CN204404310U - Air cooling unit exhaust steam waste heat plural serial stage heating system - Google Patents
Air cooling unit exhaust steam waste heat plural serial stage heating system Download PDFInfo
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- CN204404310U CN204404310U CN201520011643.6U CN201520011643U CN204404310U CN 204404310 U CN204404310 U CN 204404310U CN 201520011643 U CN201520011643 U CN 201520011643U CN 204404310 U CN204404310 U CN 204404310U
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- 238000010438 heat treatment Methods 0.000 title claims abstract description 87
- 239000002918 waste heat Substances 0.000 title claims abstract description 20
- 238000001816 cooling Methods 0.000 title claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000000605 extraction Methods 0.000 claims description 20
- 239000007789 gas Substances 0.000 claims 6
- 238000009833 condensation Methods 0.000 claims 4
- 230000005494 condensation Effects 0.000 claims 4
- 238000005516 engineering process Methods 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000006378 damage Effects 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
Description
技术领域 technical field
本实用新型涉及一种利用直接空冷机组背压的梯度逐级加热热网循环水的多级串联供热系统,是直接回收机组乏汽余热的一种供热系统。 The utility model relates to a multi-stage series heating system which utilizes the gradient of the back pressure of a direct air-cooling unit to heat the circulating water of a heating network step by step, and is a heating system for directly recovering exhausted steam waste heat of the unit.
背景技术 Background technique
随着城镇化的不断推进,现有的城市供热热源的容量已不能满足城市新增负荷的需要。近几年来,利用机组的乏汽余热来供热的工程越来越多。目前利用余热供热的技术主要有三种:第一种是热泵供热技术,利用吸收式或压缩式热泵在一定高品质能量的驱动下来提取汽轮机乏汽余热与高品质能一并对热网循环水进行加热,一个采暖季的乏汽余热供热量占总供热量的比率约为30%-40%。第二种是前置凝汽器加热泵供热技术,利用前置凝汽器直接吸收机组的乏汽余热对热网循环水进行一级加热,利用热泵在一定高品质能的驱动下提取一部分乏汽余热一并与高品质能对热网循环水进行二级加热,一个采暖季的乏汽余热供热量占总供热量的比率约为45%-55%。第三种是高背压供热技术,将一台空冷机组的背压提高,通过设置大容量的凝汽器来直接吸收机组的乏汽余热加热热网循环水,一个采暖季的乏汽余热供热量占总供热量的比率约为55%-65%。以上余热供热的技术均存在余热利用率低的问题。 With the continuous advancement of urbanization, the capacity of existing urban heating sources can no longer meet the needs of new urban loads. In recent years, there have been more and more projects using the exhaust steam waste heat of the unit for heating. At present, there are three main technologies for using waste heat for heating: the first is heat pump heating technology, which uses absorption or compression heat pumps to extract exhaust heat from steam turbines and high-quality energy to circulate the heating network under the drive of certain high-quality energy. Water is used for heating, and the ratio of exhaust steam waste heat to total heat supply in a heating season is about 30%-40%. The second is the pre-condenser heat pump heat supply technology, which uses the pre-condenser to directly absorb the exhaust heat of the unit to perform primary heating of the circulating water in the heating network, and uses the heat pump to extract a part of it under the drive of a certain high-quality performance. Combining exhaust steam and waste heat with high-quality energy can carry out secondary heating of the circulating water in the heating network. The ratio of exhaust steam and waste heat to the total heat supply in a heating season is about 45%-55%. The third is the high back pressure heating technology, which increases the back pressure of an air-cooled unit, and directly absorbs the waste steam heat of the unit by setting a large-capacity condenser to heat the circulating water of the heating network. The heat supply accounts for about 55%-65% of the total heat supply. The waste heat heating technologies above all have the problem of low utilization rate of waste heat.
发明内容 Contents of the invention
本实用新型提供了一种空冷机组乏汽余热多级串联供热系统,解决了现有余热供热技术存在的余热利用率低的技术问题。 The utility model provides a multi-stage series series heat supply system for exhaust steam waste heat of an air-cooling unit, which solves the technical problem of low utilization rate of waste heat existing in the existing waste heat heat supply technology.
本实用新型是通过以下技术方案解决以上技术问题的: The utility model solves the above technical problems through the following technical solutions:
一种空冷机组乏汽余热多级串联供热系统,包括第一级背压供热机组、第二级背压供热机组、第三级背压供热机组、第四级背压供热机组和尖峰加热器,第一级机组凝汽器的乏汽口通过第一级供热乏汽管道与第一级背压供热机组的直接空冷排汽管路连通在一起,第一级机组凝汽器的乏汽凝结水口通过第一级供热乏汽凝结水管道与第一级背压供热机组的排汽装置热井连通在一起,城市热网回水管路通过第一级机组凝汽器的进水管道与第一级机组凝汽器连通在一起,第一级背压供热机组的第一机组汽轮机通过第一级机组抽汽管道与尖峰加热器连通在一起,尖峰加热器上的第一级机组抽汽凝结水出口通过第一级机组抽汽凝结水管道与第一级背压供热机组的排汽装置热井连通在一起;第二级机组凝汽器的乏汽口通过第二级供热乏汽管道与第二级背压供热机组的直接空冷排汽管路连通在一起,第二级机组凝汽器的乏汽凝结水口通过第二级供热乏汽凝结水管道与第二级背压供热机组的排汽装置热井连通在一起,第一级机组凝汽器的出水口通过第二级机组凝汽器的进水管道与第二级机组凝汽器连通在一起,第二级背压供热机组的第二机组汽轮机通过第二级机组抽汽管道与尖峰加热器连通在一起,尖峰加热器上的第二级机组抽汽凝结水出口通过第二级机组抽汽凝结水管道与第二级背压供热机组的排汽装置热井连通在一起;第三级机组凝汽器的乏汽口通过第三级供热乏汽管道与第三级背压供热机组的直接空冷排汽管路连通在一起,第三级机组凝汽器的乏汽凝结水口通过第三级供热乏汽凝结水管道与第三级背压供热机组的排汽装置热井连通在一起,第二级机组凝汽器的出水口通过第三级机组凝汽器的进水管道与第三级机组凝汽器连通在一起,第三级背压供热机组的第三机组汽轮机通过第三级机组抽汽管道与尖峰加热器连通在一起,尖峰加热器上的第三级机组抽汽凝结水出口通过第三级机组抽汽凝结水管道与第三级背压供热机组的排汽装置热井连通在一起;第四级机组凝汽器的乏汽口通过第四级供热乏汽管道与第四级背压供热机组的直接空冷排汽管路连通在一起,第四级机组凝汽器的乏汽凝结水口通过第四级供热乏汽凝结水管道与第四级背压供热机组的排汽装置热井连通在一起,第三级机组凝汽器的出水口通过第四级机组凝汽器的进水管道与第四级机组凝汽器连通在一起,第四级机组凝汽器的出水口通过第四级机组凝汽器的出水管路与尖峰加热器连通,在尖峰加热器的出水口上连接有城市热网循环水供水管路。 A multi-stage series heat supply system of exhaust steam waste heat of an air-cooling unit, including a first-stage back-pressure heating unit, a second-stage back-pressure heating unit, a third-stage back-pressure heating unit, and a fourth-stage back-pressure heating unit And the peak heater, the exhaust steam port of the first-stage unit condenser is connected with the direct air-cooled exhaust pipeline of the first-stage back-pressure heating unit through the first-stage heating exhaust pipe, and the first-stage unit condensing The exhaust steam condensate port of the boiler is connected with the hot well of the exhaust device of the first-stage back pressure heating unit through the first-stage heat-supply exhaust-steam condensate pipe, and the return water pipe of the urban heating network passes through the first-stage unit condensate The inlet pipe of the condenser is connected with the condenser of the first-stage unit, and the steam turbine of the first unit of the first-stage back-pressure heating unit is connected with the peak heater through the extraction pipe of the first-stage unit, and the peak heater The steam extraction condensate outlet of the first-stage unit is connected with the hot well of the exhaust device of the first-stage back pressure heating unit through the steam extraction condensate pipe of the first-stage unit; the exhaust steam port of the condenser of the second-stage unit Through the second-stage heating exhaust steam pipeline, it is connected with the direct air-cooled exhaust steam pipeline of the second-stage back-pressure heating unit, and the exhaust steam condensate port of the second-stage unit condenser is condensed through the second-stage heating exhaust steam The water pipe is connected with the hot well of the exhaust device of the second-stage back pressure heating unit, and the water outlet of the first-stage unit condenser is condensed with the second-stage unit condenser through the water inlet pipe of the second-stage unit The steam turbine of the second unit of the second-stage back pressure heating unit is connected with the peak heater through the extraction pipe of the second-stage unit, and the condensate outlet of the second-stage unit on the peak heater is passed through the second-stage unit. The steam extraction condensate pipe of the second-stage unit is connected with the hot well of the exhaust device of the second-stage back pressure heating unit; the exhaust steam port of the condenser of the third-stage unit is connected to the third The direct air-cooled exhaust pipes of the first-stage back-pressure heating unit are connected together, and the exhaust steam condensate port of the third-stage unit condenser passes through the third-stage heating exhaust condensate pipe and the third-stage back-pressure heating unit. The hot well of the exhaust device is connected together, the water outlet of the condenser of the second stage unit is connected with the condenser of the third stage unit through the water inlet pipe of the condenser of the third stage unit, and the back pressure heat supply of the third stage The steam turbine of the third unit of the unit is connected with the peak heater through the third-stage unit extraction pipe, and the third-stage unit extraction condensate outlet on the peak heater is connected to the third-stage unit through the third-stage unit extraction condensate pipe. The hot well of the exhaust device of the back pressure heating unit is connected together; the exhaust steam port of the fourth-stage unit condenser passes through the fourth-stage heating exhaust pipe and the direct air-cooled exhaust pipe of the fourth-stage back-pressure heating unit The exhaust steam condensate outlet of the condenser of the fourth-stage unit is connected with the hot well of the exhaust device of the fourth-stage back-pressure heating unit through the fourth-stage heat-supply exhaust-steam condensate pipe, and the third-stage The water outlet of the condenser of the unit is connected with the condenser of the fourth unit through the inlet pipe of the condenser of the fourth unit, and the water outlet of the condenser of the fourth unit is connected with the condenser of the fourth unit The water outlet pipeline communicates with the peak heater, and the city heating network circulating water supply pipeline is connected to the water outlet of the peak heater.
本实用新型显著提高了机组供热的余热利用率,一个采暖季的乏汽余热供热量占总供热量的比率约为72-90%。并且简化了供热系统,使系统对于机组的适应性、供热温度调节的灵活性等方面得到了提高。 The utility model significantly improves the waste heat utilization rate of the heating unit, and the heat supply ratio of exhaust steam waste heat in a heating season to the total heat supply is about 72-90%. And the heating system is simplified, so that the adaptability of the system to the unit and the flexibility of heating temperature adjustment have been improved.
附图说明 Description of drawings
图1是本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
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:
一种空冷机组乏汽余热多级串联供热系统,包括第一级背压供热机组1、第二级背压供热机组2、第三级背压供热机组3、第四级背压供热机组4和尖峰加热器5,第一级机组凝汽器6的乏汽口通过第一级供热乏汽管道7与第一级背压供热机组1的直接空冷排汽管路8连通在一起,第一级机组凝汽器6的乏汽凝结水口通过第一级供热乏汽凝结水管道9与第一级背压供热机组1的排汽装置热井10连通在一起,城市热网回水管路11通过第一级机组凝汽器6的进水管道12与第一级机组凝汽器6连通在一起,第一级背压供热机组1的第一机组汽轮机13通过第一级机组抽汽管道14与尖峰加热器5连通在一起,尖峰加热器5上的第一级机组抽汽凝结水出口通过第一级机组抽汽凝结水管道24与第一级背压供热机组1的排汽装置热井10连通在一起;第二级机组凝汽器15的乏汽口通过第二级供热乏汽管道16与第二级背压供热机组2的直接空冷排汽管路17连通在一起,第二级机组凝汽器15的乏汽凝结水口通过第二级供热乏汽凝结水管道18与第二级背压供热机组2的排汽装置热井10连通在一起,第一级机组凝汽器6的出水口20通过第二级机组凝汽器15的进水管道21与第二级机组凝汽器15连通在一起,第二级背压供热机组2的第二机组汽轮机22通过第二级机组抽汽管道23与尖峰加热器5连通在一起,尖峰加热器5上的第二级机组抽汽凝结水出口通过第二级机组抽汽凝结水管道25与第二级背压供热机组2的排汽装置热井19连通在一起;第三级机组凝汽器26的乏汽口通过第三级供热乏汽管道27与第三级背压供热机组3的直接空冷排汽管路28连通在一起,第三级机组凝汽器26的乏汽凝结水口通过第三级供热乏汽凝结水管道29与第三级背压供热机组3的排汽装置热井30连通在一起,第二级机组凝汽器15的出水口31通过第三级机组凝汽器26的进水管道32与第三级机组凝汽器26连通在一起,第三级背压供热机组3的第三机组汽轮机33通过第三级机组抽汽管道34与尖峰加热器5连通在一起,尖峰加热器5上的第三级机组抽汽凝结水出口通过第三级机组抽汽凝结水管道35与第三级背压供热机组3的排汽装置热井30连通在一起;第四级机组凝汽器36的乏汽口通过第四级供热乏汽管道37与第四级背压供热机组4的直接空冷排汽管路38连通在一起,第四级机组凝汽器36的乏汽凝结水口通过第四级供热乏汽凝结水管道39与第四级背压供热机组4的排汽装置热井39连通在一起,第三级机组凝汽器26的出水口40通过第四级机组凝汽器36的进水管道41与第四级机组凝汽器36连通在一起,第四级机组凝汽器36的出水口42通过第四级机组凝汽器36的出水管路43与尖峰加热器5连通,在尖峰加热器5的出水口上连接有城市热网循环水供水管路45。 A multi-stage series heat supply system for exhaust steam and waste heat of an air-cooled unit, comprising a first-stage back-pressure heating unit 1, a second-stage back-pressure heating unit 2, a third-stage back-pressure heating unit 3, and a fourth-stage back-pressure heating unit. The heating unit 4 and the peak heater 5, the exhaust steam outlet of the first-stage unit condenser 6 passes through the first-stage heating exhaust pipeline 7 and the direct air-cooling exhaust pipeline 8 of the first-stage back-pressure heating unit 1 Connected together, the exhaust steam condensate port of the first-stage unit condenser 6 is communicated with the exhaust device hot well 10 of the first-stage back pressure heating unit 1 through the first-stage heating exhaust steam condensate pipeline 9, The urban heating network return water pipeline 11 communicates with the first-stage unit condenser 6 through the water inlet pipe 12 of the first-stage unit condenser 6, and the first-stage steam turbine 13 of the first-stage back-pressure heating unit 1 passes through The steam extraction pipe 14 of the first stage unit is connected with the peak heater 5, and the steam extraction condensate outlet of the first stage unit on the peak heater 5 is connected to the first stage back pressure supply through the steam extraction condensate pipe 24 of the first stage unit. The hot well 10 of the steam exhaust device of the thermal unit 1 is connected together; the exhaust steam port of the condenser 15 of the second-stage unit passes through the exhaust steam pipe 16 of the second-stage heating supply and the direct air-cooled exhaust of the second-stage back-pressure heating unit 2 The steam pipeline 17 is connected together, and the exhaust steam condensate port of the condenser 15 of the second-stage unit passes through the exhaust steam condensate pipe 18 of the second-stage heating supply and the hot well 10 of the exhaust device of the second-stage back-pressure heating unit 2 Connected together, the water outlet 20 of the condenser 6 of the first-stage unit communicates with the condenser 15 of the second-stage unit through the water inlet pipe 21 of the condenser 15 of the second-stage unit, and the second-stage back pressure heat supply The steam turbine 22 of the second unit of unit 2 is connected with the peak heater 5 through the steam extraction pipeline 23 of the second unit, and the steam extraction condensate outlet of the second unit on the peak heater 5 passes through the steam extraction condensate of the second unit The pipeline 25 communicates with the heat well 19 of the steam exhaust device of the second stage back pressure heating unit 2; The direct air-cooled exhaust pipeline 28 of the pressure heating unit 3 is connected together, and the exhaust steam condensate port of the condenser 26 of the third-stage unit is connected with the third-stage back-pressure heating supply through the third-stage heating exhaust condensate pipeline 29 The hot well 30 of the exhaust device of the unit 3 is connected together, and the water outlet 31 of the condenser 15 of the second-stage unit is communicated with the condenser 26 of the third-stage unit through the water inlet pipe 32 of the condenser 26 of the third-stage unit. Together, the third-stage steam turbine 33 of the third-stage back-pressure heating unit 3 communicates with the peak heater 5 through the third-stage steam extraction pipeline 34, and the third-stage air extraction condensate outlet on the peak heater 5 Through the steam extraction condensate pipe 35 of the third-stage unit, it is connected with the hot well 30 of the steam exhaust device of the third-stage back-pressure heating unit 3; The exhaust steam pipeline 37 is connected with the direct air-cooled exhaust steam pipeline 38 of the fourth-stage back pressure heating unit 4, and the exhaust steam condensate port of the condenser 36 of the fourth-stage unit passes through the fourth-stage heating exhaust steam condensate pipeline 39 is communicated with the exhaust device hot well 39 of the fourth-stage back pressure heating unit 4, and the third-stage unit condenses The water outlet 40 of the condenser 26 communicates with the fourth-stage condenser 36 through the water inlet pipe 41 of the fourth-stage condenser 36, and the water outlet 42 of the fourth-stage condenser 36 passes through the fourth-stage The water outlet pipeline 43 of the unit condenser 36 communicates with the peak heater 5 , and the city heating network circulation water supply pipeline 45 is connected to the water outlet of the peak heater 5 .
本实用新型的有益效果是将供热热网水的加热系统优化至四级加热,减小了热网水在加热过程中的温度梯度差,从而减少了传热过程中的火用损。本系统简单,可以通过调整汽轮机背压参数实现供热参数灵活调节。本系统适用于火力发电厂直接空冷机组,特别适合多台机组并列运行的场合。 The utility model has the beneficial effects of optimizing the heating system of the heating network water to four-stage heating, reducing the temperature gradient difference of the heating network water in the heating process, thereby reducing the exergy loss in the heat transfer process. The system is simple, and the heating parameters can be flexibly adjusted by adjusting the steam turbine back pressure parameters. This system is suitable for direct air-cooling units in thermal power plants, especially for occasions where multiple units operate in parallel.
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| CN107191232A (en) * | 2017-06-06 | 2017-09-22 | 大唐东北电力试验研究所有限公司 | Electric heating unit heating system |
| CN107202356A (en) * | 2017-06-19 | 2017-09-26 | 北京北方三合能源技术有限公司 | A kind of exhaust heat stepped utilization heating system of fired power generating unit |
| CN107218093A (en) * | 2017-06-14 | 2017-09-29 | 联合瑞升(北京)科技有限公司 | Heating system and operation method are reclaimed in a kind of thermal power plant's exhaust steam |
| CN108870519A (en) * | 2018-07-19 | 2018-11-23 | 北京国电蓝天节能科技开发有限公司 | A kind of across season multi-level phase change heat reservoir suitable for high back pressure thermal power plant unit |
| WO2019201281A1 (en) * | 2018-04-19 | 2019-10-24 | 联合瑞升(北京)科技有限公司 | Exhaust steam waste heat recovery heat supply system for air cooling unit of large-scale thermal power plant |
| CN113006895A (en) * | 2021-04-01 | 2021-06-22 | 济南达能动力技术有限责任公司 | Method and system for reducing station power consumption rate of power plant |
| CN114526508A (en) * | 2022-03-11 | 2022-05-24 | 国能龙源蓝天节能技术有限公司 | Multi-grade low-level energy cascade heat supply system and method based on network source comprehensive energy conservation |
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2015
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| CN107191232A (en) * | 2017-06-06 | 2017-09-22 | 大唐东北电力试验研究所有限公司 | Electric heating unit heating system |
| CN107218093A (en) * | 2017-06-14 | 2017-09-29 | 联合瑞升(北京)科技有限公司 | Heating system and operation method are reclaimed in a kind of thermal power plant's exhaust steam |
| CN107218093B (en) * | 2017-06-14 | 2018-08-07 | 联合瑞升(北京)科技有限公司 | A kind of thermal power plant's steam exhaust recycling heating system and operation method |
| CN107202356B (en) * | 2017-06-19 | 2022-12-06 | 北京北方三合能源技术有限公司 | Waste heat cascade utilization heating system of thermal power generating unit |
| CN107202356A (en) * | 2017-06-19 | 2017-09-26 | 北京北方三合能源技术有限公司 | A kind of exhaust heat stepped utilization heating system of fired power generating unit |
| WO2019201281A1 (en) * | 2018-04-19 | 2019-10-24 | 联合瑞升(北京)科技有限公司 | Exhaust steam waste heat recovery heat supply system for air cooling unit of large-scale thermal power plant |
| US11085334B2 (en) | 2018-04-19 | 2021-08-10 | Uni-Rising(Beijing) Technology Co., Ltd. | Exhaust steam waste heat recovering and supplying system of air-cooling units in large thermal power plants |
| CN108870519A (en) * | 2018-07-19 | 2018-11-23 | 北京国电蓝天节能科技开发有限公司 | A kind of across season multi-level phase change heat reservoir suitable for high back pressure thermal power plant unit |
| CN108870519B (en) * | 2018-07-19 | 2023-10-27 | 国电龙源节能技术有限公司 | A cross-season multi-stage phase change heat storage system suitable for high back pressure heating units |
| CN113006895A (en) * | 2021-04-01 | 2021-06-22 | 济南达能动力技术有限责任公司 | Method and system for reducing station power consumption rate of power plant |
| CN113006895B (en) * | 2021-04-01 | 2022-02-15 | 济南达能动力技术有限责任公司 | Method and system for reducing station power consumption rate of power plant |
| CN114526508A (en) * | 2022-03-11 | 2022-05-24 | 国能龙源蓝天节能技术有限公司 | Multi-grade low-level energy cascade heat supply system and method based on network source comprehensive energy conservation |
| CN114526508B (en) * | 2022-03-11 | 2025-05-16 | 国能龙源蓝天节能技术有限公司 | Multi-grade low-energy cascade heating method based on comprehensive energy saving of network sources |
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