CN201407075Y - Carbon dioxide power take-off device with mixed heat source of solar energy and fuel energy - Google Patents
Carbon dioxide power take-off device with mixed heat source of solar energy and fuel energy Download PDFInfo
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- CN201407075Y CN201407075Y CN2009200998953U CN200920099895U CN201407075Y CN 201407075 Y CN201407075 Y CN 201407075Y CN 2009200998953 U CN2009200998953 U CN 2009200998953U CN 200920099895 U CN200920099895 U CN 200920099895U CN 201407075 Y CN201407075 Y CN 201407075Y
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- carbon dioxide
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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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
Abstract
The utility model discloses a carbon dioxide power take-off device with mixed heat source of solar energy and fuel energy, which relates to the technical fields of water conservation, energy conservation, pneumatic machinery and refrigeration, and is designed for realizing all-weather operation of the carbon dioxide power take-off device. A solar thermal collector is connected with a pipeline at the upper part of a boiler in parallel, and connected with a heat collecting chamber; the lower end of the solar thermal collector is respectively connected with two ends of a three-way electric control valve; the common terminal of the three-way valve is connected with the heat collecting chamber through a circulation pump to form a mixed heat source device; and a liquid storage tank, a preheatingtank, a high-pressure nozzle, a vaporizing chamber, an impeller mechanism, an air cooling box, a cooling tank, a compressor and accessories are connected in series by pipelines, thus forming a carbonliquid-gas and gas-liquid conversion device. The carbon dioxide power take-off device is powered by an auxiliary power system and controlled by a photo-sensor, and conducts conversion by the three-way electric control valve; with sunlight, the solar thermal collector is used, and without sunlight, the boiler is used for heating the liquid medium in the heat collecting chamber to supply heat source for the carbon dioxide power take-off device, thus realizing all-weather operation; and the carbon dioxide power take-off device is suitable for driving loads such as generators and the like.
Description
Technical field:
A kind of solar energy, fuel can mix the carbon dioxide power take-off of thermal source, relate to water saving, energy-conservation, clean energy resource, pneumatic machinery and refrigeration technology field.
Background technique:
Single solar energy carbon dioxide power take-off can lose thermal source and can't obtain power and export under no sunlight conditions such as overcast and rainy and night; Single fuel can the carbon dioxide power take-off can produce more fuel consumption, produces more discharging simultaneously.The two is carried out technology integrate, can realize water saving, energy-conservation, round-the-clock running.
Summary of the invention:
The purpose of this utility model provides the carbon dioxide power take-off that a kind of solar energy, fuel can mix thermal source, and the problem that solve is: for carbon dioxide power take-off design solar energy, fuel can the mixing thermal source, realize round-the-clock running.It is by the mixed heat source apparatus, carbon dioxide liquid-gas transfer device, carbon dioxide gas-liquid conversion equipment and secondary power system are formed: the outside of heat collecting chamber 4 is covered with thermal insulation layer, be sleeved on the vaporizing chamber 8, solar thermal collector 1 is connected in parallel in the heat collecting chamber 4 by pipeline with the top of boiler 2, threeway electrically-controlled valve 26 is leaded up to pipeline and is linked to each other with the bottom of solar thermal collector 1, another road links to each other by the bottom of pipeline with boiler 2, its common port links to each other with heat collecting chamber 4 by recycle pump 5 and pipeline thereof, fuel pot 3 links to each other with boiler 2 by light-operated valve 25, light sensor 24 is installed in solar thermal collector 1 place, be electrically connected with light-operated valve 25 and threeway electrically-controlled valve 26, constitute the mixed heat source apparatus.
Liquid container 12 links to each other with preheating can 6 by pipeline, preheating can 6 links to each other with high pressure nozzle 7 by series flow control valve 14 and pipeline thereof, high pressure nozzle 7 is installed in the input end of vaporizing chamber 8, its spout is opened in vaporizing chamber 8, the exhaust end of vaporizing chamber 8 communicates with the inlet end of impeller mechanism 9, constitutes liquid-gas transfer device.
The exhaust end of impeller mechanism 9 links to each other by the input end of pipeline with air-cooled case 10, the output terminal of air-cooled case 10 and cooling tank 11 pass through pipeline connection, the outside of cooling tank 11 is covered with thermal insulation layer, link to each other by the inlet end of pipeline with air compressor 13, the exhaust end of air compressor 13 links to each other with liquid container 12 by one-way valve and pipeline thereof; Vaporizer 18 is installed in the cooling tank 11, the one end links to each other with the input end of refrigeration compressor 15, the other end links to each other with flow controller 17, condenser 16 installs around the outside at preheating can 6, one end links to each other with flow controller 17, the other end links to each other with the output terminal of refrigeration compressor 15, constitutes carbon dioxide gas-liquid conversion equipment.
Solar thermal collector 1, boiler 2, threeway electrically-controlled valve 26, heat collecting chamber 4 constitute the closed circulation loop with recycle pump 5 and pipeline thereof, wherein are full of the liquid medium of high-low temperature resistant.
Be full of liquid carbon dioxide in the gas holder 12, from liquid container 12, through preheating can 6, series flow control valve 14, high pressure nozzle 7, vaporizing chamber 8, impeller mechanism 9, air-cooled case 10, air compressor 13 and one-way valve, return liquid container 12, together with the pipeline separately of member, constitute the closed circulation loop of liquid-mist-gas-liquid conversion of carbon dioxide.
The utility model for the carbon dioxide power take-off designed solar energy, fuel can the mixing thermal source, make it not only save water, low energy consumption, all-weather operation is gone back in low emission, is fit to drive the generator even load and uses.
Description of drawings:
Fig. 1: the utility model schematic diagram.
Fig. 2: the utility model electrical schematic diagram.
Among the figure: 1, solar thermal collector, 2, boiler, 3, fuel pot, 4, heat collecting chamber, 5, recycle pump, 6, preheating can, 7, high pressure nozzle, 8, vaporizing chamber, 9, impeller mechanism, 10, air-cooled case, 11, cooling tank, 12, liquid container, 13, air compressor, 14, series flow control valve, 15, refrigeration compressor, 16, condenser, 17, flow controller, 18, vaporizer, 19, generator, 20, the air compressor motor, 21, refrigeration compressor motor, 22, circulating pump motor, 23, blower fan, 24, light sensor, 25, light-operated valve, 26, the threeway electrically-controlled valve, 27, power source regulating circuit, 28, storage battery.
Embodiment:
In conjunction with Fig. 1 structure of the present utility model and mode of execution are described: heat collecting chamber 4 is sleeved on the vaporizing chamber 8, solar thermal collector 1 is connected in parallel in the heat collecting chamber 4 by pipeline with boiler 2, threeway electrically-controlled valve 26 is leaded up to pipeline and is linked to each other with solar thermal collector 1, another road links to each other with boiler 2 by pipeline, its common port links to each other with heat collecting chamber 4 by recycle pump 5 and pipeline thereof, fuel pot 3 links to each other with boiler 2 by light-operated valve 25, light sensor 24 is installed in solar thermal collector 1 place, be electrically connected with light-operated valve 25 and threeway electrically-controlled valve 26, constitute the mixed heat source apparatus.Light-operated valve 25 and threeway electrically-controlled valve 26 are linkage, are controlled by light sensor 24.When solar irradiation was sufficient, threeway electrically-controlled valve 26 was connected solar thermal collector 1 and recycle pump 5, and liquid medium is heated in solar thermal collector 1, by the circulation of recycle pump 5, with heat exchange in heat collecting chamber 4; When sunlight was not enough, light control system started the fuel-device of boiler 2 automatically, and simultaneously, threeway electrically-controlled valve 26 is connected boiler 2 and recycle pump 5, liquid medium in boiler 2 by the fuel heating, by recycle pump 5 with heat exchange in heat collecting chamber 4.
Liquid container 12 links to each other with preheating can 6 by pipeline, preheating can 6 links to each other with high pressure nozzle 7 by series flow control valve 14 and pipeline thereof, high pressure nozzle 7 is installed in the input end of vaporizing chamber 8, its spout is opened in vaporizing chamber 8, the exhaust end of vaporizing chamber 8 communicates with the inlet end of impeller mechanism 9, constitutes liquid-gas transfer device.When the utility model starts, open series flow control valve 14, liquid carbon dioxide is just sprayed in the gasification room 8 with vaporific by high pressure nozzle 7, the heat energy in absorbing sets hot cell 4, and gasification is expanded, and promotes the impeller rotation work done of impeller mechanism 9, drives load operation.
The exhaust end of impeller mechanism 9 links to each other by the input end of pipeline with air-cooled case 10, the output terminal of air-cooled case 10 and cooling tank 11 pass through pipeline connection, cooling tank 11 links to each other by the inlet end of pipeline with air compressor 13, and the exhaust end of air compressor 13 links to each other with liquid container 12 by one-way valve and pipeline thereof; Vaporizer 18 is installed in the cooling tank 11, the one end links to each other with the input end of refrigeration compressor 15, the other end links to each other with flow controller 17, condenser 16 installs around the outside at preheating can 6, one end links to each other with flow controller 17, the other end links to each other with the output terminal of refrigeration compressor 15, constitutes carbon dioxide gas-liquid conversion equipment.Carbon dioxide after the work done enters in the air-cooled case 10 by the road, by blower fan 23 it is carried out air-cooledly, implements the first step and cools.Carbon dioxide after air-cooled enters in the cooling tank 11, vaporizer 18 carries out strong cold cooling to it, through the volume of the carbon dioxide after the cold cooling of cooling tank the last 11 much smaller than the volume when impeller mechanism 9 is discharged, therefore, the gas flow that the gas flow of process air compressor 13 is discharged much smaller than impeller mechanism 9, air compressor 13 can be less pressure will be pressed into the reduction of liquefying in the liquid container 12 through one-way valve by the gas of the cold cooling of cooling tank the last 11.
Vaporizer 18 is installed in the cooling tank 11, to reduce energy loss, guarantees refrigerating efficiency.Condenser 16 installs around in the outside of preheating can 6, and the heat that cooling tank 11 can be exchanged when the cooled carbon dioxide gas heats the liquid carbon dioxide that enters in the preheating can 6.
Claims (5)
1, a kind of solar energy, fuel can mix the carbon dioxide power take-off of thermal source, it is by the mixed heat source apparatus, carbon dioxide liquid-gas transfer device, carbon dioxide gas-liquid conversion equipment and secondary power system are formed, it is characterized in that: heat collecting chamber (4) is sleeved on the vaporizing chamber (8), the top of the same boiler of solar thermal collector (1) (2) is connected in parallel in the heat collecting chamber (4) by pipeline, threeway electrically-controlled valve (26) is leaded up to pipeline and is linked to each other with the bottom of solar thermal collector (1), another road links to each other by the bottom of pipeline with boiler (2), its common port links to each other with heat collecting chamber (4) by recycle pump (5) and pipeline thereof, fuel pot (3) links to each other with boiler (2) by light-operated valve (25), light sensor (24) is installed in solar thermal collector (1) and locates, be electrically connected with light-operated valve (25) and threeway electrically-controlled valve (26), constitute the mixed heat source apparatus; Liquid container (12) links to each other with preheating can (6) by pipeline, preheating can (6) links to each other with high pressure nozzle (7) by series flow control valve (14) and pipeline thereof, high pressure nozzle (7) is installed in the input end of vaporizing chamber (8), its spout is opened in vaporizing chamber (8), the exhaust end of vaporizing chamber (8) communicates with the inlet end of impeller mechanism (9), constitutes liquid-gas transfer device; The exhaust end of impeller mechanism (9) links to each other by the input end of pipeline with air-cooled case (10), the output terminal of air-cooled case (10) and cooling tank (11) pass through pipeline connection, cooling tank (11) links to each other by the inlet end of pipeline with air compressor (13), the exhaust end of air compressor (13) links to each other with liquid container (12) by one-way valve and pipeline thereof, vaporizer (18) one ends link to each other with the input end of refrigeration compressor (15), the other end links to each other with flow controller (17), condenser (16) one ends link to each other with flow controller (17), the other end links to each other with the output terminal of refrigeration compressor (15), constitutes carbon dioxide gas-liquid conversion equipment; Generator (19) is installed on the pto of impeller mechanism (9), air compressor motor (20) is coaxial to be installed on the air compressor (13), refrigeration compressor motor (21) is installed in the refrigeration compressor (15), circulating pump motor (22) is installed on the recycle pump (5), blower fan (23) is installed on the air-cooled case (10), storage battery (28) is electrically connected with power source regulating circuit (27), one end of power source regulating circuit (27) is electrically connected with generator (19), the other end respectively with air compressor motor (20), refrigeration compressor motor (21), circulating pump motor (22), blower fan (23), light-operated valve (25) and threeway electrically-controlled valve (26) are electrically connected, and form secondary power system.
2, solar energy according to claim 1, fuel can mix the carbon dioxide power take-off of thermal source, it is characterized in that: solar thermal collector (1), boiler (2), threeway electrically-controlled valve (26), heat collecting chamber (4) constitute the closed circulation loop with the pipeline that recycle pump (5) passes through separately, wherein fill the liquid medium of high-low temperature resistant.
3, solar energy according to claim 1, fuel can mix the carbon dioxide power take-off of thermal source, it is characterized in that: be full of liquid carbon dioxide in the gas holder (12), from liquid container (12), through preheating can (6), series flow control valve (14), high pressure nozzle (7), vaporizing chamber (8), impeller mechanism (9), air-cooled case (10), air compressor (13) and one-way valve, return liquid container (12), together with the pipeline separately of member, constitute the closed circulation loop of liquid-mist-gas-liquid conversion of carbon dioxide.
4, solar energy according to claim 1, fuel can mix the carbon dioxide power take-off of thermal source, it is characterized in that: vaporizer (18) is installed in the cooling tank (11); Condenser (16) installs around the outside in preheating can (6).
5, solar energy according to claim 1, fuel can mix the carbon dioxide power take-off of thermal source, it is characterized in that: the outside of heat collecting chamber (4), cooling tank (11) is covered with thermal insulation layer.
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CN2009200998953U CN201407075Y (en) | 2009-05-20 | 2009-05-20 | Carbon dioxide power take-off device with mixed heat source of solar energy and fuel energy |
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CN2009200998953U CN201407075Y (en) | 2009-05-20 | 2009-05-20 | Carbon dioxide power take-off device with mixed heat source of solar energy and fuel energy |
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Cited By (7)
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CN103737882A (en) * | 2013-12-20 | 2014-04-23 | 昆山易昌泰塑胶有限公司 | Improved temperature control device of quick cooling and heating die |
CN103912404A (en) * | 2014-04-30 | 2014-07-09 | 郭远军 | Parallel motion high-low pressure power device and application thereof |
CN103912406A (en) * | 2014-04-30 | 2014-07-09 | 郭远军 | Heat energy power machine and working method thereof |
CN103925107A (en) * | 2014-04-30 | 2014-07-16 | 郭远军 | Heat energy power equipment and work doing method thereof |
CN103939232A (en) * | 2014-04-30 | 2014-07-23 | 郭远军 | Horizontally opposed type high and low pressure power device and working method thereof |
CN104114821A (en) * | 2011-12-22 | 2014-10-22 | 迪尔曼发动机有限公司 | Improved cryogenic engine system |
CN115307334A (en) * | 2022-08-08 | 2022-11-08 | 安徽工程大学 | Multi-heat-source heat pump air conditioning system and operation control method thereof |
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2009
- 2009-05-20 CN CN2009200998953U patent/CN201407075Y/en not_active Expired - Fee Related
Cited By (11)
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CN104114821A (en) * | 2011-12-22 | 2014-10-22 | 迪尔曼发动机有限公司 | Improved cryogenic engine system |
CN104114821B (en) * | 2011-12-22 | 2016-02-10 | 迪尔曼发动机有限公司 | The cryogenic engine system improved |
US9388711B2 (en) | 2011-12-22 | 2016-07-12 | Dearman Engine Company Ltd. | Cryogenic engine system |
CN103737882A (en) * | 2013-12-20 | 2014-04-23 | 昆山易昌泰塑胶有限公司 | Improved temperature control device of quick cooling and heating die |
CN103912404A (en) * | 2014-04-30 | 2014-07-09 | 郭远军 | Parallel motion high-low pressure power device and application thereof |
CN103912406A (en) * | 2014-04-30 | 2014-07-09 | 郭远军 | Heat energy power machine and working method thereof |
CN103925107A (en) * | 2014-04-30 | 2014-07-16 | 郭远军 | Heat energy power equipment and work doing method thereof |
CN103939232A (en) * | 2014-04-30 | 2014-07-23 | 郭远军 | Horizontally opposed type high and low pressure power device and working method thereof |
CN103925107B (en) * | 2014-04-30 | 2015-07-01 | 郭远军 | Heat energy power equipment and work doing method thereof |
CN115307334A (en) * | 2022-08-08 | 2022-11-08 | 安徽工程大学 | Multi-heat-source heat pump air conditioning system and operation control method thereof |
CN115307334B (en) * | 2022-08-08 | 2024-01-26 | 安徽工程大学 | Multi-heat source heat pump air conditioning system and operation control method thereof |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100217 Termination date: 20150520 |
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EXPY | Termination of patent right or utility model |