CN205549977U - Carbon dioxide capture system is jointly assisted with geothermal energy to solar energy - Google Patents
Carbon dioxide capture system is jointly assisted with geothermal energy to solar energy Download PDFInfo
- Publication number
- CN205549977U CN205549977U CN201620129921.2U CN201620129921U CN205549977U CN 205549977 U CN205549977 U CN 205549977U CN 201620129921 U CN201620129921 U CN 201620129921U CN 205549977 U CN205549977 U CN 205549977U
- Authority
- CN
- China
- Prior art keywords
- geothermal
- heat
- energy
- carbon dioxide
- solar energy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- 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
- Y02E10/10—Geothermal energy
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses a carbon dioxide capture system is jointly assisted with geothermal energy to solar energy is mainly by the power generation system of power plant, carbon dioxide capture system, solar energy collection system and geothermal energy system composition. The utility model discloses a carbon dioxide capture system carries out carbon dioxide's in power plant's flue gas desorption, the required heat of carbon dioxide entrapment in -process reboiler is jointly provided by solar energy and geothermal energy, under daytime solar energy sufficiency, the reboiler heat is provided by the solar energy collection system, the reboiler calorific requirement is then provided by geothermol power when not enough or evening of solar energy, coupling between them has realized capture system 's steady operation, the draw gas decline of the output electric power that causes of power plant has been reduced, solved the renewable energy utilization in -process because drawback that self defect caused, the dual efficiency that has realized that carbon dioxide entrapment and renewable energy reduce discharging, the integrated development of renewable energy with traditional electric power system has been promoted.
Description
Technical field
This utility model relates to a kind of solar energy and geothermal energy united auxiliary carbon dioxide trapping technique, it is specifically related to the integrated of middle low-temperature solar energy and geothermal energy and carbon dioxide in flue gas trapping system, solar energy and geothermal energy united is utilized to provide the energy compensating of carbon dioxide capture system, to reduce the intermittent impact on trapping system of solar energy, simultaneously effective reduce the efficiency decline that power plant is brought because of steam pumping.
Background technology
Collecting carbonic anhydride is to tackle one of climate change problem solution most with prospects with sealing (CCS) up for safekeeping.The CO that mankind's activity is caused2Emission source, the power industry based on thermal power plant and other energy conversion industries account for the 40% of total release, and the industrial trade such as iron and steel, cement accounts for 25.8%, these fixing CO2Emission source promotes the development of CCS technology.
At present at CO2Trapping aspect research and to use more be hydramine method (MEA process), it applies to the existing engineering mimoir in coal-burning power plant, but due to alcamines chemical absorbent and CO2Between adhesion relatively strong, therefore during regeneration, need water to consume a large amount of heat energy, the mesolow cylinder of the energy source of prior art mainly power plant steam turbine draws gas.
Solar energy is as a kind of reproducible clean energy resource, reserves are the abundantest, its developing and utilizingpotentiality is the hugest, but the intermittence of solar energy causes the instability of system, in order to ensure the reliable utilization of solar energy, it is generally required to carry out heat accumulation or the auxiliary utilization of other aid system, but the utilization of aid system increases the cost of system.
Geothermal energy is as a kind of clean energy resource, and the feature of its rich reserves is increasingly subject to the attention of more and more national, and development and utilization geothermal energy has the most far-reaching strategic importance.Simultaneously the relative stability of heat energy also becomes its big advantage utilized.
Solar energy and geothermal energy are combined with existing carbon dioxide capture system, the heat energy utilizing daytime solar energy heating to produce trapping system desorbing temperature required carries out desorbing, geothermal energy is utilized to supplement when evening and solar energy deficiency, the stable operation of trapping system can be realized, and from the power plant steam turbine energy consumption of steam pumping is greatly reduced, the double effects of regenerative resource and power plant's carbon dioxide discharge-reduction, the strong large-scale application promoting China's regenerative resource and flue gas trapping integrated technology is realized while maintaining power plant's stability.
Utility model content
Energy consumption problem and the Intermittent Features of solar energy for collecting carbonic anhydride process, the utility model proposes a kind of solar energy and geothermal energy united auxiliary carbon dioxide trapping system, make full use of the feature of solar energy and geothermal energy, it is achieved the stable operation of carbon dioxide capture system.
In order to efficiently solve technical problem above, this utility model one solar energy and geothermal energy united auxiliary carbon dioxide trapping system, including power plants generating electricity system, carbon dioxide capture system, solar thermal collection system and geothermal energy system；Described power plants generating electricity system includes defeated coal device, boiler, steam turbine, exhaust steam condenser, the first pump, low pressure return heater and high pressure backwater heater, described exhaust steam condenser, low pressure return heater are all connected with described steam turbine with high pressure backwater heater, wherein, described boiler, steam turbine, exhaust steam condenser, the first pump, low pressure return heater and high pressure backwater heater have been followed in series to form a steam generating system；Described carbon dioxide capture system includes Flue Gas Pretreatment Device, absorption tower, rich solution pump, lean/rich liquid heat exchanger, lean pump, desorber, multistage compressing device and reboiler；The exhaust opening of described boiler is connected with the entrance of described Flue Gas Pretreatment Device, and the outlet of described Flue Gas Pretreatment Device is connected to the gas access of bottom, described absorption tower；Described lean/rich liquid heat exchanger lean solution spray inlet with described lean solution delivery side of pump, the rich solution spray inlet on described desorber top, described rich solution delivery side of pump and top, described absorption tower respectively is connected；Entrance bottom described desorber entrance with the outlet of described reboiler and described lean pump respectively is connected, and the gas outlet at described desorber top is connected to the entrance of described multistage compressing device；Described solar thermal collection system is composed in series by solar energy heat-collection field, heat collecting field inlet valve, collection heat exchanger, the second pump and heat collecting field outlet valve；Described solar energy heat-collection field is made up of solar thermal collector array；Described geothermal energy system is composed in series by geothermal production, geothermal system inlet valve, filter, geothermal heat exchanger, the 3rd pump, geothermal system outlet valve and injection well；Described reboiler high temperature side fluid is divided into first and second liang of branch roads, wherein, first branch road is connected with described collection heat exchanger, second branch road is connected with geothermal heat exchanger, first branch road is provided with the first collection heat control valve (HCV) and the second collection heat control valve (HCV), and the second branch road is provided with the first ground heat control valve (HCV) and the second ground heat control valve (HCV)；In first branch road and the second branch road, working fluid after heat exchange is entered back in reboiler by the 4th pump after converging to main line.
Further, described solar thermal collector array is formed by organizing solar thermal collector series and parallel more, and the type of described solar thermal collector 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.
The thermal source of described geothermal energy system is the combination of one or more in geothermal water, deep geothermal heat fluid and xeothermic salt.
In this utility model, power plants generating electricity system can produce a large amount of containing certain density flue gas after boiler combustion, flue gas through pretreatment unit process after from entrance absorption tower at the bottom of tower, contact with the chemical absorbing liquid of tower top spray, absorb the carbon dioxide in flue gas, form rich solution, rich solution sprays desorber from tower top after rich solution pump with lean/rich liquid heat exchanger heat exchange and regenerates, heat needed for reboiler provides desorbing simultaneously, part steam is carried out condensing reflux to desorber through gas-liquid separator by the carbon dioxide desorbed, isolated carbon dioxide stores through the laggard row of overcompression.Desorb the lean solution after carbon dioxide after lean pump, lean/rich liquid heat exchanger and lean solution condenser, again spray absorption tower and form the circulation of whole absorption and desorption.
Compared with prior art, the beneficial effects of the utility model are:
(1) by low-temperature heat collection in solar energy and CO2Trapping system combines, and can make full use of middle low-temperature solar energy collecting system high collection effciency within the scope of collecting regenerated temperature, to reduce the reduction of the arresting efficiency that conventional power plants extraction high-grade energy is caused, improves system synthesis efficiency.
(2) directly utilize middle-low grade heat energy and realize the energy requirement of reboiler, it is achieved the docking of energy grade, it is to avoid tradition capture method use cooling decompression in a large number after the irreversible loss that brought of steam, cause the waste of high-grade energy.
(3) reduce original system traditional in prior art to draw gas in a large number the regeneration adverse effect to steam turbine.
(4) solar energy and geothermal energy can be well adapted for the operational mode of power plant, make full use of solar energy by day during peak of power consumption and geothermal energy realizes the energy supply of trapping system, and when night is without solar energy during low power consumption the most just, geothermal energy or the offer heat that draws gas can be utilized, to maintain operating steadily of power plant.
Accompanying drawing explanation
Fig. 1 is this utility model solar energy and geothermal energy united auxiliary carbon dioxide trapping system structural representation；
nullIn figure: 1-defeated coal device，2-boiler，3-steam turbine，4-exhaust steam condenser，5-the first pump，6-low pressure return heat exchanger，7-high pressure backwater heat exchanger，8-Flue Gas Pretreatment Device，9-absorption tower，10-rich solution pump，11-lean/rich liquid heat exchanger，12-lean pump，13-desorber，14-multistage compressing device，15-reboiler，16-geothermal production，17-geothermal system inlet valve，18-filter，19-geothermal heat exchanger，20-the 3rd pump，21-geothermal system outlet valve，22-injects well，23-the second ground heat control valve (HCV)，24-the 4th pump，25-the first ground heat control valve (HCV)，26-first collects heat control valve (HCV)，27-collection heat exchanger，28-second collects heat control valve (HCV)，29-the second pump，30-heat collecting field outlet valve，31-collector array，32-heat collecting field inlet valve.
Detailed description of the invention
Below in conjunction with detailed description of the invention, this utility model is described in further detail.
This utility model one solar energy and geothermal energy united auxiliary carbon dioxide trapping system, as it is shown in figure 1, include power plants generating electricity system, carbon dioxide capture system, solar thermal collection system and geothermal energy system.
Described power plants generating electricity system includes defeated coal device 1, boiler 2, steam turbine 3, exhaust steam condenser the 4, first pump 5, low pressure return heater 6 and high pressure backwater heater 7, described exhaust steam condenser 4, low pressure return heater 6 are all connected with described steam turbine 3 with high pressure backwater heater 7, wherein, described boiler 2, steam turbine 3, exhaust steam condenser the 4, first pump 5, low pressure return heater 6 and high pressure backwater heater 7 have been followed in series to form a steam generating system；
Described carbon dioxide capture system includes Flue Gas Pretreatment Device 8, absorption tower 9, rich solution pump 10, lean/rich liquid heat exchanger 11, lean pump 12, desorber 13, multistage compressing device 14 and reboiler 15；The exhaust opening of described boiler 2 is connected with the entrance of described Flue Gas Pretreatment Device 8, and the outlet of described Flue Gas Pretreatment Device 8 is connected to the gas access of bottom, described absorption tower 9；Flue gas after pretreatment unit 8 desulphurization denitration enters in tower from the bottom on absorption tower 9 and carries out collecting carbonic anhydride；Described lean/rich liquid heat exchanger 11 lean solution spray inlet with the outlet of described lean pump 12, the rich solution spray inlet on described desorber 13 top, the outlet of described rich solution pump 10 and top, described absorption tower 9 respectively is connected；Entrance bottom described desorber 13 is connected with the outlet of described reboiler 15 and the entrance of described lean pump 12 respectively, and the gas outlet at described desorber 13 top is connected to the entrance bottom described multistage compressing device 14, stores after multi-stage compression.
Described solar thermal collection system is composed in series by solar energy heat-collection field, heat collecting field inlet valve 32, collection heat exchanger the 27, second pump 29 and heat collecting field outlet valve 30；Described solar energy heat-collection field is made up of solar thermal collector array 31, and heat collecting field inlet valve 32 and heat collecting field outlet valve 30 are arranged in the two ends of collector array 31, plays the effect understanding collector array 31 under accident condition.Described solar thermal collector array 31 is formed by organizing solar thermal collector series and parallel more, and the type of described solar thermal collector 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.
Described geothermal energy system is composed in series by geothermal production 16, geothermal system inlet valve 17, filter 18, geothermal heat exchanger the 19, the 3rd pump 20, geothermal system outlet valve 21 and injection well 22；The thermal source of described geothermal energy system is to utilize the combination of one or more in geothermal water, deep geothermal heat fluid and xeothermic salt.The flow process of described geothermal energy system fluids within pipes is: enter geothermal heat exchanger 19 after geothermal system inlet valve 17 and filter 18 from the middle high-temperature geothermal fluid of geothermal production 16 extraction, the heat of geothermal fluid passes to the high temperature side working fluid of reboiler 15 through geothermal heat exchanger 19, and the geothermal fluid of release heat is entered by the 3rd pump 20 and geothermal system outlet valve 21 and injects in well 22；Wherein geothermal system inlet valve 17 is arranged in the outlet of geothermal production 16, geothermal system outlet valve 21 is arranged in the entrance injecting well 22, described geothermal system inlet valve 17 and geothermal system outlet valve 21, to play regulation and to control the effect of geothermal fluid flow, close down the effect of geothermal system under there are accident or abnormal conditions simultaneously.
Indirect heat exchange is carried out by working fluid between this utility model reboiler 15 and geothermal energy system and solar thermal collection system, the most described reboiler 15 high temperature side fluid is divided into first and second liang of branch roads, wherein, first branch road is connected with described collection heat exchanger 27, second branch road is connected with geothermal heat exchanger 19, first branch road is provided with the first collection heat control valve (HCV) 26 and the second collection heat control valve (HCV) 28, and the second branch road is provided with the first ground heat control valve (HCV) 25 and the second ground heat control valve (HCV) 23；The working fluid of the first branch road enters the low-temperature end of geothermal heat exchanger 19 through the first ground heat control valve (HCV) 25, and the working fluid after heat exchange heats up converges to main line, reenters the high temperature side of reboiler 15 after the 4th pump 24；The working fluid of the second branch road enters thermal-arrest heat exchanger 27 after the first collection heat control valve (HCV) 26, and the working fluid after heat exchange is entered in reboiler 15 by the 4th pump 24 after converging with the working fluid of the first branch road after the second collection heat control valve (HCV) 28.
This utility model solar energy and geothermal energy united auxiliary carbon dioxide trapping system can provide following plurality of operating modes:
When fine day solar energy abundance, close geothermal system inlet valve 17 and geothermal system outlet valve 21, close the first ground heat control valve (HCV) 25 and the second ground heat control valve (HCV) 23, open heat collecting field inlet valve 32 and heat collecting field outlet valve 30, open the first collection heat control valve (HCV) 26 and the second collection heat control valve (HCV) 28, make to carry out heat exchange from reboiler 15 high temperature side outlet working medium with the collection heat exchanger 27 solar thermal collection system.
When overcast and rainy solar energy deficiency, open geothermal system inlet valve 17 and geothermal system outlet valve 21, open heat collecting field inlet valve 32 and heat collecting field outlet valve 30, open first ground heat control valve (HCV) the 25, second ground heat control valve (HCV) 23, first simultaneously and collect heat control valve (HCV) 26 and the second collection heat control valve (HCV) 28, utilize underground heat and solar energy to provide the heat demand of reboiler 15 simultaneously.
During when night or without solar energy, close heat collecting field inlet valve 32 and heat collecting field outlet valve 30, close the first collection heat control valve (HCV) 26 and the second collection heat control valve (HCV) 28, open geothermal system inlet valve 17 and geothermal system outlet valve 21, open the first ground heat control valve (HCV) 25 and the second ground heat control valve (HCV) 23, make to carry out heat exchange from reboiler 15 high temperature side outlet working medium with the geothermal heat exchanger 19 geothermal system, provide reboiler 15 heat individually with underground heat.
To sum up, this utility model carries out the removing of carbon dioxide in power-plant flue gas by carbon dioxide capture system, during collecting carbonic anhydride, the heat needed for reboiler is provided by solar energy and geothermal energy united, by day under the conditions of solar energy abundance, reboiler heat is provided by solar thermal collection system, when solar energy deficiency or evening, reboiler institute calorific requirement is then provided by underground heat, both couplings achieve the stable operation of trapping system, reduce power plant to draw gas the decline of the output power caused, solve the drawback caused due to self-defect during renewable energy utilization, the dual effect achieving that collecting carbonic anhydride and regenerative resource reduce discharging, promote the integrated development of regenerative resource and conventional electric power system.
Although this utility model being described above in conjunction with figure; but this utility model is not limited to above-mentioned detailed description of the invention; above-mentioned detailed description of the invention is only schematically; rather than it is restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; in the case of without departing from this utility model objective, it is also possible to make many variations, within these belong to protection of the present utility model.
Claims (2)
1. solar energy and a geothermal energy united auxiliary carbon dioxide trapping system, including power plants generating electricity system, carbon dioxide capture system, solar thermal collection system and geothermal energy system；It is characterized in that:
Described power plants generating electricity system includes defeated coal device (1), boiler (2), steam turbine (3), exhaust steam condenser (4), first pump (5), low pressure return heater (6) and high pressure backwater heater (7), described exhaust steam condenser (4), low pressure return heater (6) is all connected with described steam turbine (3) with high pressure backwater heater (7), wherein, described boiler (2), steam turbine (3), exhaust steam condenser (4), first pump (5), low pressure return heater (6) and high pressure backwater heater (7) have been followed in series to form a steam generating system；
Described carbon dioxide capture system includes Flue Gas Pretreatment Device (8), absorption tower (9), rich solution pump (10), lean/rich liquid heat exchanger (11), lean pump (12), desorber (13), multistage compressing device (14) and reboiler (15)；The exhaust opening of described boiler (2) is connected with the entrance of described Flue Gas Pretreatment Device (8), and the outlet of described Flue Gas Pretreatment Device (8) is connected to the gas access of described absorption tower (9) bottom；Described lean/rich liquid heat exchanger (11) lean solution spray inlet with the outlet of described lean pump (12), the rich solution spray inlet on described desorber (13) top, the outlet of described rich solution pump (10) and described absorption tower (9) top respectively is connected；The entrance of described desorber (13) bottom is connected with the outlet of described reboiler (15) and the entrance of described lean pump (12) respectively, and the gas outlet at described desorber (13) top is connected to the entrance of described multistage compressing device (14)；
Described solar thermal collection system is composed in series by solar energy heat-collection field, heat collecting field inlet valve (32), collection heat exchanger (27), the second pump (29) and heat collecting field outlet valve (30)；Described solar energy heat-collection field is made up of solar thermal collector array (31)；
Described geothermal energy system is composed in series by geothermal production (16), geothermal system inlet valve (17), filter (18), geothermal heat exchanger (19), the 3rd pump (20), geothermal system outlet valve (21) and injection well (22)；
Described reboiler (15) high temperature side fluid is divided into first and second liang of branch roads, wherein, first branch road is connected with described collection heat exchanger (27), second branch road is connected with geothermal heat exchanger (19), first branch road is provided with the first collection heat control valve (HCV) (26) and the second collection heat control valve (HCV) (28), and the second branch road is provided with the first ground heat control valve (HCV) (25) and the second ground heat control valve (HCV) (23)；Entered back in reboiler (15) by the 4th pump (24) after in first branch road and the second branch road, working fluid after heat exchange converges to main line.
Solar energy and geothermal energy united auxiliary carbon dioxide trapping system the most according to claim 1, it is characterized in that, described solar thermal collector array (31) is formed by organizing solar thermal collector series and parallel more, and the type of described solar thermal collector 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620129921.2U CN205549977U (en) | 2016-02-19 | 2016-02-19 | Carbon dioxide capture system is jointly assisted with geothermal energy to solar energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620129921.2U CN205549977U (en) | 2016-02-19 | 2016-02-19 | Carbon dioxide capture system is jointly assisted with geothermal energy to solar energy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205549977U true CN205549977U (en) | 2016-09-07 |
Family
ID=56818208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620129921.2U Withdrawn - After Issue CN205549977U (en) | 2016-02-19 | 2016-02-19 | Carbon dioxide capture system is jointly assisted with geothermal energy to solar energy |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205549977U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105561742A (en) * | 2016-02-19 | 2016-05-11 | 天津大学 | Carbon dioxide capture system assisted by combination of solar energy and geothermal energy |
-
2016
- 2016-02-19 CN CN201620129921.2U patent/CN205549977U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105561742A (en) * | 2016-02-19 | 2016-05-11 | 天津大学 | Carbon dioxide capture system assisted by combination of solar energy and geothermal energy |
| CN105561742B (en) * | 2016-02-19 | 2018-06-08 | 天津大学 | A kind of solar energy and geothermal energy united auxiliary carbon dioxide trapping system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103752142B (en) | A kind of solar energy auxiliary carbon dioxide trapping integrated system | |
| DK2933484T3 (en) | SUPPLEMENTARY SOL-BIOMASS HEAT POWER SYSTEM | |
| CN104399356B (en) | A kind of carbon dioxide capture system | |
| CN107741103B (en) | Ammonia water absorption type refrigeration combined carbon trapping device | |
| CN104613654B (en) | Combined-type-solar-system power-plant water-feeding and CO2-collecting assisted integrated system | |
| CN204574529U (en) | The feedwater of a kind of combination type solar system supplymentary power plant and CO 2the integrated system of trapping | |
| CN110711463A (en) | Gas power plant CO based on solar energy and LNG cold energy2Trapping system | |
| CN104607001A (en) | Solar gradient phase change heat storage indirect steam assisted carbon dioxide capture system | |
| CN203803335U (en) | Multistage split regeneration carbon dioxide trapping system | |
| CN106345222A (en) | Solar thermal assisted temperature swing adsorption carbon trapping system | |
| CN106837439A (en) | The vacuum pressure and temperature varying Coupling Adsorption carbon trapping system of solar energy organic Rankine bottoming cycle auxiliary | |
| CN106076073A (en) | A kind of solar energy and the energy utility system of geothermal energy united power plant low-carbon emission | |
| CN204563877U (en) | Solar energy cascade phase-transition heat-storage indirect steam auxiliary carbon dioxide trapping system | |
| CN204337980U (en) | A kind of carbon dioxide capture device | |
| CN105561742B (en) | A kind of solar energy and geothermal energy united auxiliary carbon dioxide trapping system | |
| CN205549977U (en) | Carbon dioxide capture system is jointly assisted with geothermal energy to solar energy | |
| CN106669372B (en) | Coal-fired power plant carbon capture system driven by solar heating absorption heat pump | |
| CN105258141B (en) | The indirect thermodynamic-driven removing CO of independent solar phase transformation step accumulation of heat2System | |
| CN204582900U (en) | A kind of decarbonization system utilizing solar energy to assist reboiler to heat | |
| CN217909691U (en) | Energy-saving and water-saving carbon capture device | |
| CN217795387U (en) | Low-energy-consumption carbon trapping device | |
| CN205760478U (en) | A kind of hydrate carbon trapping system of solar photovoltaic driving | |
| CN101788141A (en) | Absorption type heat regenerator and application thereof in regenerative circulation system of power plant | |
| CN214403871U (en) | Geothermal energy power generation system based on full flow and triangular flash cycle coupling | |
| CN105251316B (en) | The direct thermodynamic-driven of independent solar utilizes mixed working fluid removing CO2System |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160907 Effective date of abandoning: 20180608 |
|
| AV01 | Patent right actively abandoned |