 and a refrigerator 4. The heating machine 3 is used to heat the user's heating circulating water to heat the user, and the refrigerator 4 is used to cool the user's refrigeration circulating water to cool the user. Wherein, the user heating circulating water and the user cooling circulating water can use the same circulating pipe, and connect the heating machine 3 or the refrigerator 4 in different seasons to realize heating or cooling. The heating machine 3 uses the exhaust smoke S2 as the driving heat source, and uses the circulating water W5 of the shallow geothermal energy heat exchange device 5 as the low-temperature heat source to realize heat supply, while the refrigerator 4 uses the exhaust smoke S2 as the high-temperature heat source, and uses the shallow geothermal energy for heat exchange. The circulating water W2 of the thermal device 5 is used as cooling water to realize cooling.
其中,如图1所示的系统中,制热机3接收烟气余热利用子系统的排烟S2和经过浅层地热能换热装置5换热后的循环水进水W4,对进入制热机3的用户供暖循环水的回水L3进行加热,加热后的循环水作为用户供暖循环水的给水L4输出给用户进行供暖;同时制热机3将经过换热冷却的浅层地热能换热装置5的进水W5重新送入到浅层地热能换热装置5作为循环水进水W6进行换热升温,换热升温后的循环水出水W1再次进入到制热机3。Among them, in the system shown in Figure 1, the heating machine 3 receives the exhaust smoke S2 of the flue gas waste heat utilization subsystem and the circulating water inlet W4 after heat exchange by the shallow geothermal energy heat exchange device 5, and the heating machine 3 The return water L3 of the user's heating circulating water is heated, and the heated circulating water is output to the user as the supply water L4 of the user's heating circulating water for heating; at the same time, the heating machine 3 converts the shallow geothermal energy heat exchange device 5 that has been cooled by heat exchange The influent water W5 is re-sent to the shallow geothermal energy heat exchange device 5 as the circulating water inflow W6 for heat exchange and temperature rise, and the circulating water effluent W1 after heat exchange and temperature rise enters the heating machine 3 again.
制冷机4接收烟气余热利用子系统的排烟对发生器进行加热,制冷剂在蒸发器中蒸发并吸收进入制冷机4的用户制冷循环水的回水L1的热量,对用户制冷循环水进行降温后,作为用户制冷循环水的给水L2输出给用户进行降温;而在制冷循环过程中,吸收器和冷凝器产生的热量对进入制冷机4的浅层地热能换热装置5的循环水W2进行加热后,重新作为浅层地热能换热装置5循环水的进水W4进入到浅层地热能换热装置5进行换热降温,降温后的循环水出水W1作为冷却水再次进入制冷机4循环。The refrigerating machine 4 receives the waste heat of the flue gas and utilizes the smoke exhaust of the subsystem to heat the generator, and the refrigerant evaporates in the evaporator and absorbs the heat of the return water L1 of the user's refrigerating circulating water entering the refrigerating machine 4, and heats up the user's refrigerating circulating water. After cooling down, the feed water L2 used as the user’s refrigeration circulating water is output to the user for cooling; while in the refrigeration cycle process, the heat generated by the absorber and the condenser has a great impact on the circulating water W2 entering the shallow geothermal energy heat exchange device 5 of the refrigerator 4 After heating, the incoming water W4 which is used as the circulating water of the shallow geothermal energy heat exchange device 5 enters the shallow geothermal energy heat exchange device 5 for heat exchange and cooling, and the cooled circulating water outlet W1 enters the refrigerator 4 again as cooling water cycle.
作为一种具体的实施方式,上述的吸热式热泵子系统的制热机3为第一类增热型吸收式热泵,包括发生器ⅠGH、冷凝器ⅠCH、蒸发器ⅠEH、吸收器ⅠAH;发生器ⅠGH的进气口接收烟气余热利用子系统,烟气余热利用子系统的排烟作为制热机3的排烟S3进入发生器GH的进气口,发生器ⅠGH的出气口作为排气口将降温的烟气S5排入大气;蒸发器ⅠEH的入水口连接浅层地热能换热装置5的循环水出水W3,蒸发器ⅠEH的出水口连接浅层地热能换热装置5的循环水进水W5;吸收器ⅠAH的入水口连接用户供暖循环水的回水L3,冷凝器ⅠCH的出水口连接用户供暖循环水的给水L2。As a specific implementation, the heat generator 3 of the above-mentioned endothermic heat pump subsystem is a first-type heat-increasing absorption heat pump, including a generator IGH, a condenser ICH, an evaporator IEH, and an absorber IAH; The air inlet of IGH receives the flue gas waste heat utilization subsystem, and the exhaust smoke of the flue gas waste heat utilization subsystem enters the air inlet of the generator GH as the exhaust smoke S3 of the heating machine 3, and the air outlet of the generator IGH serves as the exhaust port to The cooled flue gas S5 is discharged into the atmosphere; the water inlet of the evaporator IEH is connected to the circulating water outlet W3 of the shallow geothermal energy heat exchange device 5, and the water outlet of the evaporator IEH is connected to the circulating water inlet of the shallow geothermal energy heat exchange device 5 W5; the water inlet of the absorber IAH is connected to the return water L3 of the user's heating circulating water, and the water outlet of the condenser ICH is connected to the supply water L2 of the user's heating circulating water.
上述的制热机3在工作时,发生器ⅠGH接收排烟S4后,加热发生器ⅠGH中稀溶液使制冷剂蒸发析出,气态制冷剂进入到冷凝器ⅠCH放热冷凝后成为液态,经降压后进入蒸发器ⅠEH吸热成为低压蒸气,低压蒸气被吸收器ⅠAH中的浓溶液吸收变成稀溶液,稀溶液返回发生器,完成循环。吸收器和冷凝器为放热过程,用户制冷循环水依次进入吸收器和冷凝器进行加热,加热的用户制冷循环出水在用户侧完成换热,用户制冷循环回水重新进入吸收器入口。蒸发器为吸热过程,浅层地热能换热装置5的循环水进入蒸发器放热,冷却后的浅层地热能换热装置5的循环水进入到浅层地热能换热装置5换热后,再次进入循环作为冷却水。When the above-mentioned heating machine 3 is working, after the generator IGH receives the exhaust smoke S4, it heats the dilute solution in the generator IGH to evaporate and precipitate the refrigerant. After being compressed, it enters the evaporator IE H to absorb heat and become a low-pressure steam. The low-pressure steam is absorbed by the concentrated solution in the absorber IA H to become a dilute solution, and the dilute solution returns to the generator to complete the cycle. The absorber and condenser are exothermic processes. The user refrigeration cycle water enters the absorber and condenser in turn for heating. The heated user refrigeration cycle outlet water completes heat exchange on the user side, and the user refrigeration cycle return water re-enters the absorber inlet. The evaporator is a heat-absorbing process, the circulating water of the shallow geothermal energy heat exchange device 5 enters the evaporator to release heat, and the cooled circulating water of the shallow geothermal energy heat exchange device 5 enters the shallow geothermal energy heat exchange device 5 for heat exchange After that, it enters the circulation again as cooling water.
吸热式热泵子系统的制冷机4为吸收式制冷装置,包括发生器ⅡGC、冷凝器ⅡCC、蒸发器ⅡEC、吸收器ⅡAC;发生器ⅡGC的进气口接收烟气余热利用子系统送出的排烟S4,发生器ⅡGC的出气口将经过换热的烟气S6排入大气;蒸发器ⅡEC的入水口连接用户制冷循环水的回水L1,蒸发器ⅡEC的出水口作为用户制冷循环水的给水L2,吸收器ⅡAC的入水口连接浅层地热能换热装置5的循环水出水W2,冷凝器ⅡCC的出水口连接浅层地热能换热装置5的循环水进水W4。The refrigerator 4 of the endothermic heat pump subsystem is an absorption refrigeration device, including a generator IIGC , a condenser IICC , an evaporator IIEC , and an absorber IIAC ; The exhaust smoke S 4 sent by the subsystem, the gas outlet of the generator Ⅱ G C discharges the heat-exchanged flue gas S 6 into the atmosphere; the water inlet of the evaporator Ⅱ E C is connected to the return water L 1 of the user’s refrigeration circulating water, and the evaporator Ⅱ E The water outlet of C is used as the supply water L 2 of the user's refrigeration circulating water, the water inlet of the absorber ⅡA C is connected to the circulating water outlet W 2 of the shallow geothermal energy heat exchange device 5, and the water outlet of the condenser ⅡC C is connected to the shallow geothermal energy exchange The circulating water of the heating device 5 is water W 4 .
上述的制冷机4在工作时,发生器ⅡGC接收排烟S4后,加热发生器ⅡGC中稀溶液使制冷剂蒸发析出,气态制冷剂进入到冷凝器ⅡCC放热冷凝后成为液态,经降压后进入蒸发器ⅡEC吸热成为低压蒸气,低压蒸气被吸收器ⅡAC中的浓溶液吸收变成稀溶液,稀溶液返回发生器,完成循环。蒸发器为吸热过程,对用户制冷循环水进行冷却,冷却后的用户制冷循环出水在用户侧完成换热,用户制冷循环回水重新进入蒸发器。此循环过程中,冷凝器和吸收器为放热过程,浅层地热能换热装置5的循环水依次进入吸收器和冷凝器吸热,加热后的浅层地热能换热装置5的循环水进入到浅层地热能换热装置5换热后,再次进入循环作为冷却水。When the above-mentioned refrigerator 4 is working, after the generator IIGC receives the exhaust smoke S4, the dilute solution in the generator IIGC is heated to evaporate and precipitate the refrigerant, and the gaseous refrigerant enters the condenser IICC C to release heat and condense to become a liquid state. After decompression, it enters the evaporator IIEC to absorb heat and becomes low-pressure steam. The low - pressure steam is absorbed by the concentrated solution in the absorber IIAC to become a dilute solution, and the dilute solution returns to the generator to complete the cycle. The evaporator is a heat-absorbing process that cools the user's refrigeration cycle water. After cooling, the user's refrigeration cycle outlet water completes heat exchange on the user side, and the user's refrigeration cycle return water enters the evaporator again. In this circulation process, the condenser and the absorber are exothermic processes, and the circulating water of the shallow geothermal energy heat exchange device 5 enters the absorber and the condenser in turn to absorb heat, and the heated circulating water of the shallow geothermal energy heat exchange device 5 After entering the shallow geothermal energy heat exchange device 5 for heat exchange, it enters the circulation again as cooling water.
为了更好的实现供冷和供热的控制,烟气余热利用子系统与制热机3的发生器GH进气口连通的管道上设置有阀ⅠVG1,蒸发器EH的出水口与浅层地热能换热装置5的循环水进水口连通的管道上设置有阀ⅢVH2,浅层地热能换热装置5的循环水出水口与蒸发器ⅠEH的进水口连通的管道上设置有阀ⅤVH1。In order to better control the cooling and heating supply, a valve IV G1 is set on the pipeline connecting the flue gas waste heat utilization subsystem with the generator G H inlet of the heating machine 3, and the water outlet of the evaporator E H is connected with the shallow A valve IIIV H2 is set on the pipe connecting the circulating water inlet of the geothermal energy heat exchange device 5 in the upper layer, and a valve is installed on the pipe connecting the circulating water outlet of the shallow geothermal energy heat exchange device 5 and the water inlet of the evaporator IE H VV H1 .
烟气余热利用子系统与制冷机4的发生器GC进气口连通的管道上设置有阀ⅡVG2;冷凝器ⅡCC的出水口与浅层地热能换热装置5的循环水进水口之间的管道上设置有阀ⅣVC2,浅层地热能换热装置5的循环水出水口与吸收器AC的进水口连通的管道上设置有阀ⅥVC1。There is a valve II V G2 on the pipe connecting the flue gas waste heat utilization subsystem with the inlet of the generator G C of the refrigerator 4; A valve IVV C2 is set on the pipeline between them, and a valve VIV C1 is set on the pipeline connecting the circulating water outlet of the shallow geothermal energy heat exchange device 5 with the water inlet of the absorber AC.
在制热机3工作时,阀ⅠVG1、阀ⅢVH2、阀ⅤVH1开启,阀ⅡVG2、阀ⅣVC2、阀ⅥVC1关闭;在制冷机4工作时,阀ⅡVG2、阀ⅣVC2、阀ⅥVC1开启,阀ⅠVG1、阀ⅢVH2、阀ⅤVH1关闭。When the heating machine 3 is working, the valve IV G1 , valve III V H2 , and valve V V H1 are open, and the valve II V G2 , valve IV V C2 , and valve VI V C1 are closed; when the refrigerator 4 is working, the valve II V G2 , valve IV C2 , and valve VI V C1 is open, valve IV G1 , valve IIIV H2 and valve VV H1 are closed.
作为一种具体的实施方式,烟气余热利用子系统包燃料动力转换装置1和余热制冷供热装置2,燃料动力转换装置1的排烟S1连接余热制冷供热装置2,用于实现发电、供冷、供热,燃料动力转换装置1可选择内燃机组,用于实现发电,燃料可选择天然气、沼气等;余热制冷供热装置2可选择烟气热水型吸收式热泵,用于回收燃料动力转换装置的排烟S1和缸套水余热实现供冷、供热。As a specific implementation, the flue gas waste heat utilization subsystem includes a fuel power conversion device 1 and a waste heat cooling and heating device 2, and the exhaust gas S1 of the fuel power conversion device 1 is connected to the waste heat cooling and heating device 2 to realize power generation , cooling, heating, fuel power conversion device 1 can choose internal combustion unit for power generation, fuel can choose natural gas, biogas, etc.; waste heat cooling and heating device 2 can choose flue gas hot water type absorption heat pump for recycling The exhaust smoke S1 of the fuel power conversion device and the waste heat of cylinder jacket water realize cooling and heating.
余热制冷供热装置2可以使用现有的烟气热水型吸收式热泵实现。The waste heat cooling and heating device 2 can be realized by using an existing flue gas hot water type absorption heat pump.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本实用新型。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本实用新型的精神或范围的情况下,在其它实施例中实现。因此本实用新型将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽范围。The above description of the disclosed embodiments enables those skilled in the art to realize or use the utility model. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to these embodiments shown herein, but will conform to the widest scope consistent with the principles and novel features disclosed herein.
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CN107975977A (en) * | 2017-12-28 | 2018-05-01 | 华电郑州机械设计研究院有限公司 | A kind of absorption soil source heat pump system of twin-stage of fume afterheat driving |
CN115111632A (en) * | 2022-06-21 | 2022-09-27 | 北方联合电力有限责任公司呼和浩特金桥热电厂 | A combined heat and power system and method for internal combustion engine coupled with solar energy and geothermal energy |
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CN107975977A (en) * | 2017-12-28 | 2018-05-01 | 华电郑州机械设计研究院有限公司 | A kind of absorption soil source heat pump system of twin-stage of fume afterheat driving |
CN115111632A (en) * | 2022-06-21 | 2022-09-27 | 北方联合电力有限责任公司呼和浩特金桥热电厂 | A combined heat and power system and method for internal combustion engine coupled with solar energy and geothermal energy |
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