CN106884179A - A kind of electrolysis of water steam device based on groove type solar - Google Patents
A kind of electrolysis of water steam device based on groove type solar Download PDFInfo
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- CN106884179A CN106884179A CN201510936452.5A CN201510936452A CN106884179A CN 106884179 A CN106884179 A CN 106884179A CN 201510936452 A CN201510936452 A CN 201510936452A CN 106884179 A CN106884179 A CN 106884179A
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S20/00—Solar heat collectors specially adapted for particular uses or environments
- F24S20/20—Solar heat collectors for receiving concentrated solar energy, e.g. receivers for solar power plants
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/50—Processes
- C25B1/55—Photoelectrolysis
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
- F24S10/40—Solar heat collectors using working fluids in absorbing elements surrounded by transparent enclosures, e.g. evacuated solar collectors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S10/00—Solar heat collectors using working fluids
- F24S10/70—Solar heat collectors using working fluids the working fluids being conveyed through tubular absorbing conduits
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S23/00—Arrangements for concentrating solar-rays for solar heat collectors
- F24S23/70—Arrangements for concentrating solar-rays for solar heat collectors with reflectors
- F24S23/71—Arrangements for concentrating solar-rays for solar heat collectors with reflectors with parabolic reflective surfaces
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S90/00—Solar heat systems not otherwise provided for
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02S—GENERATION OF ELECTRIC POWER BY CONVERSION OF INFRARED RADIATION, VISIBLE LIGHT OR ULTRAVIOLET LIGHT, e.g. USING PHOTOVOLTAIC [PV] MODULES
- H02S40/00—Components or accessories in combination with PV modules, not provided for in groups H02S10/00 - H02S30/00
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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
- Y02E10/44—Heat exchange systems
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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
- Y02E10/50—Photovoltaic [PV] energy
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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Abstract
The present invention discloses a kind of electrolysis of water steam device based on groove type solar, including feed pump, groove type solar heat utilization subsystem, DC/DC converters, photovoltaic array, battery, oxygen storage device, oxygen separator, electrolytic cell reactor, hydrogen reservoir, hydrogen gas segregator.Water is pumped into groove type solar heat utilization subsystem by feed pump, and water is heated to be into high-temperature vapor, is obtained high-temperature vapor and is delivered to electrolytic cell reactor, and the electric energy required for the electrolytic cell and auxiliary heater of electrolytic cell reactor comes from photovoltaic array or battery.The cathode side of electrolytic cell reactor obtains hydrogen and does not participate in the vapor of reaction, and after hydrogen reservoir is by Hydrogen Separation, in storage and hydrogen reservoir, the high-temperature vapor not participated in is returned in slot type solar thermal utilization subsystem.Electrolytic cell reactor anode-side obtains oxygen and does not participate in the air of reaction, and after dual disposal gas enters oxygen separator, oxygen is separated, and in storage and oxygen storage device, air returning air import.Water is heated into high-temperature vapor using slot light collection solar energy, solar energy power generating is recycled, high-temperature vapor is electrolysed, hydrogen and oxygen is obtained.
Description
Technical field
The present invention relates to a kind of electrolysis of water steam device based on groove type solar, the electric energy electrolysis high-temperature vapor of high-temperature vapor, photovoltaic generation is specifically produced using groove type solar, belong to technical field of new energy utilization.
Background technology
The energy of hydrogen cleaning, a kind of system by high-temperature electrolysis vapor preparing hydrogen, more than 90%, this set low energy consumption, high-performance hydrogen generating system are expected to reduce hydrogen manufacturing cost hydrogen production rate, are that new road is opened up in industrial hydrogen and hydrogen energy source production.
Hydrogen can be produced by modes such as methane reforming, electrolysis waters.Although methane reforming hydrogen manufacturing low cost, complex process is big to fossil energy consumption amount, and can produce great amount of carbon dioxide；And water electrolysis hydrogen production, although process is easy, cost is but very high.
The new energy technology Creative Lab of Commissariat A L'Energie Atomique subordinate designs a high-temperature electrolysis system, and under 700 degrees Celsius of operating temperature, electrolysis temperature is that 150 degrees Celsius of vapor carrys out hydrogen making, and production rate is more than 90%.System can also be reclaimed the heat that gas is discharged in production process, for system heating.This achievement proves that, by maximally utilizing the heat energy in system, low temperature heat energy can be provided for hydrogen making, and realize gratifying production rate high.
It is introduced that, the system compact appearance, overall volume is similar to a refrigerator, and the hydrogen of 1 to 2.5 standard cubic meter can be produced per hour.Not only cost is not high in itself for system, and running cost is also extremely limited, and the hydrogen for often producing 1 standard cubic meter only consumes 3.9 degree of electricity.
Hydrogen is the important raw material of industry, is widely used in the numerous areas such as Ferrous Metallurgy, glass processing, agricultural food product processing；Meanwhile, used as a kind of fuel, hydrogen has the characteristics of pollution-free, renewable, energy density high, convenient storage and transport, is considered as one of optimal clean energy resource.
Solar energy enriches very much, and is readily obtained, pollution-free.Current solar utilization technique mainly has solar energy utilization technique and solar photovoltaic technology.But due to the unstability of solar energy, large-scale Application of Solar Energy also there are problems that many at present.
The content of the invention
Goal of the invention：For the problem and shortage of above-mentioned existing hydrogen producing technology, it is an object of the invention to provide a kind of electrolysis of water steam device based on groove type solar, using solar energy, H2O can be efficiently converted into O2 and H2.
Technical scheme：A kind of electrolysis of water steam device based on groove type solar, including feed pump（1）, groove type solar heat utilization subsystem（2）, DC/DC converters（3）, photovoltaic array（4）, battery（5）, oxygen storage device（6）, oxygen separator（7）, electrolytic cell reactor（8）, hydrogen reservoir（9）, hydrogen gas segregator（10）.Wherein, groove type solar heat utilization subsystem（2）Including condenser（2-1）, vacuum heat collection pipe（2-2）, supporting mechanism（2-3）, drive follower（2-4）, electrolytic cell reactor（8）Including electrolysis heap（8-1）, auxiliary heating（8-2）.
The feed pump（1）Water is pumped into solar thermal utilization subsystem（2）Vacuum heat collection pipe（2-2）Entrance point, vacuum heat collection pipe（2-2）The high-temperature vapor of the port of export and electrolytic cell reactor（7）Air inlet port connection.
Electrolytic cell reactor（8）Cathode side：Electrolytic cell reactor（8）Air outlet and hydrogen gas segregator（10）Input port connection, hydrogen gas segregator（10）There are two delivery outlets, hydrogen gas segregator（10）Delivery outlet one is hydrogen gas outlet, with hydrogen reservoir（9）Input connection, hydrogen gas segregator（10）Delivery outlet two is vapor delivery outlet, with vacuum heat collection pipe（2-2）Input connection.
Electrolytic cell reactor（8）Anode-side：It is air to be input into, and is exported and oxygen separator（7）Input connection, oxygen separator（7）Output point two-way, output one is oxygen output, with oxygen storage device（6）Input connection, output two be air output, be connected with air-in.
The photovoltaic array（4）Generate electricity output respectively with DC/DC converters（3）And battery（5）Input connection, battery（5）Output and DC/DC converters（3）Input connection, DC/DC converters（3）With battery（5）In parallel form, DC/DC converters（3）There is two-way to export, DC/DC converters（3）Output one and electrolytic cell（7-1）Supply port is connected, DC/DC converters（3）Output two and auxiliary heater（7-2）Supply port connection.
A kind of electrolysis of water steam device based on groove type solar, it is characterised in that electrolytic cell reactor（8）Including electrolytic cell（8-1）And auxiliary heater（8-2）.
Auxiliary heater（8-2）Energy source in photovoltaic array（4）, electrolytic cell（8-1）Electric energy equally derive from photovoltaic array（4）, electrolytic cell（8-1）On the one hand required heat energy come from high-temperature gas mixture body, on the one hand from auxiliary heater（8-2）.
The feed pump（1）Water is pumped into groove type solar heat utilization subsystem（2）In, cold water is in solar thermal utilization subsystem（2）High-temperature vapor is converted to after middle heating.
The groove type solar heat utilization subsystem（2）It is that water will be heated after Salar light-gathering, including condenser（2-1）, vacuum heat collection pipe（2-2）, supporting mechanism（2-3）, drive follower（2-4）, condenser（2-1）It is to be made up of the minute surface of parabolic shape, for reflected sunlight, focal line is in vacuum heat collection pipe（2-2）Place, vacuum heat collection pipe（2-2）For absorbing solar energy, supporting mechanism（2-3）Support condenser（2-1）With vacuum heat collection pipe（2-2）, drive follower（2-4）It is mainly used in solar energy tracking, mainly has hydraulic-driven and drive mechanism to constitute.
The DC/DC converters（3）For by photovoltaic array（4）Direct current energy of the transformation of electrical energy of generation required for system, including electrolytic cell（8-1）And auxiliary heater（8-2）Required electric energy.
The photovoltaic array（4）For solar energy to be converted directly into electric energy, it is made up of monocrystalline silicon or polysilicon photovoltaic cells, the electric energy of output is directly fed to DC/DC converters（3）Or battery（5）.
The battery（5）It is to be made up of lead-acid accumulator or maintenance-free battery etc., for storing photovoltaic array（4）Dump energy, or in the case of sunlight is insufficient, give electrolytic cell reactor（8）.
The oxygen storage device（6）It is to be made up of high pressure oxygen storage device, for the oxygen that stocking system is produced.
The oxygen separator（7）For separating air and oxygen, pure oxygen is obtained, be stored in oxygen storage device（6）In.
The electrolytic cell reactor（8）Including electrolytic cell（8-1）And auxiliary heater（8-2）.Electrolytic cell（8-1）For being electrolysed high-temperature vapor, hydrogen and oxygen are produced.Auxiliary heater（8-2）For by electrolytic cell（8-1）Operating temperature is heated to, and is maintained in this temperature, a kind of operating temperature of the electrolysis of water steam device based on groove type solar of the invention is 500 degree.
The hydrogen reservoir（9）It is made up of high pressure hydrogen storage device, for the hydrogen that stocking system is produced.
The hydrogen gas segregator（10）It is, for separating hydrogen and vapor, because there is part high-temperature vapor not participate in cell reaction, exclusion to be mixed with hydrogen.
Beneficial effect：Compared with prior art, the present invention has advantages below.
（1）Heat energy and electric energy, clean run are provided using solar energy.
（2）H2O is efficiently converted to O2 and H2, Hydrogen Energy is solved the problems, such as.
（3）Running temperature is low, about 500 degree, making material low cost, reliable, and traditional high-temp solid oxidization electrolysis pond running temperature is 900 degree.
（4）Low-temperature solid oxidization electrolysis pond is obtained using nanometer composite technology, and combines China's rare earth resources, the autonomous new high-tech industry of China can be developed.
（5）Modularized design is capable of achieving, according to different users, different installed capacitys can be designed.
Brief description of the drawings,Fig. 1 is structural representation of the invention
In figure：1 it is feed pump, 2 be groove type solar heat utilization subsystem, 3 be DC/DC converters, 4 be photovoltaic array, 5 be battery, 6 be oxygen storage device, 7 be oxygen separator, 8 be electrolytic cell reactor, 9 be hydrogen reservoir, 10 is hydrogen gas segregator.
Fig. 2 is groove type solar heat utilization subsystem schematic diagram
In figure：2-1 is that condenser, 2-2 are that vacuum heat collection pipe, 2-3 are that supporting mechanism, 2-4 are to drive follower.
Fig. 3 is electrolytic cell reactor structure figure.
In figure：8-1 is that electrolytic cell, 8-2 are auxiliary heaters.
Specific embodiment,Reference picture 1, Fig. 2 and Fig. 3, a kind of electrolysis of water steam device based on groove type solar, including feed pump（1）, groove type solar heat utilization subsystem（2）, DC/DC converters（3）, photovoltaic array（4）, battery（5）, oxygen storage device（6）, oxygen separator（7）, electrolytic cell reactor（8）, hydrogen reservoir（9）, hydrogen gas segregator（10）.Wherein, groove type solar heat utilization subsystem（2）Including condenser（2-1）, vacuum heat collection pipe（2-2）, supporting mechanism（2-3）, drive follower（2-4）, electrolytic cell reactor（8）Including electrolysis heap（8-1）, auxiliary heating（8-2）；
The feed pump（1）Water is pumped into solar thermal utilization subsystem（2）Vacuum heat collection pipe（2-2）Entrance point, vacuum heat collection pipe（2-2）The high-temperature vapor of the port of export and electrolytic cell reactor（7）Air inlet port connection；
Electrolytic cell reactor（8）Cathode side：Electrolytic cell reactor（8）Air outlet and hydrogen gas segregator（10）Input port connection, hydrogen gas segregator（10）There are two delivery outlets, hydrogen gas segregator（10）Delivery outlet one is hydrogen gas outlet, with hydrogen reservoir（9）Input connection, hydrogen gas segregator（10）Delivery outlet two is vapor delivery outlet, with vacuum heat collection pipe（2-2）Input connection.
Electrolytic cell reactor（8）Anode-side：It is air to be input into, and is exported and oxygen separator（7）Input connection, oxygen separator（7）Output point two-way, output one is oxygen output, with oxygen storage device（6）Input connection, output two be air output, be connected with air-in.
The photovoltaic array（4）Generate electricity output respectively with DC/DC converters（3）And battery（5）Input connection, battery（5）Output and DC/DC converters（3）Input connection, DC/DC converters（3）With battery（5）In parallel form, DC/DC converters（3）There is two-way to export, DC/DC converters（3）Output one and electrolytic cell（7-1）Supply port is connected, DC/DC converters（3）Output two and auxiliary heater（7-2）Supply port connection.
A kind of electrolysis of water steam device based on groove type solar, it is characterised in that electrolytic cell reactor（8）Including electrolytic cell（8-1）And auxiliary heater（8-2）.
Auxiliary heater（8-2）Energy source in photovoltaic array（4）, electrolytic cell（8-1）Electric energy equally derive from photovoltaic array（4）, electrolytic cell（8-1）On the one hand required heat energy come from high-temperature gas mixture body, on the one hand from auxiliary heater（8-2）.
Operation principle：Using above-mentioned technical proposal, when there is sunlight, start the device, feed pump（1）Water is pumped into groove type solar heat utilization subsystem（2）, water is heated to be high-temperature vapor using solar energy, obtain high-temperature vapor and deliver to electrolytic cell reactor（8）, electrolytic cell reactor（8）Electrolytic cell（8-1）And auxiliary heater（8-2）Required electric energy comes from DC/DC converters（3）, DC/DC converters（3）Electric energy come from photovoltaic array（4）Or battery（5）, so in electrolytic cell reactor（8）Negative electrode and anode will chemically react, and obtain corresponding gas
Electrolytic cell reactor（8）Cathode side：Obtain H2 and do not participate in the vapor of reaction, by hydrogen reservoir（10）After Hydrogen Separation, store and hydrogen reservoir（9）In, the high-temperature vapor not participated in returns to slot type solar thermal utilization subsystem（2）In.
Electrolytic cell reactor（8）Anode-side can directly obtain and oxygen and not participate in the air of reaction, dual disposal gas enters oxygen separator（7）Afterwards, oxygen is separated, and is stored and oxygen storage device（6）In, air returning air import.
H2O is so heated into high-temperature vapor using slot light collection solar energy, solar energy power generating is recycled, high-temperature vapor is electrolysed, H2 and O2 is obtained.
The foregoing is only better embodiment of the invention; protection scope of the present invention is not limited with above-mentioned implementation method; in every case those of ordinary skill in the art are made according to disclosed content equivalent modification or change, should all include in the protection domain described in claims.
Claims (2)
1. a kind of electrolysis of water steam device based on groove type solar, including feed pump（1）, groove type solar heat utilization subsystem（2）, DC/DC converters（3）, photovoltaic array（4）, battery（5）, oxygen storage device（6）, oxygen separator（7）, electrolytic cell reactor（8）, hydrogen reservoir（9）, hydrogen gas segregator（10）；
Wherein, groove type solar heat utilization subsystem（2）Including condenser（2-1）, vacuum heat collection pipe（2-2）, supporting mechanism（2-3）, drive follower（2-4）, electrolytic cell reactor（8）Including electrolysis heap（8-1）, auxiliary heating（8-2）；
The feed pump（1）Water is pumped into groove type solar heat utilization subsystem（2）Vacuum heat collection pipe（2-2）Entrance point, vacuum heat collection pipe（2-2）The high-temperature vapor of the port of export and electrolytic cell reactor（8）Air inlet port connection；
Electrolytic cell reactor（8）Cathode side：
Electrolytic cell reactor（8）Air outlet and hydrogen gas segregator（10）Input port connection, hydrogen gas segregator（10）There are two delivery outlets, hydrogen gas segregator（10）Delivery outlet one is hydrogen gas outlet, with hydrogen reservoir（9）Input connection, hydrogen gas segregator（10）Delivery outlet two is vapor delivery outlet, with vacuum heat collection pipe（2-2）Input connection；
Electrolytic cell reactor（8）Anode-side：
It is air to be input into, and is exported and oxygen separator（7）Input connection, oxygen separator（7）Output point two-way, output one is oxygen output, with oxygen storage device（6）Input connection, output two be air output, be connected with air-in；
The photovoltaic array（4）Generate electricity output respectively with DC/DC converters（3）And battery（5）Input connection, battery（5）Output and DC/DC converters（3）Input connection, DC/DC converters（3）With battery（5）In parallel form, DC/DC converters（3）There is two-way to export, DC/DC converters（3）Output one and electrolytic cell（7-1）Supply port is connected, DC/DC converters（3）Output two and auxiliary heater（7-2）Supply port connection.
2. a kind of electrolysis of water steam device based on groove type solar according to right 1, it is characterised in that electrolytic cell reactor（8）Including electrolytic cell（8-1）And auxiliary heater（8-2）；
Auxiliary heater（8-2）Energy source in photovoltaic array（4）, electrolytic cell（8-1）Electric energy equally derive from photovoltaic array（4）, electrolytic cell（8-1）On the one hand required heat energy come from high-temperature gas mixture body, on the one hand from auxiliary heater（8-2）.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE1026169B1 (en) * | 2018-09-18 | 2019-10-23 | AGOC bvba | Energy extraction systems |
| CN110762852A (en) * | 2019-09-12 | 2020-02-07 | 宁波大学 | A vacuum straight-through heat collector tube for hydrogen production by trough concentrating heat collecting and electrolysis |
| CN110762853A (en) * | 2019-09-12 | 2020-02-07 | 宁波大学 | Solar heat collecting tube for high-temperature electrolytic hydrogen production |
| CN110923738A (en) * | 2019-12-02 | 2020-03-27 | 中国科学院上海应用物理研究所 | A device and method for producing hydrogen by electrolysis of seawater at high temperature |
| CN113463113A (en) * | 2021-07-23 | 2021-10-01 | 浙江工业大学 | Photovoltaic and chemical heat pump coupled solar high-temperature water electrolysis hydrogen production system and process |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100230272A1 (en) * | 2007-11-14 | 2010-09-16 | Fidel Franco Gonzalez | Method and apparatus for using hydrogen |
| US20140194539A1 (en) * | 2013-01-04 | 2014-07-10 | Saudi Arabian Oil Company | Carbon dioxide conversion to hydrocarbon fuel via syngas production cell harnessed from solar radiation |
| CN104204303A (en) * | 2012-03-26 | 2014-12-10 | 通用电气公司 | Systems and methods for generating oxygen and hydrogen for plant equipment |
| CN104593803A (en) * | 2015-01-15 | 2015-05-06 | 东北石油大学 | A solar-driven high-temperature electrolysis CO2/H2O synthesis gas system and its application |
-
2015
- 2015-12-16 CN CN201510936452.5A patent/CN106884179A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100230272A1 (en) * | 2007-11-14 | 2010-09-16 | Fidel Franco Gonzalez | Method and apparatus for using hydrogen |
| CN104204303A (en) * | 2012-03-26 | 2014-12-10 | 通用电气公司 | Systems and methods for generating oxygen and hydrogen for plant equipment |
| US20140194539A1 (en) * | 2013-01-04 | 2014-07-10 | Saudi Arabian Oil Company | Carbon dioxide conversion to hydrocarbon fuel via syngas production cell harnessed from solar radiation |
| CN104593803A (en) * | 2015-01-15 | 2015-05-06 | 东北石油大学 | A solar-driven high-temperature electrolysis CO2/H2O synthesis gas system and its application |
Non-Patent Citations (4)
| Title |
|---|
| HOUCHENG ZHANG等: "Configuration design and performance optimum analysis of a solar-driven high temperature steam electrolysis system for hydrogen production", 《INTERNATIONAL JOURNAL OF HYDROGEN ENERGY》 * |
| J. PADIN等: "Hybrid solar high-temperature hydrogen production system", 《INTERNATIONAL JOURNAL OF HYDROGEN ENERGY》 * |
| STUART LICHT: "Solar water splitting to generate hydrogen fuel—a photothermal electrochemical analysis", 《INTERNATIONAL JOURNAL OF HYDROGEN ENERGY》 * |
| 黄志刚等: "太阳能高温电解水蒸气制氢系统热力学分析", 《工程热物理学报》 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE1026169B1 (en) * | 2018-09-18 | 2019-10-23 | AGOC bvba | Energy extraction systems |
| CN110762852A (en) * | 2019-09-12 | 2020-02-07 | 宁波大学 | A vacuum straight-through heat collector tube for hydrogen production by trough concentrating heat collecting and electrolysis |
| CN110762853A (en) * | 2019-09-12 | 2020-02-07 | 宁波大学 | Solar heat collecting tube for high-temperature electrolytic hydrogen production |
| CN110762853B (en) * | 2019-09-12 | 2020-11-17 | 宁波大学 | Solar heat collecting tube for high-temperature electrolytic hydrogen production |
| CN110762852B (en) * | 2019-09-12 | 2021-03-09 | 宁波大学 | A vacuum straight-through heat collector tube for hydrogen production by trough concentrating heat collecting and electrolysis |
| CN110923738A (en) * | 2019-12-02 | 2020-03-27 | 中国科学院上海应用物理研究所 | A device and method for producing hydrogen by electrolysis of seawater at high temperature |
| CN110923738B (en) * | 2019-12-02 | 2021-02-05 | 中国科学院上海应用物理研究所 | Device and method for preparing hydrogen by electrolyzing seawater at high temperature |
| CN113463113A (en) * | 2021-07-23 | 2021-10-01 | 浙江工业大学 | Photovoltaic and chemical heat pump coupled solar high-temperature water electrolysis hydrogen production system and process |
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Application publication date: 20170623 |