CN204574529U - The feedwater of a kind of combination type solar system supplymentary power plant and CO 2the integrated system of trapping - Google Patents
The feedwater of a kind of combination type solar system supplymentary power plant and CO 2the integrated system of trapping Download PDFInfo
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- CN204574529U CN204574529U CN201520038652.4U CN201520038652U CN204574529U CN 204574529 U CN204574529 U CN 204574529U CN 201520038652 U CN201520038652 U CN 201520038652U CN 204574529 U CN204574529 U CN 204574529U
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- 238000010248 power generation Methods 0.000 claims abstract description 22
- 238000010521 absorption reaction Methods 0.000 claims abstract description 15
- 239000000126 substance Substances 0.000 claims abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000003245 coal Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 52
- 239000007788 liquid Substances 0.000 claims description 14
- 239000012530 fluid Substances 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract description 22
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 9
- 239000003546 flue gas Substances 0.000 abstract description 9
- 238000005516 engineering process Methods 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000005086 pumping Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract description 3
- 239000000446 fuel Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 16
- 239000000243 solution Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000002427 irreversible Effects 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000011358 absorbing material Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- HZAXFHJVJLSVMW-UHFFFAOYSA-N ethanolamine Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 230000001737 promoting Effects 0.000 description 2
- 230000001172 regenerating Effects 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000023298 conjugation with cellular fusion Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000021037 unidirectional conjugation Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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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
Abstract
The utility model discloses the feedwater of a kind of combination type solar system supplymentary power plant and CO
2the integrated system of trapping, primarily of coal fuel heating power generation sub-system, chemical absorption method CO
2trapping subsystem, combined solar heat collector subsystem and multiple heat exchanger formed.Carry out being connected mainly through heat exchanger and associated pipe and valve between each subsystem and switch.Best heat-collecting temperature according to middle low-temperature solar energy heat collector realizes different combining forms, adopts different connected modes to the heat output of combined solar heat collector subsystem simultaneously, by solar energy heating and power generation sub-system and CO
2between trapping subsystem, to have carried out rational distribution integrated for the height of energy requirement grade of associated components, achieve the cascade utilization of energy, significantly can reduce the energy consumption of steam pumping from power plant steam turbine, while maintenance power plant stability, realize renewable energy utilization, power plant's efficiency improves and CO
2the multi-efficiencies such as reduction of discharging, promote the large-scale application of solar energy and flue gas trapping integrated technology.
Description
Technical field
The utility model relates to the feedwater heating of a kind of solar energy auxiliary power plant and CO
2trapping integrated technology, to be specifically related in a kind of combined type CO in low-temperature solar energy collecting system auxiliary power plant's backheat and flue gas
2the integrated system of trapping and method thereof, utilize solar energy to provide feed-water preheating and the CO of power plant's diverse location simultaneously
2the energy compensating of trapping system, while the combination thermal-arrest of low-temperature solar energy heat collector in the implementation, adequately achieves the cascade utilization of energy, significantly reduces the irreversible loss produced in the process of drawing gas, compensate for and draw gas for CO
2the impact of trapping on power plant.
Background technology
At present, in China Power structure, coal-fired thermal power generation is still in occupation of leading position, although technology is comparatively ripe, need to consume a large amount of fossil fuels, efficiency of energy utilization is low, CO
2discharge capacity is large, brings tremendous influence to climate change.
Coal-burning power plant CO
2trapping can realize a large amount of CO in a short time as one
2the possible technique of discharge, will play a significant role in reduction greenhouse gas emission, be that development and the alternative traditional energy thereof of regenerative resource provides transit time simultaneously.
The CO low for concentration in coal-fired plant flue gas, flow is large
2, the most promising method is that use can selective absorbing CO
2solvent carry out chemical absorbing, wherein monoethanolamine (MEA) solution is because absorption rate is fast, absorption efficiency is high, technology maturation, has been applied to coal-burning power plant CO
2trapping, but need during regeneration of waste liquor to consume a large amount of power plant steam, cause the decline of power plant efficiency, add trapping cost, become restriction CO
2the principal element of trapping technique large-scale application.
Solar energy is as the reproducible clean energy resource of one, and its developing and utilizingpotentiality is very huge.The solar thermal collector of different for solar energy heat-collecting temperature is combined, and with boiler water feeding preheating and CO
2trapping system combines, and utilizes solar energy heating to produce feed-water preheating at different levels and CO
2the temperature required heat energy of trapping system desorb carries out desorb, significantly can reduce the energy consumption of steam pumping from power plant steam turbine, while maintenance power plant stability, realize regenerative resource and power plant CO
2the double effects reduced discharging, the strong large-scale application promoting China's solar energy and flue gas trapping integrated technology.
The patent of the utility model related invention people, application number is disclose a kind of solar energy in the application for a patent for invention of 201410037906.0 to assist CO
2the integrated system of trapping, its major scheme is the feedwater heating of high-temperature heat-gathering auxiliary power plant Boiler High Pressure and CO in utilizing
2trapping, its mode implemented requires that solar thermal collector is middle high temperature heat collector.And this patent is utilizing the high-pressure feed water heating of solar energy auxiliary power plant and CO
2while trapping, propose the different schemes of auxiliary low pressure feed-water heater, introduce the concept that low-temperature heat collection device and high temperature heat collector are combined, achieve low-temperature heat collection device and heat and CO in power plant's feedwater
2application in trapping.
Summary of the invention
For the irreversible loss of the high-grade steam that high energy consumption problem and the trapping of drawing gas of current trapping system cause, the utility model proposes the feedwater heating of a kind of cascade utilization combined solar heat collector auxiliary power plant and CO
2the integrated system of trapping, according to the different temperatures demand of power plant feed water heater and trapping system, realizes solar energy and CO
2the difference of trapping and power plant's feedwater heating is integrated and connected relation, make full use of middle low-temperature solar energy thermal-arrest to compensate the energy requirements of traditional trapping system and power plant's feed heating system, while realizing solar energy cascade utilization, effectively reduce the efficiency decline that power plant brings because of steam pumping.
In order to effectively solve technical problem above, the feedwater heating of a kind of combined solar heat collector system supplymentary of the utility model power plant and CO
2the integrated system of trapping, comprises power generation sub-system, combined solar heat collector subsystem, CO
2trapping subsystem.
Described power generation sub-system is have single reheat coal generating system by the routine in series to water-to-water heat exchanger, boiler, steam turbine and exhaust steam condenser, coal-burning boiler produces superheated steam and enters the acting of steam turbine high-pressure cylinder, intermediate pressure cylinder and low pressure (LP) cylinder pushing turbine successively, exhaust steam is after condenser condensation, after four low-pressure feed heaters, oxygen-eliminating device and three high-pressure feed-water heaters, enter boiler successively again, complete steam/water circulating.Described power generation sub-system has eight grades and draws gas, and supply feed-water heater is used for heating boiler feed water.
Described CO
2trapping subsystem comprises absorption tower, rich solution pump, lean solution condenser, lean/rich liquid heat exchanger, lean pump, desorber, gas-liquid separator and reboiler; In described power generation sub-system, the smoke evacuation of boiler (comprises desulphurization denitration and dedusting) and enters absorption tower from the bottom on absorption tower, with chemical absorbent reactive absorption CO in absorption tower after flue gas pretreatment
2after, discharge from the top on absorption tower; Absorb CO
2after rich solution spray from the top of desorber after rich solution pump and the heat exchange of lean/rich liquid heat exchanger successively and carry out desorb into desorber, lean solution after desorb sprays into absorption tower from top, absorption tower more successively after lean pump, lean/rich liquid heat exchanger and lean solution condenser, thus forms whole flue gas CO
2trapping circulation.The gas vent at described desorber top is connected to the bottom of described gas-liquid separator, as the backflow of condensate liquid.
Described combined solar heat collector subsystem is made up of middle high temperature solar concentrating collector array and low temperature non-focusing type solar thermal collector array; Described middle high temperature solar concentrating collector array comprises some unit heat collector connection in series-parallel composition, described low temperature non-focusing type solar thermal collector is formed by the connection in series-parallel of some low-temperature heat collection devices, has multiple combination mode between middle high temperature focus type solar heat collector and low temperature non-focusing type solar thermal collector; One is tandem compound form: namely thermal-arrest working medium is successively through low temperature non-focusing type solar thermal collector array and middle high temperature solar concentrating collector array; One is parallel combination form: namely thermal-arrest working medium is divided into some stocks and enters by middle high-temp solar heat collector array and low temperature non-focusing type solar thermal collector array in porch, and heat collector outlet working medium mixes through blender; Also can be the combination of two kinds of modes above in addition.
Described high-pressure feed water heat exchanger 16 is in order to replace any one-level or whole in one-level high-pressure feed-water heater 05, secondary high-pressure feed-water heater 06 and three grades of high-pressure feed-water heaters 07; Described low pressure feed water heat exchanger 15 in order to replace in low-pressure feed heater 10 ~ 13 any one or more levels.
The utility model provides two kinds of different coupled modes according to the change of the change of solar thermal collector heat-collecting temperature and different heat collector combining form, namely the heat output of described solar thermal collector subsystem comprises one of following two kinds of situations with described high-low pressure to the annexation between water-to-water heat exchanger and described reboiler: Yi Zhongshi: the sender property outlet end in described combined solar heat collector subsystem is connected with the described high temperature side entrance of water-to-water heat exchanger of giving, described outlet to the high temperature side of water-to-water heat exchanger is connected with the high temperature side entrance of described reboiler, the high temperature side outlet of described reboiler is connected with the working medium arrival end of described combined solar heat collector subsystem, this connected mode can by combined solar heat collector subsystem thermal-arrest to high-temperature in about 200-350 DEG C, steam power plant's feed temperature is added by heat exchanger, heat exchange is proceeded through reboiler again after heat exchange, to provide the heat of reboiler, and the insufficient section of reboiler institute calorific requirement is provided by the steam extracting steam turbine low-temp low-pressure again, such formation solar energy heating circulation, achieves the cascade utilization of energy grade, reduces the irreversible loss of system, another kind is: the sender property outlet end of described combined solar heat collector subsystem is connected with the high temperature side arrival end of described reboiler, the high temperature side outlet of described reboiler is connected with the heat source side entrance of the low-pressure feed heater in power generation sub-system, outlet is then connected with the working medium arrival end of described combined solar heat collector subsystem, this connected mode can directly utilize combined solar heat collector subsystem to be utilized to the temperature range supply reboiler needed for reboiler by the working fluid thermal-arrest in solar thermal collector series, the waste heat simultaneously utilized by reboiler is as the Power supply of low-pressure feed heater, also structure can be made full use of more simple while simplification system, the middle low-temperature heat collection device that cost is cheaper, take full advantage of the collecting efficiency that solar thermal collection system is higher at low temperatures, decrease working fluid radiation loss at high temperature.Above-mentioned two kinds of connected modes all devise the connecting line from extracted steam from turbine, and can utilize to draw gas when solar energy is not enough like this provides heat.
Compared with prior art, the beneficial effects of the utility model are:
(1) high temperature solar concentrating collector and low temperature non-focusing type solar thermal collector are combined, achieve low-temperature heat collection device and the Appropriate application of high temperature heat collector under different temperatures scope, both avoid the low economy of high temperature heat collector in low-temperature end, turn avoid the poor efficiency of low-temperature heat collection device in temperature end.
(2) system has multiple CGCM, can carry out mating and switching according to solar energy heating temperature and heat-collecting capacity, and the method for operation is flexible, farthest achieves the cascade utilization of solar energy.
Accompanying drawing explanation
Fig. 1 is a kind of combination type solar system supplymentary of the utility model power plant's feedwater and CO
2the systematic schematic diagram of the integrated system embodiment 1 of trapping and structural representation;
Fig. 2 is a kind of combination type solar system supplymentary of the utility model power plant's feedwater and CO
2the systematic schematic diagram of the integrated system embodiment 2 of trapping and structural representation.
Fig. 3 is a kind of combination type solar system supplymentary of the utility model power plant's feedwater and CO
2the integrated system combination formula solar energy heating subsystem parallel combination schematic diagram of trapping and structural representation.
Fig. 4 is a kind of combination type solar system supplymentary of the utility model power plant's feedwater and CO
2the integrated system combination formula solar energy heating subsystem tandem compound schematic diagram of trapping and structural representation.
Fig. 5 ~ 7 are respectively a kind of combination type solar system supplymentary of the utility model power plant's feedwater and CO
2integrated system high-pressure feed water heat exchanger and the low pressure feed water heat exchanger of trapping replace feed-water heater combinatorial principle figure and structural representation.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the utility model is described in further detail.
The feedwater heating of a kind of combined solar heat collector system supplymentary of the utility model power plant and CO
2the integrated system of trapping, as shown in figures 1-4, comprises power generation sub-system 1, combined solar heat collector subsystem 2 and CO
2trapping subsystem 3, high-pressure feed water heat exchanger 15 and low pressure feed water heat exchanger 16.
Described power generation sub-system 1 is the coal generating system with single reheat be made up of boiler 01, steam turbine 02 ~ 04, feed-water heater 05 ~ 13 and exhaust steam condenser 14.Coal-burning boiler generation superheated steam enters steam turbine high-pressure cylinder 02, intermediate pressure cylinder 03 and low pressure (LP) cylinder 04 successively and does work, output power, exhaust steam after condenser 14 condensation successively through four low-pressure feed heaters 10 ~ 13, enter boiler after oxygen-eliminating device 09 and three high-pressure feed-water heaters 05 ~ 07, complete steam/water circulating.
Heat collector field in described combined solar heat collector subsystem 2 is combined by high temperature focusing solar collector array 21 and low temperature non-focusing type collector array 22, both forms thermal-arrest array by some heat collector serial or parallel connections.The heat-transfer working medium entered in combined solar heat collector subsystem 2 is introduced into low temperature non-focusing lane thermal-arrest array 22 and carries out preheating, then enters focus type thermal-arrest array 21 thermal-arrest temperature required to outlet.
Described CO
2trapping subsystem 3 comprises absorption tower 38, rich solution pump 37, lean solution condenser 31, lean/rich liquid heat exchanger 32, lean pump 33, desorber 34, gas-liquid separator 35 and reboiler 36; In described power generation sub-system, the smoke evacuation of boiler 3 is first through flue gas pretreatment, comprises desulphurization denitration and dust collecting process, and the flue gas after process is connected to bottom, absorption tower 38 gas access after temperature is reduced to 30-50 DEG C enters in tower carries out CO
2trapping; The outlet of described lean solution condenser 31 is connected with the upper liquid spray inlet on described absorption tower 38; Described lean/rich liquid heat exchanger 32 is connected with the entrance of the outlet of described lean pump 33, the rich solution spray inlet on described desorber 34 top, the outlet of described rich solution pump 37 and described lean solution condenser 31 respectively; Entrance bottom described desorber 34 is connected with the outlet of described reboiler 36 and the entrance of described lean pump 33 respectively, and the gas vent at described desorber 34 top is connected to the bottom of described gas-liquid separator 35, as the backflow of condensate liquid.CO
2the heat needed for reboiler 36 in trapping subsystem 3 is provided by solar energy, when solar energy provides deficiency then from the intermediate pressure cylinder 03 power generation sub-system 1 export with the tube connector of low pressure (LP) cylinder entrance 04 in extract steam reboiler heat be provided.
In the utility model, according to the difference of combined solar heat collector subsystem outlet temperature, combined solar heat collector subsystem and power generation sub-system and CO
2the connected mode of trapping subsystem has multiple.
Embodiment 1:
When the heat-collecting temperature of combined solar heat collector subsystem 2 exceedes boiler of power plant high-pressure feed-water heater outlet temperature (being greater than 300 DEG C), its annexation is: as shown in Figure 1, in in described combined solar heat collector subsystem 2, the sender property outlet end of high temperature solar concentrating collector array 21 is connected with the high temperature heat source side entrance of the high-pressure feed water heat exchanger 16 in power generation sub-system 1, in utilization, high-temp solar heat collector absorbs solar energy and carries out heat exchange and heat to replace HTHP extraction feedwater, the high temperature heat source side outlet of described high-pressure feed water heat exchanger 16 again with described CO
2the entrance of the reboiler 36 in trapping system 3 is connected, its outlet is then connected with the heat source side entrance of the low pressure feed water heat exchanger 15 in described power generation sub-system 1, the heat source side outlet of low pressure feed water heat exchanger 15 is connected with the working medium arrival end of combined solar heat collector subsystem 2 again, thus forms solar energy heating circulation.The connected mode of embodiment 1 can by the working medium thermal-arrest in combined solar heat collector subsystem to high-temperature in about 200-300 DEG C, realize the Power supply of feedwater and reboiler according to high-temperature heat-gathering in the positive good utilisation solar energy of variations in temperature of power plant's feed-water heater at different levels and reboiler, the insufficient section that simultaneity factor changes due to solar energy still can be realized by different levels drawing gas.The solar energy heating circulation of such formation, achieves the cascade utilization of energy grade, decreases the irreversible loss of system.
Embodiment 2:
When the heat-collecting temperature of combined solar heat collector subsystem 2 is no more than 150 DEG C, its annexation as shown in Figure 2, the sender property outlet end of described combined solar heat collector subsystem 2 and described CO
2the thermal source inlet end of the reboiler 36 in trapping subsystem 3 connects, the heat source side outlet of described reboiler 36 is connected with the heat source side entrance of the low pressure feed water heat exchanger 15 in described power generation sub-system 1, the heat source side outlet of low pressure feed water heat exchanger 15 is connected with the working medium arrival end of described combined solar heat collector subsystem 2, thus forms solar energy heating circulation.Solar energy heat-collection field in the connected mode of embodiment 2 can utilize structure more simple, low-temperature solar energy heat collector in lower to heat-collecting temperature requirement, thus reduces the cost of system.
To sum up, for the heat output of combined solar heat collector subsystem by adopting different connected mode, by solar energy heating and power generation sub-system and CO
2between trapping subsystem, the height of energy requirement grade of associated components has carried out rational distribution and integrated, achieve the cascade utilization of energy, significantly can reduce the energy consumption of steam pumping from power plant steam turbine, while maintenance power plant stability, realize renewable energy utilization and power plant CO
2the double effects reduced discharging, the strong large-scale application promoting China's solar energy and flue gas trapping integrated technology.
Described in the utility model, power generation sub-system is compared with conventional power generation systems, add the bypass of the high-pressure feed-water heater and low-pressure feed heater replacing diverse location to water-to-water heat exchanger, controlled by increasing valve, can switch utilizing solar energy and do not utilize between solar energy heating feedwater at different levels, do not affect the normal operation of the auxiliary heating that draws gas at different levels simultaneously.
CO described in the utility model
2trapping subsystem 3 is mainly applicable to the chemical absorbent aqueous solution based on alcamines material, namely can be the absorbent solution that single chemical absorbing material is made into, and also can be the composite absorber of number of chemical absorbing material proportioning composition.
In described combined solar heat collector subsystem 2, the selection form of high temperature focusing solar collector array 21 can be the forms such as groove type heat collector, Fresnel heat collector, dish-style heat collector and tower-type heat collector, and the selection of low temperature non-focusing type solar thermal collector array 22 can be the forms such as flat plate collector, vacuum tube collector and heat pipe collector.
In described combined solar heat collector subsystem 3, circulation of fluid generally adopts high temperature heat conductive oil as heat transfer medium, in addition, fuse salt or water also can be used as heat transfer medium.
Although composition graphs is described the utility model above; but the utility model is not limited to above-mentioned detailed description of the invention; above-mentioned detailed description of the invention is only schematic; instead of it is restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; when not departing from the utility model aim, can also make a lot of distortion, these all belong within protection of the present utility model.
Claims (5)
1. a combination type solar system supplymentary power plant feedwater and CO
2the integrated system of trapping, comprises coal fired power generation subsystem (1), combined solar heat collector subsystem (2), CO
2trapping subsystem (3); It is characterized in that:
Described power generation sub-system (1) is by coal-burning boiler (01), steam turbine high-pressure cylinder (02), intermediate pressure cylinder (03), low pressure (LP) cylinder (04), exhaust steam condenser (14), high-pressure feed-water heater (05 ~ 07), feed pump (08), oxygen-eliminating device (09) and low-pressure feed heater (10 ~ 13) steam generating system in series;
Described combined solar heat collector subsystem (2) mainly comprises middle high temperature solar concentrating collector array (21), low temperature non-focusing type solar thermal collector array (22);
Described CO
2trapping subsystem (3) comprises absorption tower (38), rich solution pump (37), lean solution condenser (31), lean/rich liquid heat exchanger (32), lean pump (33), desorber (34), gas-liquid separator (35) and reboiler (36);
The heat output of described combined solar heat collector subsystem (2) and described power generation sub-system high-pressure feed water heat exchanger (16), low pressure feed water heat exchanger (15), CO
2the connected mode of trapping subsystem reboiler (36) mainly comprises one of following two kinds of situations: Yi Zhongshi: the sender property outlet end in described combined solar heat collector subsystem (2) is connected with the high temperature side entrance of described high-pressure feed water heat exchanger (16), the high temperature side outlet of described high-pressure feed water heat exchanger (16) is connected with the high temperature side entrance of described reboiler (36), the high temperature side outlet of described reboiler (36) is connected with the heat source side entrance of described low-pressure feed heater (15), the heat source side outlet of described low pressure feed water heat exchanger (15) is connected with the working medium arrival end of described combined solar heat collector subsystem (2), another kind is: the sender property outlet end of described combined solar heat collector subsystem (2) is connected with the high temperature side arrival end of described reboiler (36), the high temperature side outlet of described reboiler (36) is connected with the heat source side import of described low pressure feed water heat exchanger (15), and the heat source side outlet of described low pressure feed water heat exchanger (15) is connected with the working medium arrival end of described combined solar heat collector subsystem (2).
2. a kind of combination type solar system supplymentary power plant according to claim 1 feedwater and CO
2the integrated system of trapping, it is characterized in that, described high-pressure feed water heat exchanger (16) is in order to replace any one-level or whole in one-level high-pressure feed-water heater (05), secondary high-pressure feed-water heater (06) and three grades of high-pressure feed-water heaters (07); Described low pressure feed water heat exchanger (15) in order to replace in low-pressure feed heater (10 ~ 13) any one or more levels.
3. a kind of combination type solar system supplymentary power plant according to claim 1 feedwater and CO
2the integrated system of trapping, it is characterized in that, described middle high temperature solar concentrating collector series is a kind of or several combination in compound parabolic concentrating collector, groove type heat collector, Fresnel heat collector, dish-style heat collector and tower-type heat collector, and described low temperature non-focusing type solar thermal collector series is a kind of or several combination in flat plate collector, vacuum tube collector and heat pipe collector.
4. a kind of combination type solar system supplymentary power plant according to claim 1 feedwater and CO
2the integrated system of trapping, it is characterized in that, the combination of described middle high temperature solar concentrating collector and low temperature non-focusing solar thermal collector can be series, parallel or hybrid mode, namely fluid working substance can be divided into the parallel series pipe that multiply enters low temperature non-focusing type solar thermal collector and middle high temperature solar concentrating collector, and the outlet working medium of different temperatures mixes to realize temperature required fluid again.
5. a kind of combination type solar system supplymentary power plant according to claim 1 feedwater and CO
2the integrated system of trapping, is characterized in that, the heat transfer medium of described combined solar heat collector subsystem selects the one in conduction oil, fuse salt, water, organic working medium and nano-fluid.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104613654A (en) * | 2015-01-13 | 2015-05-13 | 宁波瑞信能源科技有限公司 | Combined-type-solar-system power-plant water-feeding and CO2-collecting assisted integrated system |
| CN105169944A (en) * | 2015-08-26 | 2015-12-23 | 中石化节能环保工程科技有限公司 | Solar heating system |
| CN106076073A (en) * | 2016-07-28 | 2016-11-09 | 天津大学 | A kind of solar energy and the energy utility system of geothermal energy united power plant low-carbon emission |
| CN110404387A (en) * | 2019-06-19 | 2019-11-05 | 河北工程大学 | Solar energy assisted coal fired unit CO2Resource utilization system and device |
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| CN114183789A (en) * | 2021-11-22 | 2022-03-15 | 国家电投集团电站运营技术（北京）有限公司 | Thermodynamic system for supplying heat by complementation of solar energy and biomass |
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| CN104613654A (en) * | 2015-01-13 | 2015-05-13 | 宁波瑞信能源科技有限公司 | Combined-type-solar-system power-plant water-feeding and CO2-collecting assisted integrated system |
| CN105169944A (en) * | 2015-08-26 | 2015-12-23 | 中石化节能环保工程科技有限公司 | Solar heating system |
| CN106076073A (en) * | 2016-07-28 | 2016-11-09 | 天津大学 | A kind of solar energy and the energy utility system of geothermal energy united power plant low-carbon emission |
| CN106076073B (en) * | 2016-07-28 | 2019-01-11 | 天津大学 | A kind of energy utility system of solar energy and geothermal energy united power plant low-carbon emission |
| CN110404387A (en) * | 2019-06-19 | 2019-11-05 | 河北工程大学 | Solar energy assisted coal fired unit CO2Resource utilization system and device |
| CN114183790A (en) * | 2021-11-22 | 2022-03-15 | 国家电投集团电站运营技术（北京）有限公司 | Solar energy and biomass complementary heat supply method |
| CN114183789A (en) * | 2021-11-22 | 2022-03-15 | 国家电投集团电站运营技术（北京）有限公司 | Thermodynamic system for supplying heat by complementation of solar energy and biomass |
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