WO2009105930A1 - A kind of concentrated heat-supply system - Google Patents
A kind of concentrated heat-supply system Download PDFInfo
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- WO2009105930A1 WO2009105930A1 PCT/CN2008/001605 CN2008001605W WO2009105930A1 WO 2009105930 A1 WO2009105930 A1 WO 2009105930A1 CN 2008001605 W CN2008001605 W CN 2008001605W WO 2009105930 A1 WO2009105930 A1 WO 2009105930A1
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- Prior art keywords
- pipe
- water
- heat pump
- steam
- heat
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Classifications
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- 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
- F01K7/00—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
- F01K7/34—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of extraction or non-condensing type; Use of steam for feed-water heating
- F01K7/38—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of extraction or non-condensing type; Use of steam for feed-water heating the engines being of turbine type
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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]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
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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
- 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 invention relates to a central heating system.
- the present invention provides a device for supplying heat to a heating network.
- the apparatus for heating a primary network comprises: a steam turbine including a condenser 2, at least one steam absorption heat pump 3, a steam-water heat exchanger 4, a pipe 7, a pipe 8 and a pipe 9; Passing through the steam turbine 1 and the condenser 2 in sequence;
- the pipe 8 is composed of a main pipe and two branch pipes.
- the main pipe 8 passes through the steam turbine 1 and is divided into two branch pipes.
- the branch pipe 8-1 passes through the steam absorption heat pump 3, and the branch pipe 8-2 passes through the steam-water heat exchanger. 4;
- the pipe 9 is composed of a main pipe and two branch pipes.
- the main pipe 9 passes through the condenser 2 and is divided into two branch pipes.
- the branch pipe 9-1 passes through the steam absorption heat pump 3 and the primary network return pipe.
- the passage 13 communicates, and the branch conduit 9-2 passes through the steam absorption heat pump 3 and the steam-water heat exchanger 4 in sequence.
- the branch pipe 8-1 may be further branched to form two or more secondary branch pipes, each of which passes through a steam absorption heat pump 3 respectively. Convergence.
- the steam absorption heat pump 3 is two or more, and the branch pipe 8-1 may pass through each of the steam absorption heat pumps 3 in order.
- the branch pipe 9-2 can be branched into two secondary branch pipes before passing through the steam absorption heat pump 3, and the secondary branch pipes 9-2-1 pass through the steam absorption heat pump 3 and the steam-water heat exchanger 4 in sequence.
- the secondary branch pipe 9-2-2 is in communication with the primary heat network return pipe 13.
- the apparatus may also include a circulating water cooling device 14.
- the circulating water cooling device (14) can be accessed by any of the following two methods -
- the steam-water heat exchanger 4 can also be replaced by other heating equipment, such as a boiler.
- the heating system may include more than one heat exchange device in addition to the above device; the primary heat network heating device and the heat exchange device pass through a heat network water supply pipe 12 and a heat network backwater The pipe 13 is connected;
- the heat exchange device comprises at least one hot water type absorption heat pump 5, at least one water-water heat exchanger 6, a pipe 10 and a pipe 11;
- the hot water type absorption heat pump 5 comprises: a generator, an evaporation , the condenser, the absorber;
- the pipe 10 sequentially forms a primary heat network system through the generator of the hot water type absorption heat pump 5, the water-water heat exchanger 6 and the evaporator of the hot water type absorption heat pump 5;
- the duct 11 forms a secondary heat network system through an absorber of the hot water type absorption heat pump 5, a condenser of the hot water type absorption heat pump 5, and a water-water heat exchanger 6.
- the pipe 9 communicates with the primary heat network return pipe 13 before passing through the condenser 2, and the branch pipe 9-2 or the secondary branch pipe 9-2-1 passes through the steam-
- the water heat exchanger 4 is connected to the primary heat network water supply pipe 12, and the pipe 10 communicates with the primary heat network water supply pipe 12 before passing through the generator of the hot water type absorption heat pump 5.
- the pipe 9 communicates with the primary heat network return pipe 13 before passing through the condenser 1, and the branch pipe 9-2 or the secondary branch pipe 9-2 - 1 After passing through the steam-water heat exchanger 4, it is in communication with the primary heat network water supply pipe 12, and the pipes 10 of the respective heat exchange devices are in communication with the primary heat network water supply pipe 12.
- the pipe 11 may sequentially pass through an absorber of the hot water type absorption heat pump 5, a condenser of the hot water type absorption heat pump 5, and a water-water heat exchanger 6, as shown in Fig. 1.
- the pipe .11 is composed of at least two independent pipes, and an independent pipe passes through the absorber of the hot water type absorption heat pump 5 and the condenser of the hot water type absorption heat pump 5 in turn, other
- each pipeline passes through a water-water heat exchanger 6, respectively, as shown in Fig. 2.
- the secondary heat network hot water parameters of the absorption heat pump 1 and the secondary heat network hot water parameters of the water-water heat exchanger 2 may be different, and respectively delivered to different heat users through respective secondary network systems.
- the pipe 11 is composed of a main pipe and two branch pipes, and the main pipe 11 is first divided into two branch pipes, branches
- the pipe 11-1 passes through the absorber of the hot water type absorption heat pump 5 and the condenser of the hot water type absorption heat pump 5 in sequence, the branch pipe 11-2 passes through the water-water heat exchanger 6, and then the two branch pipes merge, see image 3.
- the pipe 11 is composed of a main pipe and three branch pipes, and the main pipe 11 is first divided into three branch pipes, branches.
- the pipe 11-1 passes through the absorber of the hot water type absorption heat pump 1 and the condenser of the hot water type absorption heat pump 1, and the branch pipe 11-2 passes through a water-water heat exchanger, and the branch pipe 11-3 passes another A water-water heat exchanger, then three branch pipes merge.
- the pipe 11 is composed of a main pipe and two branch pipes, and the main pipe 11 is first divided into two branch pipes, branches
- the pipe 11-1 passes through the absorber of the hot water type absorption heat pump 1 and the condenser of the hot water type absorption heat pump 1, and the branch pipe 11-2 passes through a water-water heat exchanger, and then the two branch pipes are combined. After passing another water-water heat exchanger.
- the pipe 11 is composed of a main pipe and two branch pipes, and the main pipe 11 is sequentially passed through a hot water type absorption type.
- the absorber of the heat pump 1 and the condenser of the hot water type absorption heat pump 1 are then divided into two branch pipes, the branch pipe 11-1 passes through one water-water heat exchanger, and the branch pipe 11-2 passes through another water- The water heat exchanger, then the two branch pipes meet.
- the hot water type absorption heat pump 1 satisfies the following conditions: After the hot water of the primary heat network passes through the generator of the hot water absorption heat pump 1, the temperature is lowered by 10 to 40 Torr, and the hot water flows out from the water-water heat exchanger 2 After passing through the evaporator of the hot water type absorption heat pump 1, the temperature is lowered by 20 to 40 ⁇ ; after the secondary heat network is returned to the water through the absorber and condenser of the hot water type absorption heat pump 1, the temperature rises by 10 to 30".
- the temperature of the hot water in the primary water supply pipe is 80 to 130 °C.
- Both the primary heat network heating device and the heating system can be applied to central heating.
- the steam absorption heat pump can adopt a multi-stage heat pump device in series with each other, and the multi-stage serial steam absorption heat pump device can be selected from the same model, or different models can be selected according to operating parameters.
- the steam turbine is a steam turbine in a power plant of a power plant; a valve can be installed on the large heat network return pipe 13 and the branch pipe 9-2; and the second branch pipe 9-2-2 can be equipped with an adjustment
- the valve adjusts the amount of bypass water and controls the temperature of the circulating water at the inlet of the condenser, so that the power generation production of the power plant is not affected by the changes of the parameters of the large heat network.
- the heating system includes a device for supplying heat to the primary heating network and two parallel heat exchange devices
- the system schematic is shown in Fig. 4.
- Turbine 1 The final stage exhaust enters the condenser 2 to heat the circulating water, which is cooled and condensed before returning to the boiler for heating.
- the steam extracted by the steam turbine 1 is divided into two paths, one into the steam absorption heat pump 3, which is used as a driving heat source to recover the residual heat of the circulating water and heat the primary heating network, and the other enters the steam-water heat exchanger 4, directly heating the primary heating network, steam The condensate returns to the boiler for heating.
- the circulating cooling water enters the condenser 2, is heated by the steam exhaust of the steam turbine 1 and is sent out, enters the steam absorption heat pump 3, and serves as a low-level heat source, and then returns to the condenser after the heat is cooled down to complete the cycle, if the exhaust heat of the steam turbine 1 is greater than If necessary, a part of the circulating cooling water can be separated into the circulating water cooling device 14 to release the heat.
- the primary heat network returns to the power plant at a low temperature, first enters the condenser 2, is sent to the condenser after being warmed up, and is sent to the steam absorption heat pump 3 to be sent after secondary heating, and then enters the steam-water heat exchanger 4 and is heated three times.
- the power After being heated to the temperature of the hot water supply, the power is sent to the power plant.
- the hot water supply of the hot network is sent to the end heat station. First, it enters the hot water absorption heat pump 5 as the driving heat source. After the heat is cooled, it enters the water-water heat exchanger 6 and heats twice. The hot network supplies hot water. After cooling, it enters the hot water absorption heat pump 5 again as a low-level heat source. After the heat is cooled down to the heat return temperature of the hot network, it returns to the power plant to complete the cycle.
- the heating system of the present invention uses a condenser 2, a steam absorption heat pump 3 inside the power plant and
- the steam-water heat exchanger 4 combines to recover the waste heat of the power plant and heats the hot water of the heat network one by one, and gradually reduces the temperature by the combination of the hot water absorption heat pump 5 and the water-water heat exchanger 6 at the end.
- the heating hot water temperature of the heating network increases the temperature difference between the supply and return water of the hot water.
- FIG. 1 is a schematic flow chart of a first connection mode of a heat exchange device of the present invention.
- FIG. 2 is a schematic flow chart of a second connection mode of the heat exchange device of the present invention.
- FIG. 3 is a schematic flow chart of a third connection mode of the heat exchange device of the present invention.
- Figure 4 is a schematic view of Embodiment 1.
- Figure 5 is a schematic view of Embodiment 2.
- Fig. 6 is a schematic view of a hot water type absorption heat pump applied in the embodiment.
- the hot water type absorption heat pump 5 used in the following embodiments is shown in Fig. 6, and is composed of a generator 5-1, a condenser 5-2, an absorber 5-3, an evaporator 5-4, and a solution heat exchanger 5- 5.
- a dilute solution such as a lithium bromide aqueous solution
- a dilute solution is heated and boiled by the high temperature hot water in the generator to generate a refrigerant vapor and a concentrated solution
- the concentrated solution enters the absorber after being cooled by the solution heat exchanger, and the concentrated solution absorbs the refrigerant vapor to become a dilute solution, and then is heated by the solution heat exchanger and then enters the generator by the solution pump to complete the solution circulation;
- the refrigerant vapor enters the condenser, releases the condensation heat, and condenses into a refrigerant liquid; the refrigerant liquid enters the evaporator through the throttling device to absorb heat and evaporates, and the generated vapor enters the absorber and is absorbed by the solution, completing the refrigerant circulation. .
- Embodiment 1 Application of Central Heating System
- Turbine with condenser 2 assembly 1 C145/n200- 130/535, Dongfang Steam Turbine Co., Ltd.
- Steam-water heat exchanger 4 purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
- Large temperature difference heat exchange unit including hot water type absorption heat pump 5 and water-water heat exchanger 6 Model AHE8000A, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
- connection diagram is shown in Figure 4.
- the device for heating the primary heating network the pipeline 7 passes through the steam turbine 1 and the condenser 2 in sequence; the pipeline 8 is composed of the main road and two branch pipes, and the main road 8 passes through the steam turbine 1 and is divided into two branch pipes, and the branch pipe 8 -1 through the steam absorption heat pump 3, the branch pipe 8-2 passes through the steam-water heat exchanger 4; the pipe 9 is composed of the main pipe and its three branch pipes, and the main road 9 passes through the condenser 2 and is divided into three branch pipes
- the branch pipe 9-1 is connected to the primary heat network return pipe 13 through the steam absorption heat pump 3, and the branch pipe 9-2 can be branched into two secondary branch pipes before passing through the steam absorption heat pump 3, and the secondary branch
- the pipe 9-2-1 passes through the steam absorption heat pump 3 and the steam-water heat exchanger 4 in sequence, the secondary branch pipe 9-2-2 communicates with the primary heat network return pipe 13, and the branch pipe 9-3 is cooled by circulating water.
- the device 14 is then in communication with a primary heat
- Heat exchange device The pipe 10 passes through the generator of the hot water type absorption heat pump 5, the water-water heat exchanger 6 and the evaporator of the hot water type absorption heat pump 5 in sequence; the pipe 11 passes through the hot water type absorption heat pump 5 in sequence.
- Heating system the pipeline 9 is communicated with the primary heat network return pipe 13 before passing through the condenser 2, and the secondary branch pipe 9-2-1 is passed through the steam-water heat exchanger 4 and communicated with the primary heat network water supply pipe 12
- the plurality of heat exchange devices are connected in parallel, and the respective water inlet pipes of the heat exchange device are connected to the primary heat network water supply pipe 12, and the water outlet pipe is connected with the primary heat network return water pipe 13.
- the last stage exhaust steam of the steam turbine 1 enters the condenser to heat the circulating water, and is cooled and condensed before returning to the boiler for heating.
- the steam extracted by the steam turbine 1 is divided into two paths, one into the steam absorption heat pump 3, which is used as a driving heat source to recover the residual heat of the circulating water and heat the primary heating network, and the other enters the steam-water heat exchanger 4, directly heating the primary heating network, steam The condensate returns to the boiler for heating.
- the circulating cooling water enters the condenser 2, is heated by the steam exhaust of the steam turbine 1 and is sent out, enters the steam absorption heat pump 3, and acts as a low-level heat source, and then returns to the condenser after the heat is cooled down to complete the cycle, such as the exhaust heat of the steam turbine 1 Then, it is discharged to the environment through the circulating water cooling device 14.
- the primary heat network returns to the power plant at a low temperature, first enters the condenser 2, is warmed up and sent out, and is sent to the steam absorption heat pump 3 to be sent after secondary heating, and then enters the steam-water heat exchanger 3 and is heated three times.
- the power After being heated to the temperature of the hot water supply, the power is sent to the power plant, and the hot water supply of the hot network is sent to the end heat station, first entering the hot water as the driving heat source.
- the invention adopts a combined heating mode of a condenser, a steam absorption heat pump and a steam-water heat exchanger in a power plant, and adopts a combination of a hot water absorption heat pump and a water-water heat exchanger at the end.
- the waste heat generated in the power generation process of the power plant is effectively recovered.
- the temperature difference between the supply and return water of the primary heat network is greatly increased compared with the conventional centralized heating mode.
- Turbine with condenser 2 assembly 1 C145/n200- 130/535, Dongfang Steam Turbine Co., Ltd.
- Steam absorption heat pump 3a Model SHP1300, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
- Steam absorption heat pump 3b Model DHP1750, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
- Model AHE8000A purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
- connection diagram is shown in Figure 5.
- Three-stage steam absorption heat pump 3 is used for series heating.
- the device for supplying heat to the heat network the pipe 7 passes through the steam turbine 1 and the condenser 2 in sequence; the pipe 8 is composed of the main pipe and its two branch pipes, and the main pipe passes through the steam turbine 1 and is divided into two branch pipes, and the branch pipe 8- 1 further branching, forming three secondary branch pipes, respectively passing through the steam absorption heat pump 3a, the steam absorption heat pump 3b, the steam absorption heat pump 3c, and the branch pipe 8-2 passing through the steam-water heat exchanger 4;
- the main pipe 9 is divided into three branch pipes through the condenser 2, and the branch pipe 9-1 is divided into three branches respectively through the steam absorption heat pump 3a, the steam absorption heat pump 3b, and the steam.
- the absorption heat pump 3c After the absorption heat pump 3c is merged, it is connected to the primary heat network return pipe 13, and the branch pipe 9-2 can be branched into two secondary branch pipes before passing through the steam absorption heat pump 3, and the secondary branch pipes 9-2-1 pass sequentially.
- Steam absorption heat pump 3a, The steam absorption heat pump 3b, the steam absorption heat pump 3c and the steam-water heat exchanger 4, the secondary branch pipe 9-2-2 communicate with the primary heat network return pipe 13, and the branch pipe 9-3 passes the circulating water cooling device 14. It communicates with the primary heat network return pipe 13.
- Heat exchange device The pipe 10 passes through the generator of the hot water type absorption heat pump 5, the water-water heat exchanger 6 and the evaporator of the hot water type absorption heat pump 5 in sequence; the pipe 11 passes through the hot water type absorption heat pump 5 in sequence.
- the pipeline 9 communicates with the primary heat network return pipe 13 before passing through the condenser 2, and the secondary branch pipe 9-2-1 passes through the steam-water heat exchanger 4 and communicates with the primary heat network water supply pipe 12,
- the heat exchange devices are connected in parallel, and the respective water inlet pipes of the heat exchange device are connected to the primary heat network water supply pipe 12, and the water outlet pipe is connected to the primary heat network return water pipe 13.
- the steam exhaust of the first stage of the steam turbine enters the condenser to heat the circulating water, which is cooled and condensed before returning to the boiler for heating.
- the steam extracted by the steam turbine 1 is divided into two paths, one into a first-stage steam absorption heat pump 3a, a second-stage steam absorption heat pump 3b, and a third-stage steam absorption heat pump 3c, which are used as a driving heat source to recover the residual heat of the circulating water and are heated step by step.
- the circulating cooling water enters the condenser 2, is heated by the steam exhaust of the steam turbine 1, and is sent out to enter the first-stage steam absorption heat pump 3a, the second-stage steam absorption heat pump 3b, and the third-stage steam absorption heat pump 3c as low-level heat sources. After the heat is cooled, it is returned to the condenser to complete the cycle, and excess heat is discharged to the environment through the circulating water cooling device 14.
- the primary heating network returns to the power plant at a low temperature, first enters the condenser 2, is warmed up and sent out, and passes through the first-stage steam absorption heat pump 3a, the secondary steam absorption heat pump 3b and the third-stage steam absorption heat pump 3c.
- the high-temperature water supply of the hot network is sent to the end heat station, and firstly enters the hot water as the driving heat source.
- the features of the invention are mainly embodied in three aspects: 1) preheating the primary heat network backwater by using the steam exhaust of the steam turbine, and using the circulating cooling water as the low heat source of the absorption heat pump, the advantage is effective recovery The waste heat generated during the power generation process of the power plant; 2) The condenser network, the steam absorption heat pump and the steam-water heat exchanger are used to heat the hot water of the hot network three times, which has the advantages of increasing the temperature of the hot water supply and increasing the heat once.
Abstract
A kind of concentrated heat-supply system includes a steam turbine (1), which has a condenser (2), at least a steam absorption type heat pump (3), a steam-water heat exchanger (4) and pipes (7, 8, 9). The exhausted steam of the steam turbine (1) is used to pre-heat the back-water of the first heat network, and drive the steam absorption type heat pump (3). The hot water of the heat network is heated by the condenser (2), the steam absorption type heat pump (3) and the steam-water heat exchanger (4) for three times. At the end, the heat-supply hot water of the second network is heated by a hot water absorption type heat pump (5) and a water-water heat exchanger (6) in a combination form.
Description
一种集中供热系统 技术领域 Central heating system
本发明涉及一种集中供热系统。 The invention relates to a central heating system.
背景技术 Background technique
随着城市规模的不断发展, 集中供热面积不断增大, 带来了两个方面 的问题: 1 ) 集中供热热源的能力不足。 新建大型的热源投资高、 建设周 期长,并且受到环境容量的强烈制约,一些地方盲目发展小型燃煤锅炉房, 给大气带来了严重的污染, 一些地方盲目发展燃气采暖、 甚至电采暖, 在 带来采暖高成本的同时, 造成了燃气、 电力的全面紧张。 2 ) 热源产生的 高温热水往往需要经过较长距离的输送才能到达末端用户。 目前城市集中 供热的一次网供、 回水温度一般为 120°C和 60°C左右, 由于受到二次网用 热要求的限制, 回水温度利用常规的换热器己经无法再降低了, 因此热水 的输送量非常大, 使得供热半径小、 管道投资大以及水泵运行电耗大等问 题日益凸现。 With the continuous development of the city scale, the district heating area is increasing, which brings about two problems: 1) The ability to centrally supply heat sources is insufficient. The new large-scale heat source has high investment, long construction period, and is strongly restricted by environmental capacity. Some places have blindly developed small coal-fired boiler houses, which have brought serious pollution to the atmosphere. Some places have blindly developed gas heating and even electric heating. At the same time, the high cost of heating brings about the overall tension of gas and electricity. 2) High-temperature hot water generated by heat sources often needs to be transported over a long distance to reach the end user. At present, the primary network supply and return water temperature of urban central heating is generally about 120 ° C and 60 ° C. Due to the limitation of the secondary network heat requirements, the return water temperature can no longer be reduced by using conventional heat exchangers. Therefore, the amount of hot water delivered is very large, which makes the heating radius small, the pipeline investment and the power consumption of the pump run more and more prominent.
火力发电厂内还有大量的循环水余热资源没有得到有效利用, 白白浪 费掉了。如果能够利用火力发电厂循环水供热,相当于在不增加电厂容量、 不增加当地排放的情况下,扩大了热源的供热能力,但因为其热能品质低, 目前尚没有得到有效的利用。 There is still a large amount of circulating water waste heat resources in the thermal power plant that have not been effectively utilized, and the white waves have been spent. If we can use the circulating water supply of thermal power plants, it is equivalent to expanding the heat supply capacity of the heat source without increasing the capacity of the power plant and increasing the local emissions. However, due to its low thermal energy quality, it has not been effectively utilized.
发明公开 Invention disclosure
本发明的目的是提供一种集中供热系统。 It is an object of the invention to provide a central heating system.
本发明提供了一种给一次热网供热的装置. The present invention provides a device for supplying heat to a heating network.
本发明提供的给一次网供热的装置包括: 含有凝汽器 2的汽轮机 1、 至少一台蒸汽吸收式热泵 3、 汽-水换热器 4、 管道 7、 管道 8和管道 9; 管道 7依次通过汽轮机 1和凝汽器 2 ; The apparatus for heating a primary network provided by the present invention comprises: a steam turbine including a condenser 2, at least one steam absorption heat pump 3, a steam-water heat exchanger 4, a pipe 7, a pipe 8 and a pipe 9; Passing through the steam turbine 1 and the condenser 2 in sequence;
管道 8由主干管及其两支分支管道组成, 主干管 8通过汽轮机 1后分 成两支分支管道, 分支管道 8-1通过蒸汽吸收式热泵 3, 分支管道 8- 2通 过汽-水换热器 4; The pipe 8 is composed of a main pipe and two branch pipes. The main pipe 8 passes through the steam turbine 1 and is divided into two branch pipes. The branch pipe 8-1 passes through the steam absorption heat pump 3, and the branch pipe 8-2 passes through the steam-water heat exchanger. 4;
管道 9由主干管及其两支分支管道组成, 主干管 9通过凝汽器 2后分 成两支分支管道, 分支管道 9-1通过蒸汽吸收式热泵 3后与一次网回水管
道 13相通, 分支管道 9-2依次通过蒸汽吸收式热泵 3和汽-水换热器 4。 所述蒸汽吸收式热泵 3为两台以上时, 所述分支管道 8-1可进一步分 支, 形成两个以上二级分支管道, 每个所述二级分支管道分别通过一个蒸 汽吸收式热泵 3后再汇合。 The pipe 9 is composed of a main pipe and two branch pipes. The main pipe 9 passes through the condenser 2 and is divided into two branch pipes. The branch pipe 9-1 passes through the steam absorption heat pump 3 and the primary network return pipe. The passage 13 communicates, and the branch conduit 9-2 passes through the steam absorption heat pump 3 and the steam-water heat exchanger 4 in sequence. When the steam absorption heat pump 3 is two or more, the branch pipe 8-1 may be further branched to form two or more secondary branch pipes, each of which passes through a steam absorption heat pump 3 respectively. Convergence.
所述蒸汽吸收式热泵 3为两台以上, 所述分支管道 8-1也可依次通过 每个蒸汽吸收式热泵 3。 The steam absorption heat pump 3 is two or more, and the branch pipe 8-1 may pass through each of the steam absorption heat pumps 3 in order.
所述分支管道 9-2在通过蒸汽吸收式热泵 3前可分支为两支二级分支 管道, 二级分支管道 9-2-1依次通过蒸汽吸收式热泵 3和汽-水换热器 4, 二级分支管道 9-2-2与一次热网回水管道 13相通。 The branch pipe 9-2 can be branched into two secondary branch pipes before passing through the steam absorption heat pump 3, and the secondary branch pipes 9-2-1 pass through the steam absorption heat pump 3 and the steam-water heat exchanger 4 in sequence. The secondary branch pipe 9-2-2 is in communication with the primary heat network return pipe 13.
所述装置还可包括循环水冷却装置 14。 所述循环水冷却装置(14 )可 通过如下两种方式中的任一种接入- The apparatus may also include a circulating water cooling device 14. The circulating water cooling device (14) can be accessed by any of the following two methods -
①串接于分支管道 9-1的吸收式热泵 3出口管段上; 1 is connected in series to the outlet pipe section of the absorption heat pump 3 of the branch pipe 9-1;
②并联于分支管道 9-1的吸收式热泵 3的出口管段。 2 Connected to the outlet pipe section of the absorption heat pump 3 of the branch pipe 9-1.
所述汽 -水换热器 4也可以用其他加热设备代替, 如锅炉。 The steam-water heat exchanger 4 can also be replaced by other heating equipment, such as a boiler.
含有所述给一次热网供热装置的供热系统也属于本发明的保护范围。 所述供热系统除上述装置外, 还可包括一个以上的换热装置; 所述给 一次热网供热装置与所述换热装置之间通过一次热网供水管道 12 和一次 热网回水管道 13连通; It is also within the scope of the present invention to include a heating system for the primary heating network heating device. The heating system may include more than one heat exchange device in addition to the above device; the primary heat network heating device and the heat exchange device pass through a heat network water supply pipe 12 and a heat network backwater The pipe 13 is connected;
所述换热装置, 包括至少一台热水型吸收式热泵 5、至少一台水-水换 热器 6、 管道 10和管道 11 ; 所述热水型吸收式热泵 5包括: 发生器、 蒸 发器、 冷凝器、 吸收器; 所述管道 10依次通过热水型吸收式热泵 5的发 生器、 水-水换热器 6和热水型吸收式热泵 5的蒸发器形成一次热网系统; 所述管道 11通过热水型吸收式热泵 5的吸收器、 热水型吸收式热泵 5的 冷凝器和水-水换热器 6形成二次热网系统。 The heat exchange device comprises at least one hot water type absorption heat pump 5, at least one water-water heat exchanger 6, a pipe 10 and a pipe 11; the hot water type absorption heat pump 5 comprises: a generator, an evaporation , the condenser, the absorber; the pipe 10 sequentially forms a primary heat network system through the generator of the hot water type absorption heat pump 5, the water-water heat exchanger 6 and the evaporator of the hot water type absorption heat pump 5; The duct 11 forms a secondary heat network system through an absorber of the hot water type absorption heat pump 5, a condenser of the hot water type absorption heat pump 5, and a water-water heat exchanger 6.
所述供热系统包括一个所述换热装置时, 管道 9通过凝汽器 2前与一 次热网回水管道 13相通, 分支管道 9-2或二级分支管道 9-2-1通过汽-水 换热器 4后与一次热网供水管道 12相通, 管道 10通过热水型吸收式热泵 5的发生器前与一次热网供水管道 12相通。 When the heating system includes one of the heat exchange devices, the pipe 9 communicates with the primary heat network return pipe 13 before passing through the condenser 2, and the branch pipe 9-2 or the secondary branch pipe 9-2-1 passes through the steam- The water heat exchanger 4 is connected to the primary heat network water supply pipe 12, and the pipe 10 communicates with the primary heat network water supply pipe 12 before passing through the generator of the hot water type absorption heat pump 5.
所述供热系统包括两个以上并联的所述换热装置时, 管道 9通过凝汽 器 1前与一次热网回水管道 13相通,分支管道 9-2或二级分支管道 9- 2 - 1
通过汽 -水换热器 4后与一次热网供水管道 12相通, 各个换热装置的管道 10与一次热网供水管 12相通。 When the heating system includes two or more heat exchange devices connected in parallel, the pipe 9 communicates with the primary heat network return pipe 13 before passing through the condenser 1, and the branch pipe 9-2 or the secondary branch pipe 9-2 - 1 After passing through the steam-water heat exchanger 4, it is in communication with the primary heat network water supply pipe 12, and the pipes 10 of the respective heat exchange devices are in communication with the primary heat network water supply pipe 12.
所述换热装置中, 所述管道 11可依次通过热水型吸收式热泵 5的吸 收器、 热水型吸收式热泵 5的冷凝器和水 -水换热器 6, 见图 1。 In the heat exchange device, the pipe 11 may sequentially pass through an absorber of the hot water type absorption heat pump 5, a condenser of the hot water type absorption heat pump 5, and a water-water heat exchanger 6, as shown in Fig. 1.
所述换热装置中, 所述管道.11 由至少两支独立的管道组成, 一支独 立管道依次通过热水型吸收式热泵 5的吸收器和热水型吸收式热泵 5的冷 凝器, 其它管道中, 每支管道分别通过一台水-水换热器 6, 见图 2。 In the heat exchange device, the pipe .11 is composed of at least two independent pipes, and an independent pipe passes through the absorber of the hot water type absorption heat pump 5 and the condenser of the hot water type absorption heat pump 5 in turn, other In the pipeline, each pipeline passes through a water-water heat exchanger 6, respectively, as shown in Fig. 2.
通过吸收式热泵 1 的二次热网热水参数和通过水-水换热器 2的二次 热网热水参数可不相同, 分别通过各自的二次网系统输送到不同的热用 户。 The secondary heat network hot water parameters of the absorption heat pump 1 and the secondary heat network hot water parameters of the water-water heat exchanger 2 may be different, and respectively delivered to different heat users through respective secondary network systems.
所述换热装置包括一台水-水换热器 6 时, 所述换热装置中, 所述管 道 11由主干管及其两支分支管道组成, 主干管 11先分成两支分支管道, 分支管道 11-1依次通过热水型吸收式热泵 5的吸收器和热水型吸收式热 泵 5的冷凝器, 分支管道 11-2通过水-水换热器 6, 然后两支分支管道汇 合, 见图 3。 When the heat exchange device comprises a water-water heat exchanger 6, in the heat exchange device, the pipe 11 is composed of a main pipe and two branch pipes, and the main pipe 11 is first divided into two branch pipes, branches The pipe 11-1 passes through the absorber of the hot water type absorption heat pump 5 and the condenser of the hot water type absorption heat pump 5 in sequence, the branch pipe 11-2 passes through the water-water heat exchanger 6, and then the two branch pipes merge, see image 3.
所述换热装置包括两台水-水换热器 2时, 所述换热装置中, 所述管 道 11由主干管及其三支分支管道组成, 主干管 11先分成三支分支管道, 分支管道 11-1依次通过热水型吸收式热泵 1的吸收器和热水型吸收式热 泵 1的冷凝器, 分支管道 11-2通过一台水 -水换热器, 分支管道 11-3通 过另一台水 -水换热器,然后三支分支管道汇合。 When the heat exchange device comprises two water-water heat exchangers 2, in the heat exchange device, the pipe 11 is composed of a main pipe and three branch pipes, and the main pipe 11 is first divided into three branch pipes, branches. The pipe 11-1 passes through the absorber of the hot water type absorption heat pump 1 and the condenser of the hot water type absorption heat pump 1, and the branch pipe 11-2 passes through a water-water heat exchanger, and the branch pipe 11-3 passes another A water-water heat exchanger, then three branch pipes merge.
所述换热装置包括两台水-水换热器 2时, 所述换热装置中, 所述管 道 11由主干管及其两支分支管道组成, 主干管 11先分成两支分支管道, 分支管道 11-1依次通过热水型吸收式热泵 1的吸收器和热水型吸收式热 泵 1的冷凝器, 分支管道 11-2通过一台水 -水换热器, 然后两支分支管道 汇合成后通过另一台水 -水换热器。 When the heat exchange device comprises two water-water heat exchangers 2, in the heat exchange device, the pipe 11 is composed of a main pipe and two branch pipes, and the main pipe 11 is first divided into two branch pipes, branches The pipe 11-1 passes through the absorber of the hot water type absorption heat pump 1 and the condenser of the hot water type absorption heat pump 1, and the branch pipe 11-2 passes through a water-water heat exchanger, and then the two branch pipes are combined. After passing another water-water heat exchanger.
所述换热装置包括两台水-水换热器 2时, 所述换热装置中, 所述管 道 11由主干管及其两支分支管道组成, 主干管 11先依次通过热水型吸收 式热泵 1的吸收器和热水型吸收式热泵 1的冷凝器, 然后分成两支分支管 道, 分支管道 11- 1通过一台水-水换热器, 分支管道 11- 2通过另一台水- 水换热器, 然后两支分支管道汇合。
所述热水型吸收式热泵 1满足如下条件: 一次热网的热水通过热水吸 收式热泵 1的发生器后, 温度降低 10〜40Ό, 从水-水换热器 2中流出的 热水通过热水型吸收式热泵 1的蒸发器后, 温度降低 20〜40Ό ; 二次热网 热水回水通过热水型吸收式热泵 1的吸收器和冷凝器后,温度升高 10〜30 "C o When the heat exchange device comprises two water-water heat exchangers 2, in the heat exchange device, the pipe 11 is composed of a main pipe and two branch pipes, and the main pipe 11 is sequentially passed through a hot water type absorption type. The absorber of the heat pump 1 and the condenser of the hot water type absorption heat pump 1 are then divided into two branch pipes, the branch pipe 11-1 passes through one water-water heat exchanger, and the branch pipe 11-2 passes through another water- The water heat exchanger, then the two branch pipes meet. The hot water type absorption heat pump 1 satisfies the following conditions: After the hot water of the primary heat network passes through the generator of the hot water absorption heat pump 1, the temperature is lowered by 10 to 40 Torr, and the hot water flows out from the water-water heat exchanger 2 After passing through the evaporator of the hot water type absorption heat pump 1, the temperature is lowered by 20 to 40 Ό; after the secondary heat network is returned to the water through the absorber and condenser of the hot water type absorption heat pump 1, the temperature rises by 10 to 30". C o
通常一次网供水管热水的温度为 80〜130°C。 Usually, the temperature of the hot water in the primary water supply pipe is 80 to 130 °C.
所述一次热网供热装置和所述供热系统均可应用于集中供热中。 Both the primary heat network heating device and the heating system can be applied to central heating.
所述蒸汽吸收式热泵可以采用多级热泵设备相互串联的方式, 多级串 联的蒸汽吸收式热泵设备可以选用相同型号的, 也可以根据运行参数选用 不同型号的。 The steam absorption heat pump can adopt a multi-stage heat pump device in series with each other, and the multi-stage serial steam absorption heat pump device can be selected from the same model, or different models can be selected according to operating parameters.
所述汽轮机为电厂发电设备中的汽轮机; 在所述大热网回水管道 13 和分支管道 9-2上可装有阀门; 在所述二级分支管道 9-2-2上可装有调节 阀, 调节旁通水量, 控制凝汽器进口的循环水温度, 使电厂发电生产不会 受到大热网参数变化的影响。 The steam turbine is a steam turbine in a power plant of a power plant; a valve can be installed on the large heat network return pipe 13 and the branch pipe 9-2; and the second branch pipe 9-2-2 can be equipped with an adjustment The valve adjusts the amount of bypass water and controls the temperature of the circulating water at the inlet of the condenser, so that the power generation production of the power plant is not affected by the changes of the parameters of the large heat network.
当所述供热系统包括一个给一次热网供热的装置和两个并联的换热 装置时, 系统示意图见图 4。 汽轮机 1末级排汽进入凝汽器 2中加热循环 水, 被冷却凝结后再返回锅炉加热。 由汽轮机 1抽出的蒸汽分为两路, 一 路进入蒸汽吸收式热泵 3,作为驱动热源回收循环水余热并加热一次热网, 另一路进入汽-水换热器 4, 直接加热一次热网, 蒸汽凝水返回锅炉加热。 循环冷却水进入凝汽器 2中, 被汽轮机 1排汽加热后送出, 进入蒸汽吸收 式热泵 3, 作为低位热源, 放热降温后再返回凝汽器, 完成循环, 若汽轮 机 1排汽热量大于所需, 则可分出一部分循环冷却水进入循环水冷却装置 14放热降温。 一次热网低温回水返回电厂, 首先进入凝汽器 2, 被预热升 温后送出, 进入蒸汽吸收式热泵 3 被二次加热后送出, 再进入汽-水换热 器 4中被三次加热, 加热到一次热网供水温度后送出电厂, 一次热网高温 供水被输送到末端热力站, 首先作为驱动热源进入热水吸收式热泵 5, 放 热降温后进入水-水换热器 6 加热二次热网供热热水, 降温后再次进入热 水吸收式热泵 5作为低位热源, 最终放热降温到一次热网回水温度后返回 电厂, 完成循环。 When the heating system includes a device for supplying heat to the primary heating network and two parallel heat exchange devices, the system schematic is shown in Fig. 4. Turbine 1 The final stage exhaust enters the condenser 2 to heat the circulating water, which is cooled and condensed before returning to the boiler for heating. The steam extracted by the steam turbine 1 is divided into two paths, one into the steam absorption heat pump 3, which is used as a driving heat source to recover the residual heat of the circulating water and heat the primary heating network, and the other enters the steam-water heat exchanger 4, directly heating the primary heating network, steam The condensate returns to the boiler for heating. The circulating cooling water enters the condenser 2, is heated by the steam exhaust of the steam turbine 1 and is sent out, enters the steam absorption heat pump 3, and serves as a low-level heat source, and then returns to the condenser after the heat is cooled down to complete the cycle, if the exhaust heat of the steam turbine 1 is greater than If necessary, a part of the circulating cooling water can be separated into the circulating water cooling device 14 to release the heat. The primary heat network returns to the power plant at a low temperature, first enters the condenser 2, is sent to the condenser after being warmed up, and is sent to the steam absorption heat pump 3 to be sent after secondary heating, and then enters the steam-water heat exchanger 4 and is heated three times. After being heated to the temperature of the hot water supply, the power is sent to the power plant. The hot water supply of the hot network is sent to the end heat station. First, it enters the hot water absorption heat pump 5 as the driving heat source. After the heat is cooled, it enters the water-water heat exchanger 6 and heats twice. The hot network supplies hot water. After cooling, it enters the hot water absorption heat pump 5 again as a low-level heat source. After the heat is cooled down to the heat return temperature of the hot network, it returns to the power plant to complete the cycle.
本发明的供热系统, 在电厂内部采用凝汽器 2、 蒸汽吸收式热泵 3和
汽-水换热器 4组合的方式回收电厂余热并逐级加热一次热网的供热热水, 在末端利用热水吸收式热泵 5和水-水换热器 6组合的方式逐级降低一次 热网的供热热水温度, 增大了高温热水的供、 回水温差。 The heating system of the present invention uses a condenser 2, a steam absorption heat pump 3 inside the power plant and The steam-water heat exchanger 4 combines to recover the waste heat of the power plant and heats the hot water of the heat network one by one, and gradually reduces the temperature by the combination of the hot water absorption heat pump 5 and the water-water heat exchanger 6 at the end. The heating hot water temperature of the heating network increases the temperature difference between the supply and return water of the hot water.
附图说明 DRAWINGS
图 1为本发明换热装置第一种连接方式的流程示意图。 1 is a schematic flow chart of a first connection mode of a heat exchange device of the present invention.
图 2为本发明换热装置第二种连接方式的流程示意图。 2 is a schematic flow chart of a second connection mode of the heat exchange device of the present invention.
图 3为本发明换热装置第三种连接方式的流程示意图。 3 is a schematic flow chart of a third connection mode of the heat exchange device of the present invention.
图 4为实施例 1的示意图。 Figure 4 is a schematic view of Embodiment 1.
图 5为实施例 2的示意图。 Figure 5 is a schematic view of Embodiment 2.
图 6为实施例中所应用的热水型吸收式热泵示意图。 Fig. 6 is a schematic view of a hot water type absorption heat pump applied in the embodiment.
实施发明的最佳方式 The best way to implement the invention
下面结合具体实施例, 对本发明的具体实施方式进行说明。 Specific embodiments of the present invention will be described below in conjunction with specific embodiments.
以下实施例中所用的热水型吸收式热泵 5如图 6所示, 由发生器 5-1、 冷凝器 5-2、 吸收器 5-3、 蒸发器 5-4、 溶液热交换器 5-5、 节流装置 5 - 6、 溶液泵 5-7、 冷剂泵 5-8以及各类连接管路组成。 The hot water type absorption heat pump 5 used in the following embodiments is shown in Fig. 6, and is composed of a generator 5-1, a condenser 5-2, an absorber 5-3, an evaporator 5-4, and a solution heat exchanger 5- 5. Throttle device 5 - 6, solution pump 5-7, refrigerant pump 5-8 and various connecting pipes.
热水型吸收式热泵工作时, 稀溶液 (如溴化锂水溶液) 在发生器中被 高温热水加热沸腾, 产生冷剂蒸汽和浓溶液; When the hot water type absorption heat pump is working, a dilute solution (such as a lithium bromide aqueous solution) is heated and boiled by the high temperature hot water in the generator to generate a refrigerant vapor and a concentrated solution;
浓溶液通过溶液热交换器降温后进入吸收器, 浓溶液吸收冷剂蒸汽, 成为稀溶液, 再在溶液泵的驱动下通过溶液热交换器升温后进入发生器 中, 完成了溶液循环; The concentrated solution enters the absorber after being cooled by the solution heat exchanger, and the concentrated solution absorbs the refrigerant vapor to become a dilute solution, and then is heated by the solution heat exchanger and then enters the generator by the solution pump to complete the solution circulation;
冷剂蒸汽进入冷凝器中, 放出凝结热, 凝结为冷剂液; 冷剂液通过节 流装置进入蒸发器中吸热蒸发, 产生出的蒸气进入吸收器中被溶液吸收, 完成了冷剂循环。 The refrigerant vapor enters the condenser, releases the condensation heat, and condenses into a refrigerant liquid; the refrigerant liquid enters the evaporator through the throttling device to absorb heat and evaporates, and the generated vapor enters the absorber and is absorbed by the solution, completing the refrigerant circulation. .
实施例 1、 集中供热系统的应用 Embodiment 1. Application of Central Heating System
一、 组装 First, assembly
含有凝汽器 2组件的汽轮机 1 : C145/n200- 130/535, 东方汽轮机有限 公司。 Turbine with condenser 2 assembly 1 : C145/n200- 130/535, Dongfang Steam Turbine Co., Ltd.
蒸汽吸收式热泵 3 : 型号为 DHP1750 , 购自北京环能瑞通科技发展有 限公司。 Steam absorption heat pump 3 : Model DHP1750, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
汽-水换热器 4: 购自北京环能瑞通科技发展有限公司。
包括热水型吸收式热泵 5和水-水换热器 6的大温差换热机组: 型号 为 AHE8000A, 购自北京环能瑞通科技发展有限公司。 Steam-water heat exchanger 4: purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd. Large temperature difference heat exchange unit including hot water type absorption heat pump 5 and water-water heat exchanger 6: Model AHE8000A, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
连接示意图见图 4。 The connection diagram is shown in Figure 4.
给一次热网供热的装置: 管道 7依次通过汽轮机 1和凝汽器 2 ; 管道 8由主干道及其两支分支管道组成, 主干道 8通过汽轮机 1后分成两支分 支管道, 分支管道 8-1通过蒸汽吸收式热泵 3, 分支管道 8- 2通过汽 -水换 热器 4; 管道 9由主干管及其三支分支管道组成, 主干道 9通过凝汽器 2 后分成三支分支管道, 分支管道 9-1通过蒸汽吸收式热泵 3后与一次热网 回水管道 13相通, 分支管道 9-2在通过蒸汽吸收式热泵 3前又可分支为 两支二级分支管道, 二级分支管道 9- 2-1依次通过蒸汽吸收式热泵 3和汽 -水换热器 4, 二级分支管道 9- 2- 2与一次热网回水管道 13相通, 分支管 道 9-3通过循环水冷却装置 14后与一次热网回水管道 13相通。 The device for heating the primary heating network: the pipeline 7 passes through the steam turbine 1 and the condenser 2 in sequence; the pipeline 8 is composed of the main road and two branch pipes, and the main road 8 passes through the steam turbine 1 and is divided into two branch pipes, and the branch pipe 8 -1 through the steam absorption heat pump 3, the branch pipe 8-2 passes through the steam-water heat exchanger 4; the pipe 9 is composed of the main pipe and its three branch pipes, and the main road 9 passes through the condenser 2 and is divided into three branch pipes The branch pipe 9-1 is connected to the primary heat network return pipe 13 through the steam absorption heat pump 3, and the branch pipe 9-2 can be branched into two secondary branch pipes before passing through the steam absorption heat pump 3, and the secondary branch The pipe 9-2-1 passes through the steam absorption heat pump 3 and the steam-water heat exchanger 4 in sequence, the secondary branch pipe 9-2-2 communicates with the primary heat network return pipe 13, and the branch pipe 9-3 is cooled by circulating water. The device 14 is then in communication with a primary heat network return conduit 13.
换热装置: 管道 10依次通过热水型吸收式热泵 5的发生器、 水-水换 热器 6和热水型吸收式热泵 5的蒸发器; 管道 11依次通过热水型吸收式 热泵 5的吸收器、 .热水型吸收式热泵 5的冷凝器和水-水换热器 6。 Heat exchange device: The pipe 10 passes through the generator of the hot water type absorption heat pump 5, the water-water heat exchanger 6 and the evaporator of the hot water type absorption heat pump 5 in sequence; the pipe 11 passes through the hot water type absorption heat pump 5 in sequence. An absorber, a condenser of the hot water type absorption heat pump 5, and a water-water heat exchanger 6.
供热系统: 将管道 9通过凝汽器 2·前与一次热网回水管道 13相通, 二级分支管道 9-2-1通过汽-水换热器 4后与一次热网供水管道 12相通, 多个换热装置并联, 换热装置各自的进水管道与一次热网供水管道 12 连 接, 出水管道与一次热网回水管道 13连接。 Heating system: the pipeline 9 is communicated with the primary heat network return pipe 13 before passing through the condenser 2, and the secondary branch pipe 9-2-1 is passed through the steam-water heat exchanger 4 and communicated with the primary heat network water supply pipe 12 The plurality of heat exchange devices are connected in parallel, and the respective water inlet pipes of the heat exchange device are connected to the primary heat network water supply pipe 12, and the water outlet pipe is connected with the primary heat network return water pipe 13.
二、 应用 Second, the application
汽轮机 1末级排汽进入凝汽器中加热循环水, 被冷却凝结后再返回锅 炉加热。 由汽轮机 1抽出的蒸汽分为两路, 一路进入蒸汽吸收式热泵 3, 作为驱动热源回收循环水余热并加热一次热网, 另一路进入汽 -水换热器 4, 直接加热一次热网, 蒸汽凝水返回锅炉加热。 循环冷却水进入凝汽器 2 中, 被汽轮机 1排汽加热后送出, 进入蒸汽吸收式热泵 3, 作为低位热源, 放热降温后再返回凝汽器, 完成循环, 如汽轮机 1排汽热量多余, 则通过 循环水冷却装置 14 排放到环境。 一次热网低温回水返回电厂, 首先进入 凝汽器 2, 被预热升温后送出, 进入蒸汽吸收式热泵 3被二次加热后送出, 再进入汽-水换热器 3 中被三次加热, 加热到一次热网供水温度后送出电 厂, 一次热网高温供水被输送到末端热力站, 首先作为驱动热源进入热水
吸收式热泵 5, 放热降温后进入水-水换热器 6加热二次热网供热热水, 降 温后再次进入热水吸收式热泵 5作为低位热源, 最终放热降温到一次热网 回水温度后返回电厂, 完成循环。 The last stage exhaust steam of the steam turbine 1 enters the condenser to heat the circulating water, and is cooled and condensed before returning to the boiler for heating. The steam extracted by the steam turbine 1 is divided into two paths, one into the steam absorption heat pump 3, which is used as a driving heat source to recover the residual heat of the circulating water and heat the primary heating network, and the other enters the steam-water heat exchanger 4, directly heating the primary heating network, steam The condensate returns to the boiler for heating. The circulating cooling water enters the condenser 2, is heated by the steam exhaust of the steam turbine 1 and is sent out, enters the steam absorption heat pump 3, and acts as a low-level heat source, and then returns to the condenser after the heat is cooled down to complete the cycle, such as the exhaust heat of the steam turbine 1 Then, it is discharged to the environment through the circulating water cooling device 14. The primary heat network returns to the power plant at a low temperature, first enters the condenser 2, is warmed up and sent out, and is sent to the steam absorption heat pump 3 to be sent after secondary heating, and then enters the steam-water heat exchanger 3 and is heated three times. After being heated to the temperature of the hot water supply, the power is sent to the power plant, and the hot water supply of the hot network is sent to the end heat station, first entering the hot water as the driving heat source. The absorption heat pump 5, after the heat release and cooling, enters the water-water heat exchanger 6 to heat the secondary heat network to supply hot water, and then enters the hot water absorption heat pump 5 as a low-level heat source after cooling, and finally releases the heat to a heat network back. Return to the power plant after the water temperature, complete the cycle.
可以看出, 本发明在电厂内采用了凝汽器、 蒸汽吸收式热泵和汽-水 换热器组合加热方式, 在末端采用热水吸收式热泵和水-水换热器组合换 热的方式, 一方面有效回收了电厂发电过程中产生的余热, 另一方面使一 次热网的供、 回水温差较常规的集中供热方式有大幅增大。 It can be seen that the invention adopts a combined heating mode of a condenser, a steam absorption heat pump and a steam-water heat exchanger in a power plant, and adopts a combination of a hot water absorption heat pump and a water-water heat exchanger at the end. On the one hand, the waste heat generated in the power generation process of the power plant is effectively recovered. On the other hand, the temperature difference between the supply and return water of the primary heat network is greatly increased compared with the conventional centralized heating mode.
实施例 2、 集中供热系统的应用 Example 2, Application of Central Heating System
一、 组装 First, assembly
含有凝汽器 2组件的汽轮机 1 : C145/n200- 130/535, 东方汽轮机有限 公司。 Turbine with condenser 2 assembly 1 : C145/n200- 130/535, Dongfang Steam Turbine Co., Ltd.
蒸汽吸收式热泵 3a: 型号为 SHP1300 , 购自北京环能瑞通科技发展有 限公司。 Steam absorption heat pump 3a: Model SHP1300, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
蒸汽吸收式热泵 3b : 型号为 DHP1750 , 购自北京环能瑞通科技发展有 限公司。 Steam absorption heat pump 3b: Model DHP1750, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
蒸汽吸收式热泵 3c: 型号为 LTHP1260 , 购自北京环能瑞通科技发展 有限公司。 Steam absorption heat pump 3c: Model LTHP1260, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
汽-水换热器 4: 购自北京环能瑞通科技发展有限公司。 Steam-water heat exchanger 4: Purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
• 包括热水型吸收式热泵 5和水-水换热器 6的大温差换热机组: 型号 为 AHE8000A, 购自北京环能瑞通科技发展有限公司。 • Large temperature difference heat exchanger unit including hot water type absorption heat pump 5 and water-water heat exchanger 6: Model AHE8000A, purchased from Beijing Huaneng Ruitong Technology Development Co., Ltd.
连接示意图见图 5。 采用三级蒸汽吸收式热泵 3串联加热方式。 The connection diagram is shown in Figure 5. Three-stage steam absorption heat pump 3 is used for series heating.
给一次热网供热的装置: 管道 7依次通过汽轮机 1和凝汽器 2 ; 管道 8由主干管及其两支分支管道组成, 主干管通过汽轮机 1后分成两支分支 管道, 分支管道 8-1进一步分支, 形成三支二级分支管道, 分别通过蒸汽 吸收式热泵 3a、 蒸汽吸收式热泵 3b、 蒸汽吸收式热泵 3c后汇合, 分支管 道 8-2通过汽-水换热器 4; 管道 9由主干管及其三支分支管道组成, 主干 管 9通过凝汽器 2后分成三支分支管道, 分支管道 9-1分为三支分别通过 蒸汽吸收式热泵 3a、 蒸汽吸收式热泵 3b、 蒸汽吸收式热泵 3c后汇合与一 次热网回水管道 13相通, 分支管道 9-2在通过蒸汽吸收式热泵 3前可分 支为两支二级分支管道,二级分支管道 9-2-1依次通过蒸汽吸收式热泵 3a、
蒸汽吸收式热泵 3b、 蒸汽吸收式热泵 3c和汽-水换热器 4, 二级分支管道 9-2-2与一次热网回水管道 13相通, 分支管道 9-3通过循环水冷却装置 14与一次热网回水管道 13相通。 The device for supplying heat to the heat network: the pipe 7 passes through the steam turbine 1 and the condenser 2 in sequence; the pipe 8 is composed of the main pipe and its two branch pipes, and the main pipe passes through the steam turbine 1 and is divided into two branch pipes, and the branch pipe 8- 1 further branching, forming three secondary branch pipes, respectively passing through the steam absorption heat pump 3a, the steam absorption heat pump 3b, the steam absorption heat pump 3c, and the branch pipe 8-2 passing through the steam-water heat exchanger 4; The main pipe 9 is divided into three branch pipes through the condenser 2, and the branch pipe 9-1 is divided into three branches respectively through the steam absorption heat pump 3a, the steam absorption heat pump 3b, and the steam. After the absorption heat pump 3c is merged, it is connected to the primary heat network return pipe 13, and the branch pipe 9-2 can be branched into two secondary branch pipes before passing through the steam absorption heat pump 3, and the secondary branch pipes 9-2-1 pass sequentially. Steam absorption heat pump 3a, The steam absorption heat pump 3b, the steam absorption heat pump 3c and the steam-water heat exchanger 4, the secondary branch pipe 9-2-2 communicate with the primary heat network return pipe 13, and the branch pipe 9-3 passes the circulating water cooling device 14. It communicates with the primary heat network return pipe 13.
换热装置: 管道 10依次通过热水型吸收式热泵 5的发生器、 水 -水换 热器 6和热水型吸收式热泵 5的蒸发器; 管道 11依次通过热水型吸收式 热泵 5的吸收器、 热水型吸收式热泵 5的冷凝器和水 -水换热器 6, 然后两 支分支管道汇合。 Heat exchange device: The pipe 10 passes through the generator of the hot water type absorption heat pump 5, the water-water heat exchanger 6 and the evaporator of the hot water type absorption heat pump 5 in sequence; the pipe 11 passes through the hot water type absorption heat pump 5 in sequence. The absorber, the condenser of the hot water type absorption heat pump 5, and the water-water heat exchanger 6, and then the two branch pipes merge.
供热系统: 管道 9通过凝汽器 2前与一次热网回水管道 13相通, 二 级分支管道 9-2-1通过汽-水换热器 4后与一次热网供水管道 12相通, 多 个换热装置并联, 换热装置各自的进水管道与一次热网供水管道 12连接, 出水管道与一次热网回水管道 13连接。 Heating system: The pipeline 9 communicates with the primary heat network return pipe 13 before passing through the condenser 2, and the secondary branch pipe 9-2-1 passes through the steam-water heat exchanger 4 and communicates with the primary heat network water supply pipe 12, The heat exchange devices are connected in parallel, and the respective water inlet pipes of the heat exchange device are connected to the primary heat network water supply pipe 12, and the water outlet pipe is connected to the primary heat network return water pipe 13.
二、 应用 Second, the application
汽轮机 1末级排汽进入凝汽器中加热循环水, 被冷却凝结后再返回锅 炉加热。 由汽轮机 1抽出的蒸汽分为两路, 一路分别进入一级蒸汽吸收式 热泵机 3a、 二级蒸汽吸收式热泵 3b、 三级蒸汽吸收式热泵 3c, 作为驱动 热源回收循环水余热并逐级加热一次热网, 另一路进入汽 -水换热器 4, 直 接加热一次热网, 蒸汽凝水返回锅炉加热。 循环冷却水进入凝汽器 2中, 被汽轮机 1排汽加热后送出, 分别进入一级蒸汽吸收式热泵 3a、 二级蒸汽 吸收式热泵 3b和三级蒸汽吸收式热泵 3c, 作为低位热源, 放热降温后再 返回凝汽器, 完成循环, 多余热量通过循环水冷却装置 14 排放到环境。 一次热网低温回水返回电厂, 首先进入凝汽器 2, 被预热升温后送出, 依 次通过一级蒸汽吸收式热泵 3a、 二级蒸汽吸收式热泵 3b和三级蒸汽吸收 式热泵 3c, 被逐级加热后送出, 再进入汽-水换热器 4中被三次加热, 加 热到一次热网供水温度后送出电厂, 一次热网高温供水被输送到末端热力 站, 首先作为驱动热源进入热水吸收式热泵 5, 放热降温后进入水-水换热 器 6加热二次侧供热热水, 降温后再次进入热水吸收式热泵 5作为低位热 源, 最终放热降温到一次热网回水温度后返回电厂, 完成循环。 The steam exhaust of the first stage of the steam turbine enters the condenser to heat the circulating water, which is cooled and condensed before returning to the boiler for heating. The steam extracted by the steam turbine 1 is divided into two paths, one into a first-stage steam absorption heat pump 3a, a second-stage steam absorption heat pump 3b, and a third-stage steam absorption heat pump 3c, which are used as a driving heat source to recover the residual heat of the circulating water and are heated step by step. One heat network, the other enters the steam-water heat exchanger 4, directly heats the heat network once, and the steam condensate returns to the boiler for heating. The circulating cooling water enters the condenser 2, is heated by the steam exhaust of the steam turbine 1, and is sent out to enter the first-stage steam absorption heat pump 3a, the second-stage steam absorption heat pump 3b, and the third-stage steam absorption heat pump 3c as low-level heat sources. After the heat is cooled, it is returned to the condenser to complete the cycle, and excess heat is discharged to the environment through the circulating water cooling device 14. The primary heating network returns to the power plant at a low temperature, first enters the condenser 2, is warmed up and sent out, and passes through the first-stage steam absorption heat pump 3a, the secondary steam absorption heat pump 3b and the third-stage steam absorption heat pump 3c. After heating step by step, it is sent out, and then enters the steam-water heat exchanger 4 and is heated three times. After being heated to the temperature of the hot water supply, it is sent to the power plant. The high-temperature water supply of the hot network is sent to the end heat station, and firstly enters the hot water as the driving heat source. The absorption heat pump 5, after the heat release and cooling, enters the water-water heat exchanger 6 to heat the secondary side heating hot water, and then enters the hot water absorption heat pump 5 as a low-level heat source after cooling, and finally releases the heat to a heat network backwater. Return to the power plant after the temperature and complete the cycle.
工业应用 Industrial application
本发明的特征主要体现在三个方面: 1 ) 利用汽轮机排汽预热一次热 网回水, 并利用循环冷却水作为吸收式热泵的低位热源, 优点是有效回收
了电厂发电过程中产生的余热; 2 ) 采用凝汽器、 蒸汽吸收式热泵和汽-水 换热器对热网热水进行三次加热, 优点是可以提高热网供水温度, 增大了 一次热网的回、 供水温差; 3 ) 在末端采用热水吸收式热泵和水-水换热器 组合的方式加热二次网供热热水, 优点是可以充分降低一次热网的回水温 度, 增大了一次热网的供、 回水温差。
The features of the invention are mainly embodied in three aspects: 1) preheating the primary heat network backwater by using the steam exhaust of the steam turbine, and using the circulating cooling water as the low heat source of the absorption heat pump, the advantage is effective recovery The waste heat generated during the power generation process of the power plant; 2) The condenser network, the steam absorption heat pump and the steam-water heat exchanger are used to heat the hot water of the hot network three times, which has the advantages of increasing the temperature of the hot water supply and increasing the heat once. The return of the net and the temperature difference of the water supply; 3) heating the secondary network for hot water supply by means of a combination of a hot water absorption heat pump and a water-water heat exchanger at the end, which has the advantage of sufficiently reducing the return water temperature of the primary heat network, increasing The temperature difference between the supply and return water of the hot network was increased.
Claims
1、 给一次网供热的装置, 包括: 含有凝汽器 (2) 的汽轮机 (1) 、 至少一台蒸汽吸收式热泵 (3) 、 汽-水换热器 (4) 、 管道 (7) 、 管道(8) 和管道 (9); 1. A device for supplying heat to a net, comprising: a steam turbine (1) containing a condenser (2), at least one steam absorption heat pump (3), a steam-water heat exchanger (4), a pipe (7) , pipe (8) and pipe (9);
管道(7)依次通过汽轮机(1)和凝汽器(2); The pipe (7) passes through the steam turbine (1) and the condenser (2) in sequence;
管道 (8)由主干管及其两支分支管道组成, 主干管(8)通过汽轮机(1) 后分成两支分支管道, 分支管道 (8-1) 通过蒸汽吸收式热泵 (3) , 分支 管道 (8-2) 通过汽-水换热器 (4); The pipe (8) is composed of a main pipe and two branch pipes, and the main pipe (8) is divided into two branch pipes through a steam turbine (1), and the branch pipe (8-1) passes through a steam absorption heat pump (3), a branch pipe (8-2) through a steam-water heat exchanger (4);
管道(9)由主干管及其两支分支管道组成,主干管(9)通过凝汽器(2) 后分成两支分支管道, 分支管道 (9-1) 通过蒸汽吸收式热泵 (3) 后与一 次网回水管道(13)相通, 分支管道(9-2)依次通过蒸汽吸收式热泵(3) 和汽-水换热器 (4) 。 The pipe (9) consists of a main pipe and two branch pipes. The main pipe (9) is divided into two branch pipes by a condenser (2), and the branch pipe (9-1) passes through a steam absorption heat pump (3). It is connected to the primary network return pipe (13), which in turn passes through the steam absorption heat pump (3) and the steam-water heat exchanger (4).
2、 如权利要求 1所述的装置, 其特征在于: 所述蒸汽吸收式热泵(3) 为两台以上, 所述分支管道 (8-1) 进一步分支, 形成两个以上二级分支 管道, 每个所述二级分支管道分别通过一个蒸汽吸收式热泵 (3) 后再汇 合。 2. The apparatus according to claim 1, wherein: the steam absorption heat pump (3) is two or more, and the branch pipe (8-1) further branches to form two or more secondary branch pipes. Each of the secondary branch pipes is passed through a vapor absorption heat pump (3) and then merged.
3、 如权利要求 1所述的装置, 其特征在于: 所述分支管道 (9-2) 在 通过蒸汽吸收式热泵 (3) 前分支为两支二级分支管道, 二级分支管道 (9-2-1) 依次通过蒸汽吸收式热泵 (3) 和汽-水换热器 (4) , 二级分支 管道 (9-2-2) 与一次热网回水管道 (13) 相通。 3. The device according to claim 1, characterized in that: the branch pipe (9-2) branches into two secondary branch pipes and a secondary branch pipe (9- before passing through the steam absorption heat pump (3). 2-1) Pass the steam absorption heat pump (3) and the steam-water heat exchanger (4) in turn, and the secondary branch pipe (9-2-2) communicates with the primary heat network return pipe (13).
4、 含有权利要求 1至 3中任一所述给一次网供热装置的供热系统。 4. A heating system comprising a primary heating device as claimed in any one of claims 1 to 3.
5、 如权利要求 4所述的供热系统, 其特征在于: 所述系统还包括一 个以上换热装置; 所述给一次网供热装置与所述换热装置之间通过一次热 网供水管道 (12) 和一次热网回水管道 (13) 连通; 5. The heating system according to claim 4, wherein: the system further comprises one or more heat exchange devices; and the primary network heating device and the heat exchange device pass through a heat network water supply pipe (12) connected to the primary heat network return pipe (13);
所述换热装置, 包括热水型吸收式热泵 (5) 、 至少一台水-水换热器 (6) 、 管道 (10) 和管道 (11) ; 所述热水型吸收式热泵 (5) 包括: 发 生器、 蒸发器、 冷凝器、 吸收器; 所述管道 (10) 依次通过热水型吸收式 热泵 (5) 的发生器、 水-水换热器 (6) 和热水型吸收式热泵 (5) 的蒸发 器形成一次网系统; 所述管道 (11) 通过热水型吸收式热泵 (5) 的吸收
器、 热水型吸收式热泵 (5) 的冷凝器和水-水换热器 (6) 形成二次网系 统。 The heat exchange device comprises a hot water type absorption heat pump (5), at least one water-water heat exchanger (6), a pipe (10) and a pipe (11); the hot water type absorption heat pump (5) ) includes: a generator, an evaporator, a condenser, an absorber; the pipe (10) sequentially passes through a generator of a hot water type absorption heat pump (5), a water-water heat exchanger (6), and a hot water type absorption The evaporator of the heat pump (5) forms a primary network system; the pipe (11) is absorbed by the hot water type absorption heat pump (5) The condenser of the hot water type absorption heat pump (5) and the water-water heat exchanger (6) form a secondary network system.
6、 如权利要求 5 所述的供热系统, 其特征在于: 所述供热系统包括 一个所述换热装置, 管道(9)通过凝汽器(2)前与一次热网回水管道(13) 相通, 分支管道(9-2)或二级分支管道(9-2-1)通过蒸汽吸收式热泵(3) 和汽-水换热器 (4) 后与一次热网供水管 (12) 相通, 管道 (10) 通过热 水型吸收式热泵 (5) 的发生器前与一次热网供水管 (12) 相通。 6. The heating system according to claim 5, wherein: said heating system comprises a heat exchange device, and said pipe (9) passes through a condenser (2) and a heat network return pipe ( 13) The same, branch pipe (9-2) or secondary branch pipe (9-2-1) passes through the steam absorption heat pump (3) and the steam-water heat exchanger (4) and the primary heat network water supply pipe (12 In the same way, the pipe (10) is connected to the primary heat network water supply pipe (12) through the generator of the hot water type absorption heat pump (5).
7、 如权利要求 5 所述的供热系统, 其特征在于: 所述供热系统包括 两个以上并联的所述换热装置, 管道 (9)通过凝汽器 (2) 前与一次热网回 水管道 (13) 相通, 分支管道 (9-2) 或二级分支管道 (9-2-1) 通过蒸汽 吸收式热泵 (3) 和汽-水换热器 (4) 后与一次热网供水管道 (12) 相通; 各个换热装置的管道 (10) 通过热水型吸收式热泵 (5) 的发生器前与一 次热网供水管道 (12) 相通。 7. The heating system according to claim 5, wherein: said heating system comprises two or more said heat exchange devices in parallel, and the pipe (9) passes through the condenser (2) before and once. The return water pipe (13) is connected, the branch pipe (9-2) or the secondary branch pipe (9-2-1) passes through the steam absorption heat pump (3) and the steam-water heat exchanger (4) and the primary heat network The water supply pipe (12) communicates; the pipe (10) of each heat exchange device communicates with the primary heat network water supply pipe (12) through the generator of the hot water type absorption heat pump (5).
8、 如权利要求 5至 7中任一所述的供热系统, 其特征在于: 所述管 道 (11) 依次通过热水型吸收式热泵 (5) 的吸收器、 热水型吸收式热泵 The heating system according to any one of claims 5 to 7, characterized in that: the pipe (11) passes through the absorber of the hot water type absorption heat pump (5) in turn, and the hot water type absorption heat pump
(5) 的冷凝器和水-水换热器 (6) 。 (5) Condenser and water-water heat exchanger (6).
9、 如权利要求 5至 7中任一所述的供热系统, 其特征在于: 所述管 道 (11) 由至少两支独立的管道组成, 一支独立管道依次通过热水型吸收 式热泵 (5) 的吸收器和热水型吸收式热泵 (5) 的冷凝器, 其它管道中, 每支管道分别通过一台水-水换热器 (6) 。 9. The heating system according to any one of claims 5 to 7, characterized in that: the pipe (11) consists of at least two independent pipes, and an independent pipe passes through a hot water type absorption heat pump in turn ( 5) The absorber and the condenser of the hot water absorption heat pump (5). In other pipes, each pipe passes through a water-water heat exchanger (6).
10、 如权利要求 5至 7中任一所述的供热系统, 其特征在于: 所述换 热装置包括一台水-水换热器 (6) , 所述管道 (11) 由主干管及其两支分 支管道组成, 主干管 (11) 先分成两支分支管道, 分支管道 (11-1) 依次 通过热水型吸收式热泵(5) 的吸收器和热水型吸收式热泵(5)的冷凝器, 分支管道 (11-2) 通过水-水换热器 (6) , 然后两支分支管道汇合。 10. The heating system according to any one of claims 5 to 7, wherein: said heat exchange device comprises a water-water heat exchanger (6), said pipe (11) being composed of a main pipe and It consists of two branch pipes. The main pipe (11) is first divided into two branch pipes. The branch pipe (11-1) passes through the absorber of the hot water type absorption heat pump (5) and the hot water type absorption heat pump (5). The condenser, branch pipe (11-2) passes through the water-water heat exchanger (6), and then the two branch pipes meet.
11、 如权利要求 5至 7中任一所述的供热系统, 其特征在于: 所述换 热装置包括两台水-水换热器 (2) , 所述管道 (11) 由主干管及其三支分 支管道组成, 主干管 (11) 先分成三支分支管道, 分支管道 (11-1) 依次 通过热水型吸收式热泵(1) 的吸收器和热水型吸收式热泵(1)的冷凝器, 分支管道 (11-2) 通过水-水换热器 (2a) , 分支管道 (11-3) 通过水-水
换热器 (2b) ,然后三支分支管道汇合。 11. The heating system according to any one of claims 5 to 7, wherein: said heat exchange device comprises two water-water heat exchangers (2), said pipes (11) being composed of main pipes and It consists of three branch pipes. The main pipe (11) is first divided into three branch pipes. The branch pipe (11-1) passes through the absorber of the hot water type absorption heat pump (1) and the hot water type absorption heat pump (1). Condenser, branch pipe (11-2) through water-water heat exchanger (2a), branch pipe (11-3) through water-water The heat exchanger (2b), then the three branch pipes meet.
12、 如权利要求 5至 7中任一所述的供热系统, 其特征在于: 所述换 热装置包括两台水-水换热器 (2) , 管道 (11) 由主干管及其两支分支管 道组成, 主干管 (11) 先分成两支分支管道, 分支管道 (11-1) 依次通过 热水型吸收式热泵 (1) 的吸收器和热水型吸收式热泵 (1) 的冷凝器, 分 支管道 (11-2) 通过水 -水换热器 (2a) , 然后两支分支管道汇合成后通 过水-水换热器 (2b) 。 12. The heating system according to any one of claims 5 to 7, wherein: said heat exchange device comprises two water-water heat exchangers (2), and the pipes (11) are composed of a main pipe and two The branch pipe is composed, and the main pipe (11) is first divided into two branch pipes, and the branch pipe (11-1) is sequentially passed through the absorption of the hot water type absorption heat pump (1) and the condensation of the hot water type absorption heat pump (1). The branch pipe (11-2) passes through the water-water heat exchanger (2a), and then the two branch pipes are combined and passed through the water-water heat exchanger (2b).
13、 如权利要求 5至 7中任一所述的供热系统, 其特征在于: 所述换 热装置包括两台水-水换热器 (2) , 管道 (11) 由主干管及其两支分支管 道组成, 主干管 (11) 先依次通过热水型吸收式热泵 (1) 的吸收器和热 水型吸收式热泵(1)的冷凝器, 然后分成两支分支管道, 分支管道(11-1) 通过水 -水换热器 (2a) , 分支管道 (11-2) 通过水-水换热器 (2b) , 然 后两支分支管道汇合。 The heating system according to any one of claims 5 to 7, wherein: said heat exchange device comprises two water-water heat exchangers (2), and the pipes (11) are composed of a main pipe and two The branch pipe is composed of a main pipe (11) which is first passed through the absorber of the hot water type absorption heat pump (1) and the condenser of the hot water type absorption heat pump (1), and then divided into two branch pipes, branch pipes (11) -1) Through the water-water heat exchanger (2a), the branch pipe (11-2) passes through the water-water heat exchanger (2b), and then the two branch pipes merge.
14、权利要求 1至 3中任一所述一次网供热装置在集中供热中的应用。 14. The use of a primary mesh heating device according to any one of claims 1 to 3 for central heating.
15、 权利要求 4至 13中任一所述供热系统在集中供热中的应用。
15. Use of a heating system according to any of claims 4 to 13 for central heating.
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