CN207166137U - A kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production - Google Patents
A kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production Download PDFInfo
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- CN207166137U CN207166137U CN201720611562.9U CN201720611562U CN207166137U CN 207166137 U CN207166137 U CN 207166137U CN 201720611562 U CN201720611562 U CN 201720611562U CN 207166137 U CN207166137 U CN 207166137U
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 223
- 239000001257 hydrogen Substances 0.000 title claims abstract description 220
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 220
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 148
- 239000007789 gas Substances 0.000 title claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 84
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 71
- 230000005611 electricity Effects 0.000 claims abstract description 50
- 239000007787 solid Substances 0.000 claims abstract description 39
- 230000033228 biological regulation Effects 0.000 claims abstract description 33
- 239000007864 aqueous solution Substances 0.000 claims abstract description 13
- 229920000642 polymer Polymers 0.000 claims abstract description 12
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 11
- 239000003245 coal Substances 0.000 claims abstract description 10
- 230000006698 induction Effects 0.000 claims abstract description 4
- 239000000446 fuel Substances 0.000 claims description 27
- 238000002156 mixing Methods 0.000 claims description 14
- 230000006835 compression Effects 0.000 claims description 11
- 238000007906 compression Methods 0.000 claims description 11
- 239000003792 electrolyte Substances 0.000 claims description 10
- 230000004888 barrier function Effects 0.000 claims description 7
- 239000000178 monomer Substances 0.000 claims description 7
- 238000002360 preparation method Methods 0.000 claims description 7
- 239000000470 constituent Substances 0.000 claims description 5
- 238000000746 purification Methods 0.000 claims description 5
- 239000010425 asbestos Substances 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 3
- 229920005597 polymer membrane Polymers 0.000 claims description 3
- 229910052895 riebeckite Inorganic materials 0.000 claims description 3
- 230000003139 buffering effect Effects 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 claims 1
- 239000002028 Biomass Substances 0.000 abstract description 7
- 238000010248 power generation Methods 0.000 abstract description 7
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 7
- 238000000926 separation method Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 230000006837 decompression Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 238000005338 heat storage Methods 0.000 description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 3
- 229910001092 metal group alloy Inorganic materials 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 229910003296 Ni-Mo Inorganic materials 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 2
- 229910000564 Raney nickel Inorganic materials 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- -1 mixing device Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- DDTIGTPWGISMKL-UHFFFAOYSA-N molybdenum nickel Chemical compound [Ni].[Mo] DDTIGTPWGISMKL-UHFFFAOYSA-N 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000007868 Raney catalyst Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000008393 encapsulating agent Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000000629 steam reforming Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J3/00—Circuit arrangements for ac mains or ac distribution networks
-
- 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
-
- 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
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
-
- 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
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
-
- 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
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
- C25B9/73—Assemblies comprising two or more cells of the filter-press type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G1/00—Steam superheating characterised by heating method
- F22G1/16—Steam superheating characterised by heating method by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil
- F22G1/165—Steam superheating characterised by heating method by using a separate heat source independent from heat supply of the steam boiler, e.g. by electricity, by auxiliary combustion of fuel oil by electricity
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J1/00—Circuit arrangements for dc mains or dc distribution networks
- H02J1/10—Parallel operation of dc sources
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J3/00—Circuit arrangements for ac mains or ac distribution networks
- H02J3/38—Arrangements for parallely feeding a single network by two or more generators, converters or transformers
- H02J3/381—Dispersed generators
-
- H02J3/387—
-
- 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
- Y02E10/70—Wind energy
- Y02E10/76—Power conversion electric or electronic aspects
-
- 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
-
- 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
-
- 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
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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
-
- 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
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/20—Climate change mitigation technologies for sector-wide applications using renewable 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/40—Fuel cell technologies in production processes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Power Engineering (AREA)
- Inorganic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model provides a kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, cloud platform is controlled including dispatching of power netwoks peak regulation, clean energy resource electricity generation system, high-voltage web system, water electrolysis hydrogen production system, pure water prepares and water charging system, Hydrogen collection purifies and external induction system, also including the clean energy resource electricity generation system described in electrolytic cell high temperature steam supply system includes wind power plant, photovoltaic generation factory, hydraulic power plant, biomass power plant, garbage incinerating power plant, nuclear plant, gas power plant, in clean coal power plant generation mode, described water electrolysis hydrogen production system includes alkaline aqueous solution electrolysis hydrogen production device, solid polymer electrolytic device for producing hydrogen, high-temperature solid oxide electrolysis hydrogen production device.By clean energy resource electric energy electrolytic hydrogen production, peak regulation is realized, while the Hydrogen Energy produced easily can be stored and transported, and can also be mixed into existing gas distributing system or directly for sale, the effectiveness of operation of increase renewable energy power generation factory.
Description
Technical field
Electrolytic hydrogen production industry is the utility model is related to, more particularly to utilizes clean energy resource generating electrolytic hydrogen production and and Gas Pipe
The system for netting mixing.
Background technology
Water electrolysis hydrogen production is a kind of efficient, cleaning hydrogen producing technology, and its process for making hydrogen is simple, and product purity is high, hydrogen, oxygen
Gas purity is typically most potential extensive hydrogen producing technology up to 99.9%.Generated electricity in particular with current clean energy resource
Growing, hydrogen is by as the ideal carrier of power storage.Pass through water electrolysis hydrogen production technology by the way that clean energy resource is generated electricity, will
Electric energy is converted into Hydrogen Energy and stored caused by clean energy resource, and according to being actually needed, can also be incited somebody to action by follow-up chemical process
Hydrogen Energy is converted into methane, methanol and other liquid fuels etc..
Current Chinese hydrogen annual production has exceeded ten million ton of scale, occupies the first in the world.Plant-scale hydrogen production process is main
Including methane steam reforming and water electrolysis hydrogen production, the yield of wherein water electrolysis hydrogen production accounts for world's hydrogen total output 4%.Although first
Alkane steam reformation is hydrogen production process most economical at present, but it not only consumes a large amount of fossil fuels in process of production, and is produced
Raw great amount of carbon dioxide.Electrolysis hydrogen producing process process is simple, and product purity is high, by using clean energy resource as energy
Source, can show the efficient of hydrogen, cleaning, extensive preparation, and the technology can be used for CO2Emission reduction and conversion, have it is more wide
Wealthy development prospect.
Current water electrolysis hydrogen production method mainly has three kinds：Electrolyzed alkaline water hydrogen manufacturing, solid polymer electrolytic water hydrogen manufacturing, and
High-temperature solid oxide water electrolysis hydrogen production.Electrolyzed alkaline water hydrogen manufacturing is hydrogen production process highly developed at present, so far, industry
Upper large-scale water electrolysis hydrogen production is essentially all that this method technical process is simple using alkaline electrolysis hydrogen producing technology, is easy to grasp
Make.The main energy consumption of electrolytic hydrogen production is electric energy, and every cubic metre of hydrogen power consumption is about 4.5~5.5kWh, and the electricity charge account for whole electrolysis system
80% or so of hydrogen production cost.Therefore, the energy that water electrolysis hydrogen production technology generates electricity especially suitable for clean energy resourcies such as wind-power electricity generations
Source carrier.For example, prior art utilizes high-temperature water vapour electrolytic hydrogen production, such as the Chinese patent of Application No. 201210370229.5
Disclose a kind of Wind power high temperature electrolytic hydrogen preparation system and method.The system includes：Dc source, by the friendship of wind power generating set
Flow the direct current that electric rectification is first voltage；AC power, by the friendship that the alternating current transformation of wind power generating set is second voltage
Stream electricity；The superthermal vapor preparation unit of high temperature, the electrically prepared superheated water steam of exchange based on AC power；Aid in heat storage units,
The alternating current of AC power is received to store energy；High-temperature electrolysis Hydrogen Unit, high temperature is surpassed using the direct current of dc source
Superthermal vapor prepared by hot steam's preparation unit carries out electrolytic hydrogen production；Heat exchange unit, in high-temperature electrolysis Hydrogen Unit and auxiliary
Heat storage units are helped to carry out heat exchange, so that high-temperature electrolysis Hydrogen Unit maintains stable temperature, wherein, when AC power is defeated
When the alternating current voltage gone out significantly reduces, auxiliary heat storage units prepare the energy supply of storage to the superthermal vapor of high temperature single
Member, so that the superthermal vapor preparation unit of high temperature stably exports superthermal vapor.Though the patent make use of wind energy, it needs
First with electrical energy production high-temperature water vapor so that the system effectiveness of its whole hydrogen generating system is relatively low, it is impossible to be adapted to large-scale hydrogen
Can production.
Utility model content
The utility model provides a kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, including electricity
It is prepared by net scheduling peak regulation control cloud platform, clean energy resource electricity generation system, high-voltage web system, water electrolysis hydrogen production system, pure water
And the purification of water charging system, Hydrogen collection and external induction system, in addition to electrolytic cell high temperature steam supply system；
Described clean energy resource electricity generation system includes wind power plant, photovoltaic generation factory, hydraulic power plant, biomass power generation
At least one of factory, garbage incinerating power plant, nuclear plant, gas power plant, clean coal power plant generation mode, the above
Water electrolysis hydrogen production system power supply can individually be given by generating electricity, can also combination of two, or multiple power plant associating power supplies；
Described water electrolysis hydrogen production system includes alkaline aqueous solution electrolysis hydrogen production device, solid polymer electrolytic hydrogen manufacturing fills
Put, at least one of high-temperature solid oxide electrolysis hydrogen production device.
Preferably, the high-voltage web system includes electric switch under one or more critical point ammeters, high-voltage fence, power network
And inverter.
Any of the above-described scheme is preferably, and the dispatching of power netwoks peak regulation control cloud platform includes grid dispatching center and peak regulation
Hydrogen manufacturing centralized control center, the peak regulation hydrogen manufacturing centralized control center are arranged in clean energy resource power plant.
Any of the above-described scheme is preferably, and the grid dispatching center is adjusted in real time by electricity volume service condition
Degree, scheduling signals are transferred to peak regulation hydrogen manufacturing centralized control center, peak regulation hydrogen manufacturing centralized control center assigns peak load regulation network instruction, passes through control
Electric switch carries out peak load regulation network under the power network, and the delivery of water electrolysis hydrogen production system is controlled by peak regulation hydrogen manufacturing centralized control center.
Any of the above-described scheme is preferably, and the power supply mode in the power plant in the clean energy resource electricity generation system includes passing through
Inverter converts electrical current into direct current and supplies electricity to electrolytic hydrogen production system power supply, or power plant institute's generated energy directly to electrolytic hydrogen production system
System power supply.
Any of the above-described scheme is preferably, and the power supply mode in the power plant in the clean energy resource electricity generation system also includes will
Power plant generated energy is transported to high-voltage fence, and the high pressure three-phase alternating current of high-voltage fence is converted to direct current by inverter, then
Give electrolytic hydrogen production system power supply.
Any of the above-described scheme is preferably, and the electrolytic cell high temperature steam supply system includes main steam bypass, electricity overheat
Device, high-temperature steam conveyance conduit, the electric superheater steam inlet connect with main steam bypass, the electric superheater steam (vapor) outlet
It is connected with high-temperature steam conveyance conduit entrance.
Any of the above-described scheme is preferably, and the main steam bypass is connected with high temperature major steam line, the main steaming of high temperature
Steam in vapor pipeline is from biomass power plant, garbage incinerating power plant, nuclear plant, gas power plant, clean coal hair
At least one of power plant.
Any of the above-described scheme is preferably, the high-temperature steam entrance of the high-temperature solid oxide electrolysis hydrogen production device and institute
State high-temperature steam conveyance conduit outlet connection, the high-temperature steam temperature in main steam bypass is at 500 DEG C or so, high-temperature steam
Into electric high temperature superheater, more than 800 DEG C are superheated to by electric high temperature superheater.
Any of the above-described scheme is preferably, and described alkaline aqueous solution electrolysis hydrogen production device is by several monomer electrolytic cell groups
Into each electrolytic cell is made up of negative electrode, anode, barrier film and electrolyte.
Any of the above-described scheme is preferably, and the electrolyte includes potassium hydroxide solution, and concentration is 20wt%~30wt%.
Any of the above-described scheme is preferably, and the barrier film constituent includes asbestos.
Any of the above-described scheme is preferably, and the negative electrode, anode constituent include metal alloy, including the metal closes
Gold includes Raney Nickel (Raney's nickel), Ni-Mo alloys, for decomposition water, produces hydrogen and oxygen.
Any of the above-described scheme is preferably, and solid polymer electrolytic hydrogen manufacturing (SPE) device is electrolysed by several monomers
Groove forms.
Any of the above-described scheme is preferably, the solid polymer electrolytic device for producing hydrogen electrolytic cell using solid polymer membrane as
Electrolyte, there is no in electrolysis cycle alkali lye to be lost in, corrosion the problems such as.
Any of the above-described scheme is preferably, and high-temperature solid oxide electrolytic hydrogen production (SOEC) device is by several monomers
Electrolytic cell forms.
Any of the above-described scheme is preferably, and the high-temperature solid oxide electrolysis hydrogen production device operating temperature is 800~950
℃.Primary energy system exports electric energy and high temperature heat to high-temperature solid oxide electrolysis hydrogen production device, in electric energy and high warm
Under the collective effect of energy, by the electrolytically generated hydrogen of vapor and oxygen.
Any of the above-described scheme is preferably, and prepared by described pure water and water charging system includes running water system, pure water
Preparation facilities, small pump and water supply conduit.
Any of the above-described scheme is preferably, and the water of the running water system outflow enters pure water preparing device, then through mending
Water pump pressurizes, and enters water electrolysis hydrogen production system by water pipeline.
Any of the above-described scheme is preferably, and the water supply conduit outlet intakes with alkaline aqueous solution electrolysis hydrogen production device respectively
Mouth, the connection of solid polymer electrolytic device for producing hydrogen water inlet, high-temperature solid oxide electrolysis hydrogen production device water inlet.
Any of the above-described scheme is preferably, described Hydrogen collection purification and externally transport system include flush of hydrogen gas tank,
Hydrogen drain sump, hydrogen gas buffer, mixing device, hydrogen compression and skid-mounted system, fuel cell generation.
Any of the above-described scheme is preferably, the flush of hydrogen gas tank outlet connection hydrogen drain sump entrance, hydrogen drain sump
The outlet of entrance connection hydrogen gas buffer, hydrogen gas buffer outlet are electric with mixing device, hydrogen compression and skid-mounted system, fuel respectively
At least one of pond electricity generation system connects.
Any of the above-described scheme is preferably, and the mixing device is connected with existing gas ductwork.
Any of the above-described scheme is preferably, and the hydrogen mixing proportion of the mixing device is less than 20%.
Any of the above-described scheme is preferably, and the hydrogen compression and bulking system include hydrogen cylinder and/or skid tank car, press
Hydrogen after contracting can be filled into high pressure skid-mounted tank car, or compressed filling enters hydrogen cylinder, can be used in externally selling.
Any of the above-described scheme is preferably, and described fuel cell generation includes large-scale fuel cell power plant or car
Carry fuel cell.
Any of the above-described scheme is preferably, and the large-scale fuel cell power plant produces electric energy by the use of hydrogen as fuel.
Any of the above-described scheme is preferably, and the on-vehicle fuel is used for the battery car using Hydrogen Energy as fuel.
The utility model controls cloud platform to carry out real-time intelligent regulation and control to power network electricity consumption by dispatching of power netwoks peak regulation, passes through profit
With the clean energy resource such as large-scale wind electricity, photovoltaic electric energy come electrolytic hydrogen production, can solve in the annual four seasons abandon wind, abandon light, abandon water, abandoning core etc.
Abandon clean energy resource power generation issues, the Peak Load of preciousness be provided for power network, meanwhile, the Hydrogen Energy of production can easily store and
Transport, existing gas distributing system or directly for sale, the operation effect of increase renewable energy power generation factory can also be directly mixed in
Benefit.
Brief description of the drawings
Fig. 1 is according to the one excellent of the system of the present utility model that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production
Select the schematic diagram of embodiment.
Illustrate：
1- wind power plants, 2- photovoltaic generations factory, 3- hydraulic power plants, 4- biomass power plants, 5- waste incineration and generating electricities
Factory, 6- nuclear plants, 7- gas power plants, 8- clean coals power plant, 9- critical points ammeter, 10- high-voltage fences, 11- main steams
Bypass, electric switch under 12- power networks, 13- peak regulation hydrogen manufacturing centralized control center, 14- grid dispatching centers, the control of 15- dispatchings of power netwoks peak regulation
Cloud platform, 16- inverters, 17- high-temperature steam conveyance conduits, 18- alkaline aqueous solution electrolysis hydrogen production devices, 19- solid polymers
Electrolysis hydrogen production device, 20- high-temperature solid oxide electrolysis hydrogen production devices, 21- flush of hydrogen gas tanks, 22- hydrogen drain sumps, 23- hydrogen
Gas surge tank, 24- mixing devices, the compression of 25- hydrogen and skid-mounted system, 26- fuel cell generations, the existing Gas Pipes of 27-
Net, 28- running water systems, 29- pure water preparing devices, 30- small pumps, 31- water supply conduits.
Embodiment
In order to be further understood that utility model content of the present utility model, below in conjunction with specific embodiment to this practicality
New to be described in more detail, embodiment only has exemplary effect to the utility model, without any restrictions
Effect；The insubstantial modifications that any those skilled in the art make on the basis of the utility model, it should all belong to this practicality
Novel protected scope.
Embodiment 1
As shown in figure 1, a kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, including dispatching of power netwoks
Peak regulation control cloud platform 15, clean energy resource electricity generation system, the system of high-voltage fence 10, water electrolysis hydrogen production system, pure water prepare and
Water charging system, Hydrogen collection purification and external induction system, in addition to electrolytic cell high temperature steam supply system；Described cleaning energy
Source electricity generation system includes wind power plant 21, photovoltaic generation factory, hydraulic power plant 3, biomass power plant 4, waste incineration and generating electricity
Factory 5, nuclear plant 6, gas power plant 7, clean coal power plant 8；Described water electrolysis hydrogen production system includes alkaline aqueous solution
Electrolysis hydrogen production device 18, solid polymer electrolytic device for producing hydrogen 19, high-temperature solid oxide electrolysis hydrogen production device 20.
In the present embodiment, the system of high-voltage fence 10 includes one or more critical point ammeters 9, high-voltage fence 10, electricity
Electric switch 12 and inverter 16 off the net.
In the present embodiment, the dispatching of power netwoks peak regulation control cloud platform 15 includes grid dispatching center 14 and peak regulation hydrogen manufacturing
Centralized control center 13, the peak regulation hydrogen manufacturing centralized control center 13 are arranged in clean energy resource power plant.
In the present embodiment, the grid dispatching center 14 carries out Real-Time Scheduling by electricity volume service condition, will adjust
Degree signal is transferred to peak regulation hydrogen manufacturing centralized control center 13, and peak load regulation network instruction is assigned by peak regulation hydrogen manufacturing centralized control center 13, by controlling
State electric switch 12 under power network and carry out peak load regulation network, the delivery of water electrolysis hydrogen production system is controlled by peak regulation hydrogen manufacturing centralized control center 13.
In the present embodiment, the power supply mode in the power plant in the clean energy resource electricity generation system includes passing through inverter 16
Convert electrical current into direct current and supply electricity to electrolytic hydrogen production system power supply, such as biomass power plant 4, garbage incinerating power plant 5, nuclear energy hair
The alternating current that the grade alternator plant of power plant 6 is sent is powered to electrolysis hydrogen production device again after inverter 16 changes into direct current；Or
Person power plant institute's generated energy directly feeds alkalescence directly to electrolytic hydrogen production system power supply, such as the direct current that photovoltaic generation factory sends
Aqueous solution electrolysis device for producing hydrogen 18 carrys out hydrogen manufacturing.
In the present embodiment, the power supply mode in the power plant in the clean energy resource electricity generation system also includes sending out in power plant
Electricity is transported to high-voltage fence 10, and the high pressure three-phase alternating current of high-voltage fence 10 is converted to direct current by inverter 16, then gives
Electrolytic hydrogen production system power supply.
In the present embodiment, the electrolytic cell high temperature steam supply system includes main steam bypass 11, electric superheater, high temperature
Steam conveying pipe 17, the electric superheater steam inlet and main steam bypass 11 be connecteds, the electric superheater steam (vapor) outlet and
The entrance of high-temperature steam conveyance conduit 17 connects.
In the present embodiment, the main steam bypass 11 is connected with high temperature major steam line, the high temperature major steam line
In steam from biomass power plant 4, garbage incinerating power plant 5, nuclear plant 6, gas power plant 7 and cleaning coal power generation
Factory 8, each power plant's main steam bypass 11 are intersected in same vapor transport pipeline, steam are conveyed into electric superheater.
In the present embodiment, the high-temperature steam entrance of the high-temperature solid oxide electrolysis hydrogen production device 20 and the high temperature
The outlet of steam conveying pipe 17 connects, and at 500 DEG C or so, high-temperature steam enters the high-temperature steam temperature in the main steam bypass 11
Enter electric high temperature superheater, more than 800 DEG C are superheated to by electric high temperature superheater.
In the present embodiment, described alkaline aqueous solution electrolysis hydrogen production device by several monomer electrolytic cell groups into each
Electrolytic cell is made up of negative electrode, anode, barrier film and electrolyte.
In the present embodiment, preferable electrolyte is potassium hydroxide solution, concentration 30wt%.
In the present embodiment, the barrier film constituent includes asbestos.
In the present embodiment, the negative electrode, anode constituent include metal alloy, including the metal alloy includes thunder
Buddhist nun's nickel, Ni-Mo alloys, for decomposition water, produce hydrogen and oxygen.
In the present embodiment, the solid polymer electrolytic device for producing hydrogen 19 by several monomer electrolytic cell groups into.
In the present embodiment, the electrolytic cell is using solid polymer membrane as electrolyte.
In the present embodiment, the high-temperature solid oxide electrolysis hydrogen production device 20 is made up of several single electrolytic cells.
In the present embodiment, the operating temperature of high-temperature solid oxide electrolysis hydrogen production device 20 is 800 DEG C.
In the present embodiment, primary energy system output electric energy and high temperature heat to high-temperature solid oxide electrolytic hydrogen production fill
20 are put, under the collective effect of electric energy and high temperature heat, by the electrolytically generated hydrogen of vapor and oxygen.
In the present embodiment, prepared by described pure water and water charging system includes running water system 28, pure water prepares dress
Put 29, small pump 30 and water supply conduit 31.
In the present embodiment, the water that the running water system 28 flows out enters pure water preparing device 29, then through small pump
30 pressurizations, enter water electrolysis hydrogen production system by water pipeline.
In the present embodiment, the purification of described Hydrogen collection and external transport system take off including flush of hydrogen gas tank 21, hydrogen
Water pot 22, hydrogen gas buffer 23, mixing device 24, hydrogen compression and skid-mounted system 25 and fuel cell generation 26.
In the present embodiment, the mixing device 24 is connected with existing gas ductwork 27.
In the present embodiment, the hydrogen mixing proportion of the mixing device 24 is 15%.
In the present embodiment, the hydrogen compression and bulking system include hydrogen cylinder and/or skid tank car, the hydrogen after compression
Gas can be filled into high pressure skid-mounted tank car, or compressed filling enters hydrogen cylinder, can be used in externally selling.
In the present embodiment, described fuel cell generation 26 includes large-scale fuel cell power plant or onboard fuel
Battery.
In the present embodiment, the large-scale fuel cell power plant produces electric energy by the use of hydrogen as fuel.
In the present embodiment, the on-vehicle fuel is used for the battery car using Hydrogen Energy as fuel.
Clean energy resource electric energy by using large-scale wind electricity, photovoltaic or photo-thermal power generation factory output comes electrolytic hydrogen production, Ke Yiquan
The four seasons in year are solved abandon wind, abandon optical issue, and the Peak Load of preciousness is provided for power network, meanwhile, the Hydrogen Energy of production can be deposited easily
Storage and transport, city natural gas pipe network or directly for sale, the warp of increase renewable energy power generation factory can also be directly mixed in
Seek benefit.
Embodiment 2
Embodiment 2 is similar to Example 1, except that, preferable water electrolysis hydrogen production system includes more in the present embodiment
Individual alkaline aqueous solution electrolysis hydrogen production device 18, described alkaline aqueous solution electrolysis hydrogen production device 18 include electrolytic bath for oxyhydrogen separation,
Hydrogen gas water separation tank, hydrogen system add alkali tank, oxygen gas water separation tank, oxygen system to add alkali tank, electrolysis liquid pipeline, flush of hydrogen gas tank
21 and drain sump, oxygen clean tank.The electrolytic bath for oxyhydrogen separation is made up of negative electrode, anode, barrier film and electrolyte.Electrolytic cell
Using carbon fibre material and foam metal net as substrate and electrode material, such as carbon cloth, carbon paper, nickel foam, three stablized
Three-dimensional nanostructured is tieed up to improve its catalytic efficiency, and carbon fiber or nickel foam are used for catalyzing manufacturing of hydrogen directly as negative electrode, are formed
Special adhesive-free electrode.
Embodiment 3
Embodiment 3 is similar to Example 1, except that, preferable water electrolysis hydrogen production system includes more in the present embodiment
Individual high-temperature solid oxide electrolysis hydrogen production device 20, water vapour including main steam bypass 11, electric superheater, high-temperature steam by conveying
The high-temperature steam supply system supply of pipeline 17.Described high-temperature solid oxide electrolysis hydrogen production device 20 includes high-temp solid
Oxide electrolytic bath for oxyhydrogen separation, flush of hydrogen gas tank 21 and drain sump, oxygen clean tank.High-temperature solid oxide hydrogen-oxygen separation electricity
Solution groove is flat SOEC electrolytic cells, and bosom is fine and close dielectric substrate, and both sides are porous hydrogen electrode and oxygen electrode,
Dielectric substrate main function is to separate oxygen and fuel gas, and conduction oxonium ion or proton.Electrolyte is fine and close and with height
Ionic conductivity.Electrode is generally loose structure, in favor of the diffusion and transmission of gas.In addition, flat SOEC is also set up
Encapsulant, multiple single electrolytic cell composition piles also set up metallic interconnection materials.The electrolytic cell high temperature steam supply system bag
Include main steam bypass 11, electric superheater, high-temperature steam conveyance conduit 17, the electric superheater steam inlet and main steam bypass 11
Connection, the electric superheater steam (vapor) outlet are connected with the entrance of high-temperature steam conveyance conduit 17, and main steam passes through high-temperature electric superheater
It is heated to more than 800 degree and is re-introduced into electrolytic tank electrolysis hydrogen manufacturing.
Embodiment 4
Embodiment 4 is similar to Example 1, except that, the source of preferable electric power is wind-power electricity generation in the present embodiment
The DC generation amount of factory 21 supplies the suitable direct current of voltage directly to electrolysis hydrogen production device, or by power network decompression and inversion
Device 16 changes into direct current and supplies electricity to electrolyzer with electricity, and wind park and the owner of electrolytic hydrogen production system sign power supply contract.
Embodiment 5
Embodiment 5 is similar to Example 1, except that, the source of preferable electric power is photovoltaic generation in the present embodiment
The DC generation amount of factory supplies the suitable direct current of voltage directly to electrolysis hydrogen production device, or by power network decompression and inverter 16
Change into direct current and supply electricity to electrolyzer with electricity, photovoltaic generation factory and the owner of electrolytic hydrogen production system sign power supply contract.
Embodiment 6
Embodiment 6 is similar to Example 1, except that, the source of preferable electric power is hydroelectric generation in the present embodiment
Factory 3 and clean coal power plant 8, the DC generation amount of hydraulic power plant 3 are suitably straight directly to electrolysis hydrogen production device supply voltage
Stream electricity, or change into direct current by power network decompression and inverter 16 and supply electricity to electrolyzer with electricity, wind park and the industry of electrolytic hydrogen production system
Main signature power supply contract.8, clean coal power plant generated energy is transported to high-voltage fence 10, by 16 turns of power network decompression and inverter
Electrolyzer with electricity is supplied electricity into direct current.Meanwhile the steam in the steam turbine of clean coal power plant 8, overheated by main steam bypass 11, electricity
Device, high-temperature steam conveyance conduit 17 are transported in high-temperature solid oxide device for preparing hydrogen.The electric superheater steam enters
Mouth is connected with main steam bypass 11, and the electric superheater steam (vapor) outlet is connected with the entrance of high-temperature steam conveyance conduit 17, main steam
More than 800 degree are heated to from 500~600 DEG C be re-introduced into electrolytic tank electrolysis hydrogen manufacturing by high-temperature electric superheater.
Although the utility model, those skilled in the art has shown and described referring particularly to its preferred embodiment
It is appreciated that the various changes that can be made in form and details are new without departing from this practicality described in appended claims
The scope of type.It is described in detail above in association with specific embodiment of the utility model, but is not to limit of the present utility model
System.Every foundation the technical essence of the utility model still falls within this practicality to any simple modification made for any of the above embodiments
The scope of new technique scheme.
Claims (25)
1. a kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, including dispatching of power netwoks peak regulation control cloud are put down
Platform (15), clean energy resource electricity generation system, high-voltage fence (10) system, water electrolysis hydrogen production system, pure water preparation and water charging system,
Hydrogen collection purifies and external induction system, it is characterised in that：Also include electrolytic cell high temperature steam supply system；
Described clean energy resource electricity generation system includes wind power plant (1), photovoltaic generation factory (2), hydraulic power plant (3), biology
Matter power plant (4), garbage incinerating power plant (5), nuclear plant (6), gas power plant (7), clean coal power plant (8) generate electricity
At least one of mode；
Described water electrolysis hydrogen production system includes alkaline aqueous solution electrolysis hydrogen production device (18), solid polymer electrolytic device for producing hydrogen
(19), at least one of high-temperature solid oxide electrolysis hydrogen production device (20).
2. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：High-voltage fence (10) system includes electric switch under one or more critical point ammeters (9), high-voltage fence (10), power network
And inverter (16) (12).
3. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The dispatching of power netwoks peak regulation control cloud platform (15) includes grid dispatching center (14) and peak regulation hydrogen manufacturing centralized control center (13),
The peak regulation hydrogen manufacturing centralized control center (13) is arranged in clean energy resource power plant.
4. the system according to claim 3 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The grid dispatching center (14) carries out Real-Time Scheduling by electricity volume service condition, and scheduling signals are transferred into peak regulation
Hydrogen manufacturing centralized control center (13), peak load regulation network instruction is assigned by peak regulation hydrogen manufacturing centralized control center (13), by controlling electric switch under power network
(12) peak load regulation network is carried out, the delivery of water electrolysis hydrogen production system is controlled by peak regulation hydrogen manufacturing centralized control center (13).
5. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The power supply mode in the power plant in the clean energy resource electricity generation system includes converting electrical current into direct current by inverter (16)
Electrolytic hydrogen production system power supply, or power plant institute's generated energy are supplied electricity to directly to electrolytic hydrogen production system power supply.
6. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The power supply mode in the power plant in the clean energy resource electricity generation system also includes power plant generated energy being transported to high-voltage fence
(10), the high pressure three-phase alternating current of high-voltage fence (10) is converted to direct current by inverter (16), then gives electrolytic hydrogen production system
Power supply.
7. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The electrolytic cell high temperature steam supply system includes main steam bypass (11), electric superheater, high-temperature steam conveyance conduit
(17), the electric superheater steam inlet is connected with main steam bypass (11), the electric superheater steam (vapor) outlet and high-temperature steam
Conveyance conduit (17) entrance connects.
8. the system according to claim 7 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The main steam bypass (11) is connected with high temperature major steam line, and the steam in the high temperature major steam line is from biology
At least one of matter power plant, garbage incinerating power plant, nuclear plant, gas power plant, clean coal power plant.
9. the system according to claim 7 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The high-temperature steam entrance of high-temperature solid oxide electrolysis hydrogen production device (20) exports with the high-temperature steam conveyance conduit (17)
Connection, the high-temperature steam that the main steam is bypassed in (11) enter electric high temperature superheater, 800 are superheated to by electric high temperature superheater
More than DEG C.
10. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：Described alkaline aqueous solution electrolysis hydrogen production device (18) is by several monomer electrolytic cell groups into each electrolytic cell is by negative electrode, sun
Pole, barrier film and electrolyte are formed.
11. the system according to claim 10 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The barrier film constituent includes asbestos.
12. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The solid polymer electrolytic device for producing hydrogen (19) by several monomer electrolytic cell groups into.
13. the system according to claim 12 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The electrolytic cell is using solid polymer membrane as electrolyte.
14. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：The high-temperature solid oxide electrolysis hydrogen production device (20) is made up of several single electrolytic cells.
15. the system according to claim 14 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：High-temperature solid oxide electrolysis hydrogen production device (20) operating temperature is 800~950 DEG C.
16. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：Prepared by described pure water and water charging system includes running water system (28), pure water preparing device (29), small pump (30)
With water supply conduit (31).
17. the system according to claim 16 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The water of running water system (28) outflow enters pure water preparing device (29), then is pressurizeed through small pump (30), passes through
Water supply conduit (31) enters water electrolysis hydrogen production system.
18. the system according to claim 17 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：Water supply conduit (31) outlet is electric with alkaline aqueous solution electrolysis hydrogen production device (18) water inlet, solid polymer respectively
Solve device for producing hydrogen (19) water inlet, the connection of high-temperature solid oxide electrolysis hydrogen production device (20) water inlet.
19. the system according to claim 1 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature exist
In：Described Hydrogen collection purification and external transport system include flush of hydrogen gas tank (21), hydrogen drain sump (22), hydrogen buffering
Tank (23), mixing device (24), hydrogen compression and skid-mounted system (25), fuel cell generation (26).
20. the system according to claim 19 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：Described flush of hydrogen gas tank (21) outlet connection hydrogen drain sump (22) entrance, hydrogen drain sump (22) entrance connection hydrogen
Surge tank (23) export, hydrogen gas buffer (23) outlet respectively with mixing device (24), hydrogen compression and skid-mounted system (25), combustion
Expect the connection of at least one of battery generating system (26).
21. the system according to claim 20 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The mixing device (24) is connected with existing gas ductwork (27).
22. the system according to claim 19 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The hydrogen compression and bulking system include hydrogen cylinder and/or skid tank car, and the hydrogen after compression can be filled into high pressure
Skid tank car, or compressed filling enter hydrogen cylinder, can be used in externally selling.
23. the system according to claim 19 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：Described fuel cell generation (26) includes large-scale fuel cell power plant or on-vehicle fuel.
24. the system according to claim 23 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The large-scale fuel cell power plant produces electric energy by the use of hydrogen as fuel.
25. the system according to claim 23 that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production, its feature
It is：The on-vehicle fuel is used for the battery car using Hydrogen Energy as fuel.
Applications Claiming Priority (2)
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| CN2017102335304 | 2017-04-11 | ||
| CN201710233530 | 2017-04-11 |
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| CN201710394058.2A Pending CN107017634A (en) | 2017-04-11 | 2017-05-28 | The system that a kind of electrolytic hydrogen production is combined with nuclear power station flexibility peak regulation |
| CN201720611562.9U Active CN207166137U (en) | 2017-04-11 | 2017-05-28 | A kind of system that gas ductwork is injected using clean energy resource generating electrolytic hydrogen production |
| CN201710394061.4A Pending CN107093898A (en) | 2017-04-11 | 2017-05-28 | The system that a kind of application clean energy resource generating electrolytic hydrogen production injects gas ductwork |
| CN201710394045.5A Pending CN107017633A (en) | 2017-04-11 | 2017-05-28 | The system that a kind of electrolytic hydrogen production is combined with water-power plant |
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| CN201710394061.4A Pending CN107093898A (en) | 2017-04-11 | 2017-05-28 | The system that a kind of application clean energy resource generating electrolytic hydrogen production injects gas ductwork |
| CN201710394045.5A Pending CN107017633A (en) | 2017-04-11 | 2017-05-28 | The system that a kind of electrolytic hydrogen production is combined with water-power plant |
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| CN107017634A (en) | 2017-08-04 |
| CN107017633A (en) | 2017-08-04 |
| CN107093898A (en) | 2017-08-25 |
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