CN204373030U - Make full use of the step heating heating system of residual heat of electric power plant - Google Patents

Make full use of the step heating heating system of residual heat of electric power plant Download PDF

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CN204373030U
CN204373030U CN201420810607.1U CN201420810607U CN204373030U CN 204373030 U CN204373030 U CN 204373030U CN 201420810607 U CN201420810607 U CN 201420810607U CN 204373030 U CN204373030 U CN 204373030U
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steam
heat
heating
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王强
刘冲
吕建国
王远清
赵瑞平
严鑫
郝相俊
丰玲
王义军
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China Energy Engineering Group Shanxi Electric Power Engineering Co Ltd
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China Energy Engineering Group Shanxi Electric Power Engineering Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/52Heat 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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Abstract

本实用新型公开了一种充分利用电厂余热的梯级加热供热系统,解决了现有技术存在的电厂余热利用率不高和供热温度调节不灵活的问题。本实用新型是将空冷机组的高背压凝汽器结合热泵回收汽轮机乏汽供热一种供热系统,改变了现有的热泵回收乏汽供热、高背压凝汽器回收乏汽供热和单纯的抽汽供热方式,本实用新型的有益效果是将供热热网水的加热系统增加至三级加热,减小了热网水在加热过程中的温度梯度差,从而减少了火用损。本实用新型系统可以分期建设,初投资相对较少,供热调节灵活。适用于火力发电厂直接空冷机组,特别适合于30万及30万以下直接空冷机组。

The utility model discloses a cascaded heating system for fully utilizing the waste heat of a power plant, which solves the problems in the prior art that the utilization rate of the waste heat of the power plant is not high and the adjustment of the heating temperature is inflexible. The utility model is a heat supply system that combines the high back pressure condenser of the air-cooling unit with the heat pump to recover the exhaust steam of the steam turbine for heat supply, which changes the existing heat pump recovery exhaust steam heat supply and the high back pressure condenser recovery exhaust steam supply. The utility model has the beneficial effect of increasing the heating system of the heating network water to three-stage heating, reducing the temperature gradient difference of the heating network water during the heating process, thereby reducing Fire damage. The system of the utility model can be constructed in stages, the initial investment is relatively small, and the heat supply can be adjusted flexibly. It is suitable for direct air-cooling units in thermal power plants, especially suitable for direct air-cooling units of 300,000 or less.

Description

充分利用电厂余热的梯级加热供热系统Cascade heating heating system that makes full use of waste heat in power plants

技术领域 technical field

本发明涉及一种火力发电厂直接空冷机组高背压结合热泵的供热系统,是将空冷机组的高背压凝汽器与热泵结合用以回收汽轮机乏汽的一种供热系统。 The invention relates to a thermal power plant direct air-cooling unit high back pressure combined with heat pump heat supply system, which is a heat supply system that combines the high back pressure condenser of the air-cooling unit with the heat pump to recover exhaust steam from the steam turbine.

背景技术 Background technique

热电联产供热机组传统的供热方式是采用抽汽供热。在节能减排政策的指引下,近几年来,采用热泵及凝汽器等余热利用设备来提取汽轮机尾部乏汽来供热的工程也越来越多。当下常用的供热方式有四种:第一种是抽汽供热,是利用汽轮机采暖抽汽,通过汽-水换热器即热网加热器加热热网循环水供热。特点是投资少,但无法利用汽轮机乏汽。第二种是热泵供热,是通过设置吸收式或压缩式热泵来提取汽轮机乏汽供热,不足的热量再通过热网加热器补充。特点是可利用一部分乏汽,但乏汽利用率不高,占比约为30%-40%。第三种是前置凝汽器加热泵供热,由于空冷机组运行背压在12-15KPa,在热泵前设置凝汽器可利用初末寒期回水温度低的特点大量吸收汽轮机乏汽,经前置凝汽器加热后的热网水进入热泵继续被加热,当热量不足时,再利用热网加热器加热热网水。特点是可大量利用初、末寒期的乏汽,余热利用率约为45%-55%。第四种是机组高背压供热,是将一台空冷机组的背压提高到25KPa以上,通过设置大容量的凝汽器来加热热网水,不足部分由热网加热器来加热。该种型式的余热利用率约在55%-65%,投资也较少,缺点是调节不灵活,供热面积需要足够大,设计供水温度不能太高,否则余热占比会降低。 The traditional heating method of cogeneration heating units is to use steam extraction for heating. Under the guidance of energy conservation and emission reduction policies, in recent years, more and more projects have used waste heat utilization equipment such as heat pumps and condensers to extract exhaust steam at the tail of steam turbines for heating. There are four commonly used heating methods at present: the first is steam extraction for heating, which uses steam turbines for heating and extracting steam, and heats the circulating water of the heating network through a steam-water heat exchanger, that is, a heating network heater. The characteristic is that the investment is small, but the exhaust steam of the steam turbine cannot be used. The second is heat pump heating, which is to extract the exhaust steam of the steam turbine for heating by setting up an absorption or compression heat pump, and the insufficient heat is supplemented by a heat network heater. The characteristic is that a part of exhaust steam can be utilized, but the utilization rate of exhaust steam is not high, accounting for about 30%-40%. The third is the pre-condenser heat pump for heat supply. Since the air-cooled unit operates at a back pressure of 12-15KPa, installing a condenser in front of the heat pump can take advantage of the low temperature of the return water in the early and late cold periods to absorb a large amount of exhaust steam from the turbine. The heating network water heated by the pre-condenser enters the heat pump to continue heating. When the heat is insufficient, the heating network heater is used to heat the heating network water. The feature is that it can use a large amount of exhaust steam in the early and late cold periods, and the utilization rate of waste heat is about 45%-55%. The fourth is the high back pressure heating of the unit, which is to increase the back pressure of an air-cooled unit to more than 25KPa, and heat the hot network water by setting a large-capacity condenser, and heat the insufficient part by the hot network heater. The waste heat utilization rate of this type is about 55%-65%, and the investment is less. The disadvantage is that the adjustment is not flexible, the heating area needs to be large enough, and the design water supply temperature should not be too high, otherwise the proportion of waste heat will be reduced.

发明内容 Contents of the invention

本发明提供了一种充分利用电厂余热的梯级加热供热系统,解决了现有技术存在的电厂余热利用率不高和供热温度调节不灵活的技术问题。 The invention provides a cascaded heating and heat supply system that fully utilizes the waste heat of the power plant, and solves the technical problems of low utilization rate of waste heat of the power plant and inflexible adjustment of the heating temperature existing in the prior art.

本发明是通过以下技术方案解决以上技术问题的: The present invention solves the above technical problems through the following technical solutions:

一种充分利用电厂余热的梯级加热供热系统,包括第一机组汽轮机、第一机组排汽装置、第二机组汽轮机和第二机组排汽装置,第一机组排汽装置通过第一机组直接空冷排汽管路与第一机组空冷散热器连通,第一机组空冷散热器通过第一机组直接空冷乏汽凝结水管路与第一机组排汽装置上的热井连通,第二机组排汽装置通过第二机组直接空冷排汽管路与第二机组空冷散热器连通,第二机组空冷散热器通过第二机组直接空冷乏汽凝结水管路与第二机组排汽装置上的热井连通;热网凝汽器的乏汽口通过第一机组乏汽管道与第一机组直接空冷排汽管路连通,热网凝汽器的乏汽凝结水口通过第一机组热网凝汽器乏汽凝结水管道与第一机组直接空冷乏汽凝结水管路连通,城市热网回水管路通过热网凝汽器进水管道与热网凝汽器的进水口连通,热网凝汽器出水管道的一端与热网凝汽器的出水口连通,热网凝汽器出水管道的另一端与热泵的热网水进水口连通,热泵的乏汽凝结水口通过第二机组热泵乏汽凝结水管道与第二机组直接空冷乏汽凝结水管路连通,热泵的乏汽口通过第二机组乏汽管道与第二机组直接空冷排汽管路连通,热泵的驱动蒸汽口通过第二机组蒸汽管道与第二机组汽轮机的抽汽口连通,热泵的热网水口通过热泵出水管道与热网加热器上的热网水进水口连通,在热泵出水管道上设置有热网循环泵,热网加热器上的热网出水口通过热网加热器出水管道与城市热网供水管道连通,热网加热器上的加热蒸汽口通过第二机组蒸汽管道与第二机组汽轮机的抽汽口连通,热网加热器上的加热蒸汽口通过第一机组蒸汽管道与第一机组汽轮机的抽汽口连通,热网加热器上的加热蒸汽疏水口通过第一机组蒸汽疏水管道与第一机组汽轮机的低压凝结水管道连通,热网加热器上的加热蒸汽疏水口通过第二机组蒸汽疏水管道与第二机组汽轮机的低压凝结水管道连通。 A cascaded heating system that makes full use of the waste heat of a power plant, including the steam turbine of the first unit, the steam exhaust device of the first unit, the steam turbine of the second unit and the exhaust device of the second unit, and the exhaust device of the first unit is directly air-cooled by the first unit The exhaust pipe is connected with the air-cooled radiator of the first unit, and the air-cooled radiator of the first unit is connected with the hot well on the exhaust device of the first unit through the direct air-cooled condensate pipeline of the first unit, and the exhaust device of the second unit is passed through The direct air-cooled exhaust pipeline of the second unit is connected with the air-cooled radiator of the second unit, and the air-cooled radiator of the second unit is connected with the hot well on the exhaust device of the second unit through the direct air-cooled exhaust steam condensate pipeline of the second unit; The exhaust steam port of the condenser is connected with the direct air-cooling exhaust pipeline of the first unit through the exhaust steam pipe of the first unit, and the exhaust steam condensate port of the heat network condenser is connected with the exhaust steam condensate pipe of the heat network condenser of the first unit It is directly connected with the air-cooled exhaust steam condensate pipeline of the first unit, the return water pipeline of the urban heating network is connected with the water inlet of the heating network condenser through the water inlet pipe of the heating network condenser, and one end of the outlet pipe of the heating network condenser is connected with the heat The water outlet of the network condenser is connected, and the other end of the water outlet pipe of the heat network condenser is connected with the heat network water inlet of the heat pump. The air-cooled exhaust steam condensate pipeline is connected, the exhaust steam port of the heat pump is connected with the direct air-cooling exhaust pipeline of the second unit through the exhaust steam pipeline of the second unit, and the driving steam port of the heat pump is connected with the exhaust pipe of the second unit steam turbine The steam port is connected, and the heat network outlet of the heat pump is connected with the heat network water inlet on the heat network heater through the heat pump outlet pipe. The water outlet pipe of the heat network heater is connected with the urban heat network water supply pipe, the heating steam port on the heat network heater is connected with the steam extraction port of the second unit steam turbine through the steam pipe of the second unit, and the heating steam port on the heat network heater is passed through The steam pipe of the first unit is connected with the steam extraction port of the steam turbine of the first unit, and the heating steam drain on the heat network heater is connected with the low-pressure condensate pipe of the steam turbine of the first unit through the steam drain pipe of the first unit, and the steam drain on the heat network heater The heating steam drain port of the second unit communicates with the low-pressure condensate water pipeline of the steam turbine of the second unit through the steam drain pipe of the second unit.

本发明的有益效果是将供热热网水的加热系统增加至三级加热,减小了热网水在加热过程中的温度梯度差,从而减少了火用损。本发明系统可以分期建设,初投资相对较少,供热调节灵活。本系统适用于火力发电厂直接空冷机组,特别适合于30万及30万以下直接空冷机组。 The invention has the beneficial effects of increasing the heating system of the heating network water to three stages of heating, reducing the temperature gradient difference of the heating network water during the heating process, thereby reducing the exergy loss. The system of the invention can be constructed in stages, the initial investment is relatively small, and the heat supply can be adjusted flexibly. This system is suitable for direct air-cooling units in thermal power plants, especially for direct air-cooling units of 300,000 or less.

附图说明 Description of drawings

图1是本发明的结构示意图。 Fig. 1 is a schematic structural view of the present invention.

具体实施方式 Detailed ways

下面结合附图对本发明进行详细说明: The present invention is described in detail below in conjunction with accompanying drawing:

一种充分利用电厂余热的梯级加热供热系统,包括第一机组汽轮机1、第一机组排汽装置2、第二机组汽轮机6和第二机组排汽装置7,第一机组排汽装置2通过第一机组直接空冷排汽管路4与第一机组空冷散热器3连通,第一机组空冷散热器3通过第一机组直接空冷乏汽凝结水管路5与第一机组排汽装置2上的热井连通,第二机组排汽装置7通过第二机组直接空冷排汽管路9与第二机组空冷散热器8连通,第二机组空冷散热器8通过第二机组直接空冷乏汽凝结水管路10与第二机组排汽装置7上的热井连通,热网凝汽器11的乏汽口通过第一机组乏汽管道12与第一机组直接空冷排汽管路4连通,热网凝汽器11的乏汽凝结水口通过第一机组热网凝汽器乏汽凝结水管道13与第一机组直接空冷乏汽凝结水管路5连通,城市热网回水管路14通过热网凝汽器进水管道16与热网凝汽器11的进水口连通,热网凝汽器出水管道15的一端与热网凝汽器11的出水口连通,热网凝汽器出水管道15的另一端与热泵17的热网水进水口连通,热泵17的乏汽凝结水口通过第二机组热泵乏汽凝结水管道18与第二机组直接空冷乏汽凝结水管路10连通,热泵17的乏汽口通过第二机组乏汽管道19与第二机组直接空冷排汽管路9连通,热泵17的驱动蒸汽口通过第二机组蒸汽管道20与第二机组汽轮机6的抽汽口连通,热泵17的热网水口通过热泵出水管道21与热网加热器23上的热网水进水口连通,在热泵出水管道21上设置有热网循环泵28,热网加热器23上的热网出水口通过热网加热器出水管道24与城市热网供水管道25连通,热网加热器23上的加热蒸汽口通过第二机组蒸汽管道20与第二机组汽轮机6的抽汽口连通,热网加热器23上的加热蒸汽口通过第一机组蒸汽管道26与第一机组汽轮机1的抽汽口连通,热网加热器23上的加热蒸汽疏水口通过第一机组蒸汽疏水管道28与第一机组汽轮机的低压凝结水管道连通,热网加热器23上的加热蒸汽疏水口通过第二机组蒸汽疏水管道27与第二机组汽轮机的低压凝结水管道连通。 A cascaded heating heating system that makes full use of the waste heat of a power plant, including a first unit steam turbine 1, a first unit exhaust device 2, a second unit steam turbine 6, and a second unit exhaust device 7, and the first unit exhaust device 2 passes through The direct air-cooled exhaust pipeline 4 of the first unit communicates with the air-cooled radiator 3 of the first unit, and the air-cooled radiator 3 of the first unit communicates with the heat on the exhaust device 2 of the first unit through the direct air-cooled exhaust steam condensate pipeline 5 of the first unit. The well is connected, the exhaust device 7 of the second unit communicates with the air-cooled radiator 8 of the second unit through the direct air-cooled exhaust pipeline 9 of the second unit, and the air-cooled radiator 8 of the second unit passes through the direct air-cooled exhaust steam condensate pipeline 10 of the second unit It communicates with the hot well on the exhaust device 7 of the second unit, and the exhaust steam port of the heat network condenser 11 communicates with the direct air-cooling exhaust pipeline 4 of the first unit through the exhaust steam pipeline 12 of the first unit, and the heat network condenser The exhaust steam condensate outlet of 11 is connected with the exhaust steam condensate pipeline 5 of the first unit direct air-cooled exhaust steam condensate pipeline 5 through the exhaust steam condensate pipeline 13 of the heat network condenser of the first unit, and the urban heating network return water pipeline 14 enters water through the heat network condenser Pipeline 16 is communicated with the water inlet of heat network condenser 11, and one end of heat network condenser water outlet pipe 15 is communicated with the water outlet of heat network condenser 11, and the other end of heat network condenser water outlet pipe 15 is connected with heat pump 17 The water inlet of the heating network is connected, the exhaust steam condensate outlet of the heat pump 17 is connected with the direct air-cooled exhaust steam condensate pipeline 10 of the second unit through the second unit heat pump exhaust steam condensate pipeline 18, and the exhaust steam outlet of the heat pump 17 is connected through the second unit The exhaust steam pipeline 19 communicates with the direct air-cooling exhaust pipeline 9 of the second unit, the drive steam port of the heat pump 17 communicates with the steam extraction port of the steam turbine 6 of the second unit through the steam pipeline 20 of the second unit, and the heat network outlet of the heat pump 17 passes through the heat pump The water outlet pipeline 21 communicates with the hot network water inlet on the heat network heater 23, and the heat network circulation pump 28 is arranged on the heat pump outlet pipeline 21, and the heat network water outlet on the heat network heater 23 passes through the heat network heater outlet pipe 24 communicates with the urban heating network water supply pipeline 25, the heating steam port on the heating network heater 23 communicates with the steam extraction port of the second unit steam turbine 6 through the steam pipeline 20 of the second unit, and the heating steam port on the heating network heater 23 passes through The steam pipe 26 of the first unit is communicated with the steam extraction port of the steam turbine 1 of the first unit, and the steam drain outlet of the heating network heater 23 is communicated with the low-pressure condensate pipe of the steam turbine of the first unit through the steam drain pipe 28 of the first unit. The heating steam drain port on the network heater 23 communicates with the low-pressure condensed water pipeline of the steam turbine of the second unit through the steam drain pipe 27 of the second unit.

本发明的供热系统按热网水三级梯度加热设计,常规供热管网中的城市热网回水管路14中水的运行参数热网回水温度T14=50℃;在直接空冷机组主机不改造的前提下,热网凝汽器出水管道(15)中水温度T15=70℃;从热泵设备本身性能考虑,热泵特性系统cop=1.8,热泵出水管道21中水温度T21=85℃;按供热管网供水温度的实际要求,城市热网供水管道25中水温度T25=110℃-90℃; The heating system of the present invention is designed according to the three-level gradient heating of the heating network water, and the operating parameter of the water in the urban heating network return water pipeline 14 in the conventional heating network is T 14 =50°C; in the direct air cooling unit On the premise that the main engine is not modified, the temperature of water in the outlet pipe (15) of the heat network condenser is T 15 =70°C; considering the performance of the heat pump itself, the heat pump characteristic system cop=1.8, and the temperature of water in the outlet pipe 21 of the heat pump is T 21 = 85°C; according to the actual requirements of the water supply temperature of the heating pipe network, the water temperature T 25 in the water supply pipe 25 of the urban heating network =110°C-90°C;

综合计算得出,本供热系统余热利用负荷系数xyr在44%-66%之间,即整个采暖季乏汽余热占比高达65%-85%; According to the comprehensive calculation, the waste heat utilization load factor x yr of this heating system is between 44% and 66%, that is to say, the proportion of exhaust steam and waste heat in the whole heating season is as high as 65% to 85%;

供热系统余热利用负荷系数计算公式: Calculation formula for waste heat utilization load factor of heating system:

xyr =                                                x yr = ;

式中:T14—热网回水(即热网凝汽器进水)温度(℃); In the formula: T 14 - temperature of return water of heating network (that is, water entering the condenser of heating network) (°C);

T15—热网凝汽器出水温度(℃); T 15 —Temperature of the outlet water of the heat network condenser (°C);

T21——热泵出水温度(℃); T 21 ——heat pump outlet water temperature (°C);

T25——热网供水(即热网加热器出水)温度(℃); T 25 ——heating network water supply (that is, heating network heater outlet water) temperature (°C);

cop——热泵特性系数,常数; cop——heat pump characteristic coefficient, constant;

G——热网水流量(t/h); G——Water flow of heating network (t/h);

Q——供热负荷(KW); Q - heating load (KW);

Qyr——余热负荷(KW); Q yr - waste heat load (KW);

c——水的比热系数[kj/(℃·kg)]; c——the specific heat coefficient of water [kj/(℃·kg)];

xyr——供热系统余热利用负荷系数; x yr - load coefficient of waste heat utilization of heating system;

公式中:为热网凝汽器回收余热负荷,为热泵回收余热负荷,为总供热负荷。(热网凝汽器回收余热负荷+热泵回收余热负荷)/总供热负荷×100=余热利用负荷系数; formula: Recovery of waste heat load for heat network condenser, Recovery of waste heat loads for heat pumps, is the total heating load. (Heating network condenser waste heat recovery load + heat pump recovery waste heat load) / total heating load × 100 = waste heat utilization load factor;

公式化简得:xyr =The formula is simplified: x yr = .

Claims (1)

1. one kind makes full use of the step heating heating system of residual heat of electric power plant, comprise the first power generator turbine (1), first unit steam exhaust device (2), second power generator turbine (6) and the second unit steam exhaust device (7), first unit steam exhaust device (2) is communicated with the first unit air cooling heat radiator (3) by the first unit Direct Air-Cooled exhaust line (4), first unit air cooling heat radiator (3) is communicated with the hot well on the first unit steam exhaust device (2) by the first unit Direct Air-Cooled exhaust steam condensate line (5), second unit steam exhaust device (7) is communicated with the second unit air cooling heat radiator (8) by the second unit Direct Air-Cooled exhaust line (9), second unit air cooling heat radiator (8) is communicated with the hot well on the second unit steam exhaust device (7) by the second unit Direct Air-Cooled exhaust steam condensate line (10), it is characterized in that, the exhaust port of heat supply network condenser (11) is communicated with the first unit Direct Air-Cooled exhaust line (4) by the first unit exhaust steam pipeline (12), the exhaust steam condensation mouth of a river of heat supply network condenser (11) is communicated with the first unit Direct Air-Cooled exhaust steam condensate line (5) by the first unit heat supply network condenser exhaust steam condensing water conduit (13), municipal heating systems water return pipeline (14) is communicated with by the water inlet of heat supply network condenser inlet channel (16) with heat supply network condenser (11), one end of heat supply network condenser outlet conduit (15) is communicated with the delivery port of heat supply network condenser (11), the other end of heat supply network condenser outlet conduit (15) is communicated with the hot net water water inlet of heat pump (17), the exhaust steam condensation mouth of a river of heat pump (17) is communicated with the second unit Direct Air-Cooled exhaust steam condensate line (10) by the second unit heat pump exhaust steam condensing water conduit (18), the exhaust port of heat pump (17) is communicated with the second unit Direct Air-Cooled exhaust line (9) by the second unit exhaust steam pipeline (19), the driving steam port of heat pump (17) is communicated with the extraction opening of the second power generator turbine (6) by the second unit jet chimney (20), the heat supply network mouth of a river of heat pump (17) is communicated with the hot net water water inlet on heat exchangers for district heating (23) by heat pump outlet conduit (21), heat pump outlet conduit (21) is provided with pumps for hot water supply net (28), heat supply network delivery port on heat exchangers for district heating (23) is communicated with municipal heating systems water supply line (25) by heat exchangers for district heating outlet conduit (24), heating steam mouth on heat exchangers for district heating (23) is communicated with the extraction opening of the second power generator turbine (6) by the second unit jet chimney (20), heating steam mouth on heat exchangers for district heating (23) is communicated with the extraction opening of the first power generator turbine (1) by the first unit jet chimney (26), heating steam drain port on heat exchangers for district heating (23) is by the low pressure condensate water pipeline communication of the first unit steam drainage pipeline (28) with the first power generator turbine, heating steam drain port on heat exchangers for district heating (23) is by the low pressure condensate water pipeline communication of the second unit steam drainage pipeline (27) with the second power generator turbine.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104501275A (en) * 2014-12-21 2015-04-08 中国能源建设集团山西省电力勘测设计院 Stepped heating and supplying system sufficiently utilizing waste heat of power plant
CN105783080A (en) * 2016-04-19 2016-07-20 刘子旺 Hot-pressing unit heat supply system matched with high-back-pressure heat supply of large air-cooled generator set and regulating method
CN105805806A (en) * 2016-04-19 2016-07-27 刘子旺 Hot pressing unit heat supply system based on large air cooling unit and adjusting method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104501275A (en) * 2014-12-21 2015-04-08 中国能源建设集团山西省电力勘测设计院 Stepped heating and supplying system sufficiently utilizing waste heat of power plant
CN105783080A (en) * 2016-04-19 2016-07-20 刘子旺 Hot-pressing unit heat supply system matched with high-back-pressure heat supply of large air-cooled generator set and regulating method
CN105805806A (en) * 2016-04-19 2016-07-27 刘子旺 Hot pressing unit heat supply system based on large air cooling unit and adjusting method thereof
CN105783080B (en) * 2016-04-19 2016-11-23 普瑞森能源科技(北京)股份有限公司 Large-scale air cooling generator group high back pressure heat supply matched with hot press group heating system and control method
CN105805806B (en) * 2016-04-19 2016-11-23 山西爱晟特环保科技有限公司 A kind of hot pressing unit heating system based on large-scale air cooling unit and control method thereof

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