CN106918030A - A kind of coal-saving high temperature tower-type solar thermal complementation coal fired power plant integrated system - Google Patents
A kind of coal-saving high temperature tower-type solar thermal complementation coal fired power plant integrated system Download PDFInfo
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- 239000003245 coal Substances 0.000 title claims description 22
- 150000003839 salts Chemical class 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 238000003303 reheating Methods 0.000 claims abstract description 6
- 229920006395 saturated elastomer Polymers 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 4
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- 230000000295 complement effect Effects 0.000 abstract description 16
- 230000010354 integration Effects 0.000 abstract description 13
- 238000006243 chemical reaction Methods 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 2
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/22—Methods of steam generation characterised by form of heating method using combustion under pressure substantially exceeding atmospheric pressure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
- F01D15/10—Adaptations for driving, or combinations with, electric generators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/26—Steam-separating arrangements
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/50—Feed-water heaters, i.e. economisers or like preheaters incorporating thermal de-aeration of feed-water
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G1/00—Steam superheating characterised by heating method
- F22G1/16—Steam superheating characterised by heating method by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S60/00—Arrangements for storing heat collected by solar heat collectors
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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
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
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Abstract
本发明公开了一种节煤型高温塔式太阳能热互补燃煤电站集成系统,其特征在于,该系统包括:多个串联的高压加热器,多个串联的低压加热器,带有省煤器以及水冷壁的锅炉,汽水分离器,燃煤电站受热装置,太阳能加热器,以及汽轮机高压缸,汽轮机中压缸,汽轮机低压缸和发电机。本发明提出以熔盐为塔式太阳能集热系统中间换热工质并同时加热过热蒸汽与再热蒸汽的新型集成方案,不仅利用塔式太阳能集热器提高了太阳能热的集热温度,采取过热、再热两段集成的方法可避免太阳能热引入燃煤机组后产生的波动影响汽轮机的正常运行。本发明在太阳能热的高温利用方面相对传统的集成方式更为合理,同时也具有显著的热力学优势和经济性优势。
The invention discloses a coal-saving high-temperature tower-type solar thermal complementary coal-fired power station integrated system, which is characterized in that the system includes: a plurality of series-connected high-pressure heaters, a plurality of series-connected low-pressure heaters, with an economizer As well as boilers with water walls, steam-water separators, heating devices for coal-fired power stations, solar heaters, high-pressure cylinders for steam turbines, medium-pressure cylinders for steam turbines, low-pressure cylinders for steam turbines and generators. The present invention proposes a new integration scheme that uses molten salt as the intermediate heat exchange working medium of the tower solar heat collection system and simultaneously heats superheated steam and reheated steam, not only using the tower solar heat collector to increase the heat collection temperature of solar heat, but also adopting The two-stage integration method of superheating and reheating can avoid the fluctuation caused by the introduction of solar heat into the coal-fired unit from affecting the normal operation of the steam turbine. The invention is more reasonable than the traditional integration method in terms of high temperature utilization of solar heat, and also has significant thermodynamic and economical advantages.
Description
技术领域technical field
本发明属于太阳能热互补燃煤电站发电技术领域,具体涉及一种节煤型高温塔式太阳能热互补燃煤电站集成系统。The invention belongs to the technical field of power generation in solar thermal complementary coal-fired power plants, and in particular relates to a coal-saving high-temperature tower-type solar thermal complementary coal-fired power plant integrated system.
背景技术Background technique
自第一次工业革命起,化石能源在人类文明进步中担任重要角色。但从上世纪50年代欧洲的光化学污染,到如今国内的大范围雾霾,化石能源消耗带来的环境污染问题已经严重影响到人们健康。如今节能减排已经成为国际共识,发展多元化能源结构是各国努力的目标。太阳能以其独特的优势逐渐被重视,总体来讲发展太阳能有以下优势:无温室气体(主要是CO2,NOX)或有毒气体(SO2,颗粒)排放;增加区域/国家能源独立性;太阳能为可再生能源,能量充沛而且廉价。我国70%的电力来自于火力发电厂,受到资源和环境的制约,节能减排的工作越来越重要,许多耗煤量较高的中小型火力发电厂面临关停的命运。因此能源的互补利用逐渐开始成为能源系统重要的发展趋势。我国的太阳能资源非常丰富,太阳能辅助燃煤发电系统逐渐受到大家的重视。在传统太阳能热互补燃煤电站系统中,太阳能根据集成位置与集成温度的不同引入系统后对汽水系统以及汽轮机的运行工况影响较大。在传统太阳能热互补燃煤电站集成系统中,利用槽式太阳能集热器产生中低温热量的集成方式,这种方式不能高效、合理利用太阳能资源。本发明提出了一种塔式太阳能与常规燃煤电厂集成方案,不仅可以高效利用高温太阳能热,也可以利用太阳能加热再热蒸汽这一过程作为调控再热蒸汽温度的主要手段。汽轮机部分的运行工况并没有因为太阳能热的引入而改变,在减少给煤量的前提下也保证了太阳能热互补燃煤电站系统的安全运行。Since the first industrial revolution, fossil energy has played an important role in the progress of human civilization. However, from the photochemical pollution in Europe in the 1950s to the large-scale smog in China today, the environmental pollution caused by fossil energy consumption has seriously affected people's health. Nowadays, energy conservation and emission reduction has become an international consensus, and the development of a diversified energy structure is the goal of all countries. Solar energy is gradually being valued due to its unique advantages. Generally speaking, the development of solar energy has the following advantages: no greenhouse gas (mainly CO 2 , NO X ) or toxic gas (SO 2 , particles) emissions; increase regional/national energy independence; Solar energy is a renewable energy source that is plentiful and cheap. 70% of my country's electricity comes from thermal power plants. Constrained by resources and the environment, the work of energy conservation and emission reduction is becoming more and more important. Many small and medium thermal power plants with high coal consumption are facing the fate of shutting down. Therefore, the complementary utilization of energy has gradually become an important development trend of the energy system. my country's solar energy resources are very rich, and the solar-assisted coal-fired power generation system has gradually attracted everyone's attention. In the traditional solar thermal complementary coal-fired power station system, the solar energy introduced into the system according to the difference of integration position and integration temperature has a great influence on the operating conditions of the steam-water system and the steam turbine. In the traditional solar thermal complementary coal-fired power plant integrated system, the integration method of using trough solar collectors to generate medium and low temperature heat cannot efficiently and rationally utilize solar energy resources. The invention proposes an integration scheme of tower solar energy and conventional coal-fired power plants, which can not only efficiently utilize high-temperature solar heat, but also use the process of solar energy to heat reheat steam as the main means for regulating the temperature of reheat steam. The operating conditions of the steam turbine part have not changed due to the introduction of solar heat, and the safe operation of the solar thermal complementary coal-fired power plant system has also been ensured under the premise of reducing the amount of coal fed.
发明内容Contents of the invention
本发明以太阳能热互补燃煤电站系统为参考系统,通过改变系统中太阳能的集成位置与集成方式,提出以高温塔式太阳能热互补燃煤电站系统的节煤型新型集成系统。该系统采用以熔盐为塔式太阳能集热系统的中间换热工质,同时加热过热蒸汽与再热蒸汽的新型集成方案,不仅利用塔式太阳能集热器提高了太阳能热的集热温度,而且采取过热、再热两段集成的方法可避免太阳能热引入燃煤机组后产生的波动影响汽轮机的正常运行。在系统接收更多的太阳能的同时,节省更多的给煤量,提高太阳能的光-电转换效率。本发明在太阳能热的高温利用方面相对传统的集成方式更为合理,同时也具有显著的热力学优势和经济性优势。The invention takes the solar thermal complementary coal-fired power station system as a reference system, and proposes a new coal-saving integrated system using a high-temperature tower solar thermal complementary coal-fired power station system by changing the integration position and integration mode of solar energy in the system. The system uses molten salt as the intermediate heat exchange working medium of the tower solar heat collection system, and a new integrated scheme of heating superheated steam and reheated steam at the same time, not only using the tower solar collector to increase the heat collection temperature of solar heat, Moreover, the two-stage integration method of superheating and reheating can avoid the fluctuation caused by the introduction of solar heat into the coal-fired unit from affecting the normal operation of the steam turbine. While the system receives more solar energy, it saves more coal supply and improves the photoelectric conversion efficiency of solar energy. The invention is more reasonable than the traditional integration method in terms of high temperature utilization of solar heat, and also has significant thermodynamic and economical advantages.
本发明采用的技术方案为:The technical scheme adopted in the present invention is:
一种节煤型高温塔式太阳能热互补燃煤电站集成系统,包括多个串联的高压加热器,多个串联的低压加热器,带有省煤器以及水冷壁的锅炉,汽水分离器,燃煤电站受热装置,太阳能加热器,以及汽轮机高压缸,汽轮机中压缸,汽轮机低压缸和发电机。A coal-saving high-temperature tower-type solar thermal complementary coal-fired power plant integrated system, including multiple high-pressure heaters in series, multiple low-pressure heaters in series, boilers with economizers and water-cooled walls, steam-water separators, fuel-fired Heating devices of coal power stations, solar heaters, high-pressure cylinders of steam turbines, medium-pressure cylinders of steam turbines, low-pressure cylinders of steam turbines and generators.
其中,系统中各个部件的连接关系以及工艺流程如下:一级高压加热器出来的给水引入锅炉中经省煤器以及水冷壁受热面加热至饱和蒸汽状态,在汽水分离器中将饱和蒸汽分为两部分。一部分饱和蒸汽按照原有燃煤电站受热面布置方式依次流经低温过热器(低过)、分割屏过热器(分割屏)、后屏过热器(后屏)以及高温过热器(高过)。由于采用节省煤型模式,高过出口蒸汽温度会有所降低。另一部分饱和蒸汽引入太阳能加热器中与高温熔盐换热,然后将这部分过热蒸汽与高过出口蒸汽混合,维持主蒸汽(高压缸进汽)温度不变(566℃),随后通入高压缸(HP)中膨胀为发电机做功。汽轮机高压缸排汽需引入至锅炉中进行再热,排汽将依次通过锅炉内部低温再热器(低再)与高温再热器(高再)。由于采用节省煤型模式,高再出口蒸汽温度会有所降低。将再热蒸汽引入另一太阳能加热器与熔盐换热,维持再热蒸汽(中压缸进汽)温度不变(566℃),随后通入中压缸(IP)中膨胀为发电机做功,进入中压缸的这部分再热蒸汽按照燃煤电站汽水系统流程继续为发电机做功,依次流经低压缸(LP)、串联的低压加热器5,6,7,8、除氧器4以及串联的高压加热器1,2,3,从而完成整个循环。Among them, the connection relationship and process flow of each component in the system are as follows: the feed water from the first-stage high-pressure heater is introduced into the boiler and heated to the state of saturated steam through the economizer and the heating surface of the water wall, and the saturated steam is separated into steam in the steam-water separator. two parts. Part of the saturated steam flows through the low temperature superheater (low superheater), split screen superheater (split screen), rear screen superheater (back screen) and high temperature superheater (high superheater) in sequence according to the original layout of the heating surface of the coal-fired power station. Due to the coal-saving mode, the steam temperature above the outlet will be reduced. Another part of saturated steam is introduced into the solar heater to exchange heat with high-temperature molten salt, and then this part of superheated steam is mixed with high-pass outlet steam to maintain the temperature of the main steam (high-pressure cylinder inlet steam) at a constant temperature (566 ° C), and then pass into high-pressure Expansion in the cylinder (HP) does work for the generator. The exhaust steam from the high-pressure cylinder of the steam turbine needs to be introduced into the boiler for reheating, and the exhaust steam will pass through the low-temperature reheater (low reheater) and the high-temperature reheater (high reheater) inside the boiler in sequence. The high re-exit steam temperature will be reduced due to the coal-saving mode. The reheated steam is introduced into another solar heater to exchange heat with molten salt, and the temperature of the reheated steam (steam entering the medium-pressure cylinder) remains constant (566°C), and then it is passed into the medium-pressure cylinder (IP) to expand to work for the generator , this part of the reheated steam entering the medium-pressure cylinder continues to work for the generator according to the steam-water system flow of the coal-fired power station, and flows through the low-pressure cylinder (LP), the series-connected low-pressure heaters 5, 6, 7, 8, and the deaerator 4 And the high pressure heaters 1,2,3 connected in series to complete the whole cycle.
进一步,所述燃煤电站受热装置包括低过、分隔屏、后屏和高过设备,以及低再和高再设备,除氧器。Further, the heating device of the coal-fired power station includes low-pass, partition screen, rear screen and high-pass equipment, low-regeneration and high-regeneration equipment, and a deaerator.
进一步,所述太阳能加热器包括定日镜,塔式接收器和多个高温熔盐槽式换热器。Further, the solar heater includes a heliostat, a tower receiver and a plurality of high-temperature molten salt tank heat exchangers.
进一步,所述高温熔盐槽式换热器的数目是2个,一个用于将饱和蒸汽加热至过热蒸汽状态,并与高过出口的过热蒸汽混合以维持高压缸进汽温度不变。另一个用于将高再出口低于额定温度的再热蒸汽加热至额定温度。Further, the number of the high-temperature molten salt tank heat exchangers is two, one is used to heat the saturated steam to a superheated steam state, and mix it with the superheated steam higher than the outlet to maintain the high-pressure cylinder inlet steam temperature constant. The other is used to heat the reheat steam below the rated temperature at the high re-exit to the rated temperature.
进一步,用于加热再热蒸汽的高温熔盐槽式换热器还带有烟道挡板装置作为辅助手段,避免挡板法调节失效的问题。传统的烟道挡板法用分割烟道挡板法调控再热蒸汽温度的优点是结构简单,操作方便,已被许多大型电站锅炉采用。但缺点是汽温调节的时滞太大,挡板的开度与汽温变化为非线性关系,开度有效范围较窄。烟气挡板在40%~60%开度具有良好的调节性能,烟气份额在30%~70%具有良好的汽温调节性能。但如果烟气份额低于25%或高于75%,挡板将起不到调节作用,再热器汽温的调节手段将失效,不再能保证再热器的额定汽温。Furthermore, the high-temperature molten salt tank heat exchanger used for heating and reheating steam is also equipped with a flue baffle device as an auxiliary means to avoid the failure of the baffle method. The traditional flue baffle method uses the divided flue baffle method to regulate the reheat steam temperature. The advantages are simple structure and convenient operation. It has been adopted by many large power plant boilers. But the disadvantage is that the time lag of the steam temperature adjustment is too large, the opening of the baffle and the change of the steam temperature are in a nonlinear relationship, and the effective range of the opening is narrow. The flue gas baffle has good regulating performance when the opening degree is 40%-60%, and the flue gas ratio is 30%-70% and has good steam temperature regulating performance. However, if the flue gas share is lower than 25% or higher than 75%, the baffle will not be able to regulate, and the means for adjusting the steam temperature of the reheater will be invalid, and the rated steam temperature of the reheater can no longer be guaranteed.
本发明的有益效果为:与以往采用太阳能加热给水/凝结水方案相比较,本发明采用太阳能加热高温蒸汽,由于没有回热抽汽量的变化,不会影响整个汽轮机通流中的蒸汽流量、压力、温度和所做功量。不用为了保证机组安全运行,对各级回热抽汽进行计算校核。另外,本发明使用超临界直流锅炉,没有汽包,储热容量小,因此,在同一程度的干扰下,蒸汽温度的变化相比汽包锅炉会更明显,而且本发明可以很好地控制主蒸汽和再热蒸汽的温度。The beneficial effects of the present invention are: compared with the previous scheme of using solar energy to heat feed water/condensate water, the present invention uses solar energy to heat high-temperature steam, and since there is no change in the amount of regenerative steam extraction, it will not affect the steam flow in the entire steam turbine flow, Pressure, temperature and amount of work done. In order to ensure the safe operation of the unit, there is no need to calculate and check the regenerative steam extraction at all levels. In addition, the present invention uses a supercritical once-through boiler, without a steam drum, and has a small heat storage capacity. Therefore, under the same degree of interference, the change of steam temperature will be more obvious than that of a steam drum boiler, and the present invention can well control the main steam and reheat steam temperature.
附图说明Description of drawings
图1为本发明节煤型高温塔式太阳能热互补燃煤电站集成系统太阳能热部分流程示意图。Fig. 1 is a schematic flow chart of the solar thermal part of the coal-saving high-temperature tower solar thermal complementary coal-fired power plant integrated system of the present invention.
图2为本发明节煤型高温塔式太阳能热互补燃煤电站集成系统燃煤电站部分流程示意图。Fig. 2 is a schematic flow diagram of part of the coal-fired power station of the coal-saving high-temperature tower-type solar thermal complementary coal-fired power station integration system of the present invention.
图中:1-一级高压加热器;2-二级高压加热器;3-三级高压加热器;4-除氧器;5-一级低压加热器;6-二级低压加热器;7-三级低压加热器;8-四级低压加热器;HP为汽轮机高压缸;IP为汽轮机中压缸;LP为汽轮机低压缸;G为发电机。In the figure: 1-level one high pressure heater; 2-two level high pressure heater; 3-three level high pressure heater; 4-deaerator; 5-level one low pressure heater; 6-two level low pressure heater; 7 -Three-stage low-pressure heater; 8-four-stage low-pressure heater; HP is the high-pressure cylinder of the steam turbine; IP is the medium-pressure cylinder of the steam turbine; LP is the low-pressure cylinder of the steam turbine; G is the generator.
具体实施方式detailed description
本发明基于传统太阳能热互补燃煤电站系统,通过改变系统流程提出了一种性能更优的系统集成方案,下面通过附图和具体实施方式对本发明做进一步说明。燃煤机组选取660MW超临界火电机组作为参考系统。Based on the traditional solar thermal complementary coal-fired power station system, the present invention proposes a system integration solution with better performance by changing the system flow. The present invention will be further described with the accompanying drawings and specific implementation methods below. The coal-fired unit selects a 660MW supercritical thermal power unit as a reference system.
系统流程图如图1和图2所示:一级高压加热器(1)出口的给水引入锅炉中经省煤器以及水冷壁等受热面加热至饱和蒸汽状态,之后在汽水分离器出口处分为两部分。一部分饱和蒸汽按照原有燃煤电站受热面布置方式依次流经低过、分隔屏、后屏以及高过。另一部分饱和蒸汽引入#1太阳能加热器中与高温熔盐换热,然后将这部分过热蒸汽与高过出口蒸汽混合,维持主蒸汽温度不变(566℃)随后通入高压缸(HP)中膨胀做功。汽轮机高压缸排汽引入至锅炉中进行再热,高压缸排汽将依次通过锅炉内部低过与高再。高过出口的再热蒸汽引入#2太阳能加热器与高温熔盐换热,将再热蒸汽温度加热至566℃,随后通入中压缸(IP)中膨胀为发电机做功,进入中压缸的这部分再热蒸汽按照燃煤电站汽水系统流程继续为发电机做功,依次流经低压缸(LP)、串联的低压加热器5,6,7,8、除氧器4以及串联的高压加热器1,2,3,从而完成整个循环。被太阳能加热后的再热蒸汽与原燃煤电站系统再热蒸汽热力参数(温度、压力、流量等)完全相同,因此经太阳能加热后的再热蒸汽并不影响之后的热力循环。由上述可知,太阳能的引入减少了燃煤电站的给煤量,锅炉传递给蒸汽(水)的热量减少,使得过热蒸汽以及再热蒸汽不能达到额定温度,影响燃煤机组的安全运行。本发明利用太阳能将过热蒸汽以及再热蒸汽加热至额定温度,弥补了因为减少给煤量而导致的蒸汽吸热量不足的影响。The system flow chart is shown in Figure 1 and Figure 2: the feed water at the outlet of the primary high-pressure heater (1) is introduced into the boiler and heated to a saturated steam state by the heating surfaces such as the economizer and the water wall, and then divided into two parts. Part of the saturated steam flows through the lower pass, the partition screen, the rear screen and the higher pass in sequence according to the original layout of the heating surface of the coal-fired power station. Another part of saturated steam is introduced into #1 solar heater to exchange heat with high-temperature molten salt, and then this part of superheated steam is mixed with high-pass outlet steam to maintain the main steam temperature (566°C) and then pass into the high-pressure cylinder (HP) Expansion works. The exhaust steam from the high-pressure cylinder of the steam turbine is introduced into the boiler for reheating, and the exhaust steam from the high-pressure cylinder will pass through the low pass and high reheat inside the boiler in turn. The reheated steam higher than the outlet is introduced into #2 solar heater to exchange heat with high-temperature molten salt, and the temperature of the reheated steam is heated to 566°C, and then it is passed into the intermediate pressure cylinder (IP) to expand to work for the generator, and then enters the medium pressure cylinder This part of the reheated steam continues to work for the generator according to the steam-water system flow of the coal-fired power station, and flows through the low-pressure cylinder (LP), the series-connected low-pressure heaters 5, 6, 7, 8, the deaerator 4 and the series-connected high-pressure heating Devices 1, 2, 3, thus completing the entire cycle. The thermal parameters (temperature, pressure, flow, etc.) of the reheated steam heated by solar energy are exactly the same as those of the original coal-fired power plant system, so the reheated steam heated by solar energy does not affect the subsequent thermodynamic cycle. It can be seen from the above that the introduction of solar energy reduces the coal feed of coal-fired power plants, and the heat transferred from boilers to steam (water) is reduced, so that superheated steam and reheated steam cannot reach the rated temperature, which affects the safe operation of coal-fired units. The invention utilizes solar energy to heat superheated steam and reheated steam to the rated temperature, which makes up for the influence of insufficient steam heat absorption caused by reducing the amount of coal fed.
在塔式太阳能集热系统中,低温熔盐经熔盐泵引入塔式太阳能接收器中接收太阳能热量,经太阳能加热后的高温熔盐分为两部分分别流入#1太阳能加热器和#2太阳能加热器加热过热蒸汽和再热蒸汽。换热后的两部分低温熔盐汇集再次流入熔盐泵中构成循环。在塔式太阳能集热系统中利用#2太阳能加热器加热再热蒸汽这一过程作为调控再热蒸汽温度的主要手段,烟道挡板法作为辅助调节手段,避免了传统分割烟道挡板法调控再热蒸汽温度时当烟气份额低于25%或高于75%挡板法调节失效的问题。In the tower solar heat collection system, the low temperature molten salt is introduced into the tower solar receiver through the molten salt pump to receive solar heat, and the high temperature molten salt heated by solar energy is divided into two parts and flows into #1 solar heater and #2 solar heater respectively The device heats superheated steam and reheated steam. After heat exchange, the two parts of low-temperature molten salt are collected and flow into the molten salt pump again to form a cycle. In the tower solar collector system, the process of heating the reheated steam with the #2 solar heater is used as the main means to control the temperature of the reheated steam, and the flue baffle method is used as an auxiliary adjustment method, avoiding the traditional division of the flue baffle method When adjusting the reheat steam temperature, when the flue gas share is lower than 25% or higher than 75%, the baffle method regulation fails.
下面结合算例,对本发明进一步说明。Below in conjunction with calculation example, the present invention is further described.
系统初始条件:本发明以一台660MW超临界火电机组作为参考系统,机组的主要参数如表1所示。为了准确衡量不同工况下太阳能的引入对机组节煤量以及性能的影响,定义两个参数:System initial conditions: The present invention takes a 660MW supercritical thermal power unit as a reference system, and the main parameters of the unit are shown in Table 1. In order to accurately measure the impact of the introduction of solar energy on the coal saving and performance of the unit under different working conditions, two parameters are defined:
式中,ηse是光电转换效率;PS是太阳能输出功率(W);是总的太阳能辐照能量(kJ/h);PZ是互补系统输出功率(W);是锅炉总的热负荷(kJ/h);ηref是参考系统原燃煤电厂的效率;b是供电煤耗(g/kWh);msc是转换到标煤的燃煤量(kg);E是电厂输出的电能(kWh)。In the formula, η se is the photoelectric conversion efficiency; P S is the solar energy output power (W); is the total solar radiation energy (kJ/h); P Z is the complementary system output power (W); is the total heat load of the boiler (kJ/h); η ref is the efficiency of the original coal-fired power plant of the reference system; b is the coal consumption for power supply (g/kWh); m sc is the coal consumption converted to standard coal (kg); E is the electrical energy output by the power plant (kWh).
表2为抽取11%蒸汽流量后的系统主要参数变化;表3为新系统中各设计点参数;表4为新系统的全年热力特性。在太阳能镜场规模的设计中,应考虑有一个最佳的太阳能镜场面积。因为当太阳能镜场面积增大时,新系统可以利用更多的太阳能从而节省更多的煤量。但是随着太阳能输入量的增加,太阳能的光-电转换效率并不是一直增大的,而是在达到某一值之后开始下降。新系统最佳设计点参数如表5所示。Table 2 shows the main parameter changes of the system after extracting 11% steam flow; Table 3 shows the parameters of each design point in the new system; Table 4 shows the annual thermodynamic characteristics of the new system. In the design of solar mirror field scale, an optimal solar mirror field area should be considered. Because when the solar mirror field area increases, the new system can use more solar energy and thus save more coal. However, with the increase of solar energy input, the photoelectric conversion efficiency of solar energy does not increase all the time, but begins to decrease after reaching a certain value. The optimal design point parameters of the new system are shown in Table 5.
表1基准燃煤电站的主要参数Table 1 The main parameters of the benchmark coal-fired power station
表2抽取11%蒸汽流量后的系统主要参数变化Table 2 Changes of main parameters of the system after extracting 11% steam flow
表3新系统中各设计点参数Table 3 Parameters of each design point in the new system
表4新系统的全年热力特性Table 4 Annual thermal characteristics of the new system
表5新系统最佳设计点参数Table 5 Optimum design point parameters of the new system
如表3、表4所示,互补系统相比原系统,煤耗减少7.7g/kWh,全厂效率提高1.07%,最大瞬时光电转换效率可达23.16%,年光电转换效率为15.36%。而在最佳设计点下,表5所示,年光电转换效率提高到16.97%。对于现有单一的太阳能热发电技术,本发明节煤型高温塔式太阳能热互补燃煤电站集成系统更加节约成本,因此具有一定的经济性优势。As shown in Table 3 and Table 4, compared with the original system, the complementary system can reduce coal consumption by 7.7g/kWh, increase the efficiency of the whole plant by 1.07%, the maximum instantaneous photoelectric conversion efficiency can reach 23.16%, and the annual photoelectric conversion efficiency is 15.36%. And under the optimal design point, as shown in Table 5, the annual photoelectric conversion efficiency increases to 16.97%. For the existing single solar thermal power generation technology, the coal-saving high-temperature tower-type solar thermal complementary coal-fired power plant integrated system of the present invention is more cost-effective, so it has certain economic advantages.
以上对本发明进行了详细说明,显然,只要实质上没有脱离本发明的发明点及效果、对本领域的技术人员来说是显而易见的变形,也均包含在本发明的保护范围之内。The present invention has been described in detail above, obviously, as long as it does not substantially deviate from the invention point and effect of the present invention and is obvious to those skilled in the art, it is also included in the protection scope of the present invention.
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