CN103629857B - Based on the thermal power cogeneration central heating system of heat pump - Google Patents
Based on the thermal power cogeneration central heating system of heat pump Download PDFInfo
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Abstract
一种基于热泵的热电联产集中供热系统,通过引入吸收式换热机组、多级电驱动热泵,多次对热源进行以动力源和换热使用,提高了蒸汽热源的利用效率,更好的为用户供热;引入太阳能集热器,利用太阳能这一清洁能源对一次网回水进行升温,节能环保;另外在热电厂中加入换热器,用凝汽机中的低品位热源提升一次网回水水温,同时引入蒸汽双效吸收式热泵、蒸汽单效吸收式热泵、蒸汽大温差吸收式热泵、汽水换热器逐级回收低品位的热量,有效的利用了汽轮机中的乏汽,提高了能源利用效率。本系统提供电厂发电效率30%以上。
A heat pump-based cogeneration central heating system, through the introduction of absorption heat exchange units and multi-stage electric drive heat pumps, the heat source is used as a power source and heat exchange multiple times, which improves the utilization efficiency of the steam heat source and is better Provide heat for users; introduce solar collectors, use solar energy as a clean energy to heat up the return water of the primary network, save energy and protect the environment; in addition, add heat exchangers to the thermal power plant, use the low-grade heat source in the condenser to increase the temperature of the primary network return At the same time, the steam double-effect absorption heat pump, steam single-effect absorption heat pump, steam large temperature difference absorption heat pump, and steam-water heat exchanger are introduced to recover low-grade heat step by step, effectively utilizing the exhaust steam in the steam turbine, and improving the energy efficiency. This system provides power generation efficiency of more than 30%.
Description
技术领域technical field
本发明属于热电联产供热领域,尤其涉及一种基于热泵的热电联产集中供热系统。The invention belongs to the field of combined heat and power heat supply, in particular to a heat pump-based centralized heat supply system for combined heat and power.
背景技术Background technique
在近些年随着我国城市供暖面积的增加及工业厂房、生产线建设的加大,使得我国热力消费量快速增长。从供热方式上进行分析,目前我国居民采暖主要有以下几种方式:热电联产方式、中小型区域锅炉房集中供热、家用小型燃气热水炉、家庭燃煤炉等等。其中热电联产方式是利用燃料的高品位热能发电后,将其低品位热能供热的综合利用能源的技术。目前我国300万千瓦火力电厂的平均发电效率为33%,而热电厂供热时发电效率可达20%,剩下的80%热量中的70%以上可用于供热。1万千焦热量的燃料,采用热电联产方式,可产生2000千焦电力和7000千焦热量。而采用普通火力发电厂发电,此2000千焦电力需消耗6000千焦燃料。因此,将热电联产方式产出的电力按照普通电厂的发电效率扣除其燃料消耗,剩余的4000千焦燃料可产生7000千焦热量。从这个意义上讲,则热电厂供热的效率为170%,约为中小型锅炉房供热效率的2倍。因此在条件允许时,应优先发展热电联产的采暖方式。尽管如此,在热电联产方式供热中还是存在着一些问题,例如:汽轮机乏汽直接进入冷却塔浪费了大量的能量,使得大量汽化潜热没有得到充分利用。同时供热所需的蒸汽大大降低了发电效率等等。In recent years, with the increase of urban heating area in my country and the construction of industrial plants and production lines, the heat consumption in my country has grown rapidly. From the analysis of heating methods, there are mainly the following heating methods for residents in my country: combined heat and power generation, central heating in small and medium-sized regional boiler rooms, small household gas-fired water heaters, household coal-fired furnaces, etc. Among them, the cogeneration method is a comprehensive energy utilization technology that uses high-grade thermal energy of fuel to generate electricity and then supplies low-grade thermal energy for heating. At present, the average power generation efficiency of 3 million kilowatt thermal power plants in my country is 33%, while the power generation efficiency of thermal power plants can reach 20% when heating, and more than 70% of the remaining 80% of heat can be used for heating. The 10,000-kilojoule fuel can generate 2,000 kilojoules of electricity and 7,000 kilojoules of heat by cogeneration. However, if ordinary thermal power plants are used to generate electricity, the 2000 kilojoules of electricity will consume 6000 kilojoules of fuel. Therefore, if the electricity produced by cogeneration is deducted from the fuel consumption according to the power generation efficiency of ordinary power plants, the remaining 4,000 kilojoules of fuel can generate 7,000 kilojoules of heat. In this sense, the heating efficiency of thermal power plants is 170%, which is about twice that of small and medium-sized boiler rooms. Therefore, when conditions permit, the heating method of combined heat and power should be developed first. Nevertheless, there are still some problems in heat supply in the way of heat and power cogeneration, for example, a large amount of energy is wasted by exhaust steam from the steam turbine directly entering the cooling tower, so that a large amount of latent heat of vaporization is not fully utilized. At the same time, the steam required for heating greatly reduces the power generation efficiency and so on.
发明内容Contents of the invention
针对汽轮机乏汽中的大量汽化潜热不能够得到充分的利用等问题,本发明提供了一种基于热泵的热电联产集中供热系统。Aiming at the problem that a large amount of latent heat of vaporization in exhaust steam of a steam turbine cannot be fully utilized, the present invention provides a heat pump-based central heating system for cogeneration of heat and power.
本发明为解决技术问题所采用的技术方案为:The technical scheme that the present invention adopts for solving technical problems is:
在热电厂中,汽轮机中一部分高温蒸汽驱动发电机发电,另一部分高温蒸汽分别输入到蒸汽双效吸收式热泵、蒸汽单效吸收式热泵、蒸汽大温差吸收式热泵、汽水换热器,作为各级吸收式热泵机组的动力源参与换热;In a thermal power plant, part of the high-temperature steam in the steam turbine drives the generator to generate electricity, and the other part of the high-temperature steam is respectively input to the steam double-effect absorption heat pump, steam single-effect absorption heat pump, steam large temperature difference absorption heat pump, and steam-water heat exchanger. The power source of the absorption heat pump unit participates in heat exchange;
汽轮机中的乏气进入到凝汽机中,其中一部分换热为40℃的热水输入到换热器中将15℃的一次网回水换热为25℃,另一部分以并联的方式接入蒸汽双效吸收式热泵、蒸汽单效吸收式热泵、蒸汽大温差吸收式热泵,作为各级吸收式热泵机组的低温热源,换热后返回凝汽机中;25℃热水依次进入蒸汽双效吸收式热泵、蒸汽单效吸收式热泵、蒸汽大温差吸收式热泵分别加热至55℃、70℃、90℃,最后进入汽水换热器与蒸汽换热温度提高至110℃,作为一次网供水输入到吸收式换热机组;The exhaust gas in the steam turbine enters the condenser, and part of the hot water with a heat exchange rate of 40°C is input into the heat exchanger to exchange the heat of the return water of the primary network at 15°C to 25°C, and the other part is connected to steam in parallel Double-effect absorption heat pumps, steam single-effect absorption heat pumps, and steam large-temperature-difference absorption heat pumps are used as low-temperature heat sources for absorption heat pump units at all levels, and return to the condenser after heat exchange; hot water at 25°C enters the steam double-effect absorption The heat pump, steam single-effect absorption heat pump, and steam large temperature difference absorption heat pump are heated to 55°C, 70°C, and 90°C respectively, and finally enter the steam-water heat exchanger and the heat exchange temperature with steam is raised to 110°C, which is used as the primary network water supply input to the absorption type heat exchange unit;
在换热站中,110℃的一次网供水输入吸收式换热机组做为动力源,做功降温之后继续做为该吸收式换热机组的低温热源,做为低温热源换热后温度降低为25℃,该25℃的热水再做为低温热源输入到多级电驱动热泵中的蒸发器侧以便使冷凝器侧为用户提供60℃的热水供热,从多级电驱动热泵中的蒸发器侧排出的5℃的一次网回水输入到太阳能集热器中将一次网回水温度加热升温到15℃,然后通过换热器进入热电厂系统中。In the heat exchange station, the 110°C primary network water supply is input into the absorption heat exchange unit as the power source, and continues to be used as the low-temperature heat source of the absorption heat exchange unit after cooling down. As a low-temperature heat source, the temperature drops to 25 ℃, the 25℃ hot water is then used as a low-temperature heat source to input to the evaporator side of the multi-stage electric drive heat pump so that the condenser side can provide users with 60 ℃ hot water heating, and the evaporation from the multi-stage electric drive heat pump The 5°C primary network return water discharged from the side of the collector is input into the solar collector to heat the temperature of the primary network return water to 15°C, and then enters the thermal power plant system through the heat exchanger.
各级吸收式热泵和汽水换热器均采用0.3MPa左右的汽轮机供暖抽汽驱动。Absorption heat pumps and steam-water heat exchangers at all levels are driven by steam turbines around 0.3MPa for heating and extraction.
本发明的有益效果是:The beneficial effects of the present invention are:
引入吸收式换热机组、多级电驱动热泵,多次对热源进行以动力源和换热使用,提高了蒸汽热源的利用效率,更好的为用户供热;The absorption heat exchange unit and multi-stage electric drive heat pump are introduced, and the heat source is used as a power source and heat exchange many times, which improves the utilization efficiency of the steam heat source and better provides heat for users;
引入太阳能集热器,利用太阳能这一清洁能源对一次网回水进行升温,节能环保;Introduce solar heat collectors, use solar energy as a clean energy to heat up the return water of the primary network, energy saving and environmental protection;
另外在热电厂中加入换热器,用凝汽机中的低品位热源提升一次网回水水温,同时引入蒸汽双效吸收式热泵、蒸汽单效吸收式热泵、蒸汽大温差吸收式热泵、汽水换热器逐级回收低品位的热量,有效的利用了汽轮机中的乏汽,提高了能源利用效率。In addition, a heat exchanger is added to the thermal power plant, and the low-grade heat source in the condenser is used to increase the return water temperature of the primary network. At the same time, a steam double-effect absorption heat pump, a steam single-effect absorption heat pump, a steam large temperature difference absorption heat pump, and steam-water heat exchange are introduced. The low-grade heat is recovered step by step by the device, which effectively utilizes the exhaust steam in the steam turbine and improves the energy utilization efficiency.
本系统提供电厂发电效率30%以上。This system provides the power generation efficiency of the power plant above 30%.
附图说明Description of drawings
图1为本发明的原理图。Fig. 1 is a schematic diagram of the present invention.
图中:1.汽轮机,2.发电机,3.凝汽机,4.冷却塔,5.换热器,6.蒸汽双效吸收式热泵,7.蒸汽单效吸收式热泵,8.蒸汽大温差吸收式热泵,9.汽水换热器,10.吸收式换热机组,11.多级电驱动热泵,12.太阳能集热器,13.用户In the figure: 1. Steam turbine, 2. Generator, 3. Condenser, 4. Cooling tower, 5. Heat exchanger, 6. Steam double-effect absorption heat pump, 7. Steam single-effect absorption heat pump, 8. Steam large Temperature difference absorption heat pump, 9. Steam-water heat exchanger, 10. Absorption heat exchange unit, 11. Multi-stage electric drive heat pump, 12. Solar collector, 13. User
具体实施方式detailed description
在热电厂中,汽轮机1中一部分高温气体驱动发电机2发电,另一部分高温蒸汽分别输入到蒸汽双效吸收式热泵6、蒸汽单效吸收式热泵7、蒸汽大温差吸收式热泵8、汽水换热器9,作为各级吸收式热泵机组的动力源参与换热;In a thermal power plant, a part of the high-temperature gas in the steam turbine 1 drives the generator 2 to generate electricity, and the other part of the high-temperature steam is respectively input to the steam double-effect absorption heat pump 6, the steam single-effect absorption heat pump 7, the steam large temperature difference absorption heat pump 8, and the steam-water heat exchange The device 9, as the power source of the absorption heat pump units at all levels, participates in heat exchange;
汽轮机1中的乏气进入到凝汽机3中,其中一部分换热为40℃的热水输入到换热器5中将15℃的一次网回水换热为25℃,另一部分以并联的方式接入蒸汽双效吸收式热泵6、蒸汽单效吸收式热泵7、蒸汽大温差吸收式热泵8,作为各级吸收式热泵机组的低温热源,换热后返回凝汽机3中;25℃热水依次进入蒸汽双效吸收式热泵6、蒸汽单效吸收式热泵7、蒸汽大温差吸收式热泵8分别加热至55℃、70℃、90℃,最后进入汽水换热器9与蒸汽换热温度提高至110℃,作为一次网供水输入到吸收式换热机组10;The exhaust gas in the steam turbine 1 enters the condenser 3, and part of the hot water with a heat exchange rate of 40°C is input into the heat exchanger 5 to exchange the heat of the 15°C primary network return water to 25°C, and the other part is connected in parallel Connect steam double-effect absorption heat pump 6, steam single-effect absorption heat pump 7, and steam large temperature difference absorption heat pump 8, as the low-temperature heat source of absorption heat pump units at all levels, and return to condenser 3 after heat exchange; 25℃ hot water Enter steam double-effect absorption heat pump 6, steam single-effect absorption heat pump 7, and steam large temperature difference absorption heat pump 8 to heat up to 55°C, 70°C, and 90°C respectively, and finally enter steam-water heat exchanger 9 to increase heat exchange temperature with steam to 110°C, input to the absorption heat exchange unit 10 as primary network water supply;
在换热站中,110℃的一次网供水输入吸收式换热机组10做为动力源,做功降温之后继续做为该吸收式换热机组10的低温热源,做为低温热源换热后温度降低为25℃,该25℃的热水再做为低温热源输入到多级电驱动热泵11中的蒸发器侧以便使冷凝器侧为用户提供60℃的热水供热,从多级电驱动热泵11中的蒸发器侧排出的5℃的一次网回水输入到太阳能集热器12中将一次网回水温度加热升温到15℃,然后通过换热器5进入热电厂系统中。In the heat exchange station, the 110°C primary network water supply is input into the absorption heat exchange unit 10 as the power source, and continues to be used as the low-temperature heat source of the absorption heat exchange unit 10 after performing work and cooling down, and the temperature decreases after heat exchange as a low-temperature heat source The temperature is 25°C, and the 25°C hot water is then used as a low-temperature heat source to be input to the evaporator side of the multi-stage electric drive heat pump 11 so that the condenser side can provide users with 60°C hot water heating, and the multi-stage electric drive heat pump The 5°C primary network return water discharged from the evaporator side in 11 is input into the solar collector 12 to heat the primary network return water temperature to 15°C, and then enters the thermal power plant system through the heat exchanger 5.
各级吸收式热泵和汽水换热器均采用0.3MPa左右的汽轮机供暖抽汽驱动。Absorption heat pumps and steam-water heat exchangers at all levels are driven by steam turbines around 0.3MPa for heating and extraction.
本发明不局限于本实施例,任何在本发明披露的技术范围内的等同构思或者改变,均列为本发明的保护范围。The present invention is not limited to this embodiment, and any equivalent ideas or changes within the technical scope disclosed in the present invention are listed in the protection scope of the present invention.
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| CN111351254A (en) * | 2018-12-20 | 2020-06-30 | 大连民族大学 | Lithium Bromide Heat Pump Heating Method for Cogeneration of Heat and Power in Unmixed Heat Power Plant |
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| CN111351110A (en) * | 2018-12-20 | 2020-06-30 | 大连民族大学 | Solar powered lithium bromide heat pump heat supply method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007064047A (en) * | 2005-08-30 | 2007-03-15 | Hitachi Eng Co Ltd | Waste heat recovery equipment for steam turbine plant |
| CN101231004A (en) * | 2008-02-28 | 2008-07-30 | 清华大学 | A central heating system with large temperature difference |
| CN101619662A (en) * | 2009-08-14 | 2010-01-06 | 清华大学 | Method for recovering waste heat of thermal power plant and heating and supplying heat to hot water in a stepping way |
| KR100975276B1 (en) * | 2009-12-01 | 2010-08-12 | 주식회사 코와 | Local heating water feeding system using absorbing type heat pump |
| CN101949612A (en) * | 2010-08-27 | 2011-01-19 | 清华大学 | Cooling mode driven by utilizing urban heat supply network |
| CN203116356U (en) * | 2013-01-11 | 2013-08-07 | 杭州能源投资管理有限公司 | Refrigerating device of novel low temperature cogeneration cooling heating and power system based on heat pump |
-
2013
- 2013-12-04 CN CN201310655660.9A patent/CN103629857B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007064047A (en) * | 2005-08-30 | 2007-03-15 | Hitachi Eng Co Ltd | Waste heat recovery equipment for steam turbine plant |
| CN101231004A (en) * | 2008-02-28 | 2008-07-30 | 清华大学 | A central heating system with large temperature difference |
| CN101619662A (en) * | 2009-08-14 | 2010-01-06 | 清华大学 | Method for recovering waste heat of thermal power plant and heating and supplying heat to hot water in a stepping way |
| KR100975276B1 (en) * | 2009-12-01 | 2010-08-12 | 주식회사 코와 | Local heating water feeding system using absorbing type heat pump |
| CN101949612A (en) * | 2010-08-27 | 2011-01-19 | 清华大学 | Cooling mode driven by utilizing urban heat supply network |
| CN203116356U (en) * | 2013-01-11 | 2013-08-07 | 杭州能源投资管理有限公司 | Refrigerating device of novel low temperature cogeneration cooling heating and power system based on heat pump |
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