CN109786803A - A kind of electrochemical appliance - Google Patents
A kind of electrochemical appliance Download PDFInfo
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- CN109786803A CN109786803A CN201910107955.XA CN201910107955A CN109786803A CN 109786803 A CN109786803 A CN 109786803A CN 201910107955 A CN201910107955 A CN 201910107955A CN 109786803 A CN109786803 A CN 109786803A
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- electrochemistry region
- reducing agent
- oxidant
- feed channel
- setting
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- 230000005518 electrochemistry Effects 0.000 claims abstract description 1336
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 851
- 239000007800 oxidant agent Substances 0.000 claims abstract description 822
- 230000001590 oxidative effect Effects 0.000 claims abstract description 816
- 230000005611 electricity Effects 0.000 claims abstract description 355
- 239000000203 mixture Substances 0.000 claims abstract description 333
- 230000008676 import Effects 0.000 claims abstract description 157
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 126
- 239000000126 substance Substances 0.000 claims abstract description 112
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- 230000009467 reduction Effects 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims description 291
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- 239000003990 capacitor Substances 0.000 claims description 39
- 230000003647 oxidation Effects 0.000 claims description 32
- 238000007254 oxidation reaction Methods 0.000 claims description 32
- 230000005684 electric field Effects 0.000 claims description 21
- -1 dielectric Substances 0.000 claims description 16
- 239000004020 conductor Substances 0.000 claims description 15
- 238000002955 isolation Methods 0.000 claims description 12
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- OMOVVBIIQSXZSZ-UHFFFAOYSA-N [6-(4-acetyloxy-5,9a-dimethyl-2,7-dioxo-4,5a,6,9-tetrahydro-3h-pyrano[3,4-b]oxepin-5-yl)-5-formyloxy-3-(furan-3-yl)-3a-methyl-7-methylidene-1a,2,3,4,5,6-hexahydroindeno[1,7a-b]oxiren-4-yl] 2-hydroxy-3-methylpentanoate Chemical compound CC12C(OC(=O)C(O)C(C)CC)C(OC=O)C(C3(C)C(CC(=O)OC4(C)COC(=O)CC43)OC(C)=O)C(=C)C32OC3CC1C=1C=COC=1 OMOVVBIIQSXZSZ-UHFFFAOYSA-N 0.000 description 51
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- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
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- 229910052788 barium Inorganic materials 0.000 description 2
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 2
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 description 2
- FFBHFFJDDLITSX-UHFFFAOYSA-N benzyl N-[2-hydroxy-4-(3-oxomorpholin-4-yl)phenyl]carbamate Chemical compound OC1=C(NC(=O)OCC2=CC=CC=C2)C=CC(=C1)N1CCOCC1=O FFBHFFJDDLITSX-UHFFFAOYSA-N 0.000 description 2
- RFVVBBUVWAIIBT-UHFFFAOYSA-N beryllium nitrate Chemical compound [Be+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O RFVVBBUVWAIIBT-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
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- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
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- TXUICONDJPYNPY-UHFFFAOYSA-N (1,10,13-trimethyl-3-oxo-4,5,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-17-yl) heptanoate Chemical compound C1CC2CC(=O)C=C(C)C2(C)C2C1C1CCC(OC(=O)CCCCCC)C1(C)CC2 TXUICONDJPYNPY-UHFFFAOYSA-N 0.000 description 1
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- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N chromium trioxide Inorganic materials O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- 229940117975 chromium trioxide Drugs 0.000 description 1
- GAMDZJFZMJECOS-UHFFFAOYSA-N chromium(6+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Cr+6] GAMDZJFZMJECOS-UHFFFAOYSA-N 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910000431 copper oxide Inorganic materials 0.000 description 1
- IJCCOEGCVILSMZ-UHFFFAOYSA-L copper;dichlorate Chemical compound [Cu+2].[O-]Cl(=O)=O.[O-]Cl(=O)=O IJCCOEGCVILSMZ-UHFFFAOYSA-L 0.000 description 1
- 208000002925 dental caries Diseases 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- SOCTUWSJJQCPFX-UHFFFAOYSA-N dichromate(2-) Chemical compound [O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O SOCTUWSJJQCPFX-UHFFFAOYSA-N 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- VTIIJXUACCWYHX-UHFFFAOYSA-L disodium;carboxylatooxy carbonate Chemical compound [Na+].[Na+].[O-]C(=O)OOC([O-])=O VTIIJXUACCWYHX-UHFFFAOYSA-L 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005370 electroosmosis Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- 229910000043 hydrogen iodide Inorganic materials 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- ZICFUFGMZGWZMA-UHFFFAOYSA-L iron(2+) diiodate Chemical compound [Fe+2].[O-]I(=O)=O.[O-]I(=O)=O ZICFUFGMZGWZMA-UHFFFAOYSA-L 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000012280 lithium aluminium hydride Substances 0.000 description 1
- MHCFAGZWMAWTNR-UHFFFAOYSA-M lithium perchlorate Chemical compound [Li+].[O-]Cl(=O)(=O)=O MHCFAGZWMAWTNR-UHFFFAOYSA-M 0.000 description 1
- 229910001486 lithium perchlorate Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 230000005404 monopole Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- GTTYPHLDORACJW-UHFFFAOYSA-N nitric acid;sodium Chemical compound [Na].O[N+]([O-])=O GTTYPHLDORACJW-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- VLTRZXGMWDSKGL-UHFFFAOYSA-M perchlorate Inorganic materials [O-]Cl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-M 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 235000019396 potassium bromate Nutrition 0.000 description 1
- 229940094037 potassium bromate Drugs 0.000 description 1
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- SDLBJIZEEMKQKY-UHFFFAOYSA-M silver chlorate Chemical compound [Ag+].[O-]Cl(=O)=O SDLBJIZEEMKQKY-UHFFFAOYSA-M 0.000 description 1
- 229910001923 silver oxide Inorganic materials 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- MSFGZHUJTJBYFA-UHFFFAOYSA-M sodium dichloroisocyanurate Chemical compound [Na+].ClN1C(=O)[N-]C(=O)N(Cl)C1=O MSFGZHUJTJBYFA-UHFFFAOYSA-M 0.000 description 1
- 229940079827 sodium hydrogen sulfite Drugs 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- 229960005076 sodium hypochlorite Drugs 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 229960001922 sodium perborate Drugs 0.000 description 1
- 229940045872 sodium percarbonate Drugs 0.000 description 1
- BAZAXWOYCMUHIX-UHFFFAOYSA-M sodium perchlorate Chemical compound [Na+].[O-]Cl(=O)(=O)=O BAZAXWOYCMUHIX-UHFFFAOYSA-M 0.000 description 1
- 229910001488 sodium perchlorate Inorganic materials 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- YKLJGMBLPUQQOI-UHFFFAOYSA-M sodium;oxidooxy(oxo)borane Chemical compound [Na+].[O-]OB=O YKLJGMBLPUQQOI-UHFFFAOYSA-M 0.000 description 1
- 239000001119 stannous chloride Substances 0.000 description 1
- 235000011150 stannous chloride Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- UHCGLDSRFKGERO-UHFFFAOYSA-N strontium peroxide Chemical compound [Sr+2].[O-][O-] UHCGLDSRFKGERO-UHFFFAOYSA-N 0.000 description 1
- 229910052716 thallium Inorganic materials 0.000 description 1
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 description 1
- 230000035922 thirst Effects 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- GTQFPPIXGLYKCZ-UHFFFAOYSA-L zinc chlorate Chemical compound [Zn+2].[O-]Cl(=O)=O.[O-]Cl(=O)=O GTQFPPIXGLYKCZ-UHFFFAOYSA-L 0.000 description 1
- TUDPEWOTGHYZBQ-UHFFFAOYSA-L zinc;dibromate Chemical compound [Zn+2].[O-]Br(=O)=O.[O-]Br(=O)=O TUDPEWOTGHYZBQ-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
- Y02E60/50—Fuel cells
-
- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Abstract
The invention discloses a kind of electrochemical appliances, including electrochemistry region A and electrochemistry region B, electrochemistry region A is connected to reducing agent feed channel, electrochemistry region A is connected to oxidant feed channel, electrochemistry region B is connected to reducing agent feed channel, electrochemistry region B is connected to oxidant feed channel, electrochemistry region A includes alternating current Jie electricity area A, electrochemistry region B includes alternating current Jie electricity area B, and it is work normality that the export of the electronics between electrochemistry region A and electrochemistry region B, which imports,.Electrochemical appliance disclosed in this invention will terminate traditional chemical energy electric energy conversion electrochemical appliance with the history for existing for necessary condition of electrolyte (such as proton exchange membrane and solid oxide electrolyte etc.), this kind of device that terminates also can not be used securely and reliably to the history of oxidant reduction agent composition, industrialization for the chemical energy electric energy conversion electrochemical appliance of efficient, long-life, low cost provides new approach, and will redefine engine.
Description
Technical field
The present invention relates to electricity field, electrochemical field more particularly to a kind of electrochemical appliances.
Background technique
Conventional electrochemical device is required to non-electronic charged particle (such as negative oxygen ion or proton) and transmits between two electrodes,
For example, it is desired to which the positive charged particle and electronics that electrochemistry region (electrode) generates are removed, or need to produce in electrochemistry region
Raw electronegative non-electronic charged particle removes.Non-electronic charged particle not only consumes electric energy in the transmission of two interpolars, but also
It is required to transmit non-electronic charged particle and does not transmit electronics and electrolyte (such as the hydrogen fuel cell with many particular/special requirements
Proton exchange membrane, solid oxide electrolyte etc.), because of the complexity of electrolyte, manufacturing technology is unqualified always, and
As the basic reason for restricting electrochemical appliance (such as fuel cell etc.) improved efficiency, life-span upgrading and cost reduction, also
The problem the most serious of electrochemical appliance (such as fuel cell etc.) efficient industrialization is hindered through becoming.If one can be invented
Kind, will termination tradition electrification not to remove model electrochemical device of the non-electronic charged particle as necessary condition from electrochemistry region
It learns device (such as fuel cell etc.) and necessity is existed for electrolyte (such as proton exchange membrane, solid oxide electrolyte etc.)
The conventional electrochemical device that terminates also cannot securely and reliably be used the history of reducing agent oxidant mixture by the history of condition, and
The industrialization for converting electrochemical appliance for efficient, long-life, inexpensive chemical energy electric energy provides new approach, and will redefine
Engine.Therefore, it is necessary to invent a kind of model electrochemical device.
Summary of the invention
To solve the above-mentioned problems, technical solution proposed by the present invention is as follows:
A kind of electrochemical appliance of scheme 1., including electrochemistry region A and electrochemistry region B, the electrochemistry region A with also
The connection setting of former agent feed channel, the electrochemistry region A are connected to setting, the electrochemistry region B with oxidant feed channel
Setting is connected to reducing agent feed channel, the electrochemistry region B is connected to setting, the electrification school district with oxidant feed channel
Domain A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, the electrochemistry region A and
It is work normality that the export of electronics between the electrochemistry region B, which imports,；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel, the electrochemistry region A and oxidant are supplied
Channel connection setting is sent, the electrochemistry region B is connected to setting, the electrochemistry region B and oxidation with reducing agent feed channel
The connection setting of agent feed channel, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternation
Electric current Jie electricity area B；Reducing agent feed channel supplies the process of the electrochemistry region A feed reducing agent and the oxidant
Send channel to the process of the electrochemistry region A feed oxidant alternately, reducing agent feed channel is to the electrification
The process of the process of school district domain B feed reducing agent and oxidant feed channel to the electrochemistry region B feed oxidant
Alternately, in some time interval, to one of described electrochemistry region A feed Oxidizing and Reducing Agents, to described
Another kind in the B feed Oxidizing and Reducing Agents of electrochemistry region；Between the electrochemistry region A and the electrochemistry region B
Electronics export import be work normality；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel, the electrochemistry region A and oxidant are supplied
Channel connection setting is sent, the electrochemistry region B is connected to setting, the electrochemistry region B and oxidation with reducing agent feed channel
The connection setting of agent feed channel, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternation
Electric current Jie electricity area B；Reducing agent feed channel supplies the process of the electrochemistry region A feed reducing agent and the oxidant
Channel is sent to there is overlapping to the process of the electrochemistry region A feed oxidant, reducing agent feed channel is to the electrification
The process of the process of school district domain B feed reducing agent and oxidant feed channel to the electrochemistry region B feed oxidant
There are overlappings；It is work normality that the export of electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel, the electrochemistry region A and oxidant are supplied
Channel connection setting is sent, the electrochemistry region B is connected to setting, the electrochemistry region B and oxidation with reducing agent feed channel
The connection setting of agent feed channel, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternation
Electric current Jie electricity area B；Process and the oxidation of the reducing agent feed channel to the interrupted feed reducing agent of the electrochemistry region A
There is overlapping, reducing agent feed channel pair to the process of the interrupted feed oxidant of the electrochemistry region A in agent feed channel
The process of the interrupted feed reducing agent of electrochemistry region B and oxidant feed channel are interrupted to the electrochemistry region B
There is overlapping in the process of feed oxidant；The export of electronics between the electrochemistry region A and the electrochemistry region B imports
For the normality that works.
A kind of electrochemical appliance of scheme 2., including electrochemistry region A and electrochemistry region B, the electrochemistry region A setting
In cavity A, the cavity A is connected to setting with reducing agent feed channel, and the cavity A is connected to oxidant feed channel and sets
Set, the electrochemistry region B is arranged in cavity B, and the cavity B is connected to setting with reducing agent feed channel, the cavity B and
The connection setting of oxidant feed channel, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes
Alternating current Jie electricity area B, it is that work is normal that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,
State；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel
It states cavity A and is connected to setting with oxidant feed channel, the electrochemistry region B is arranged in cavity B, the cavity B and reduction
The connection setting of agent feed channel, the cavity B are connected to setting with oxidant feed channel, and the electrochemistry region A includes alternation
Electric current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B；Reducing agent feed channel is to the cavity A
The process of feed reducing agent and oxidant feed channel to the process of the cavity A feed oxidant alternately, it is described
Reducing agent feed channel is to the process of the cavity B feed reducing agent and oxidant feed channel to the cavity B feed
The process of oxidant alternately, in some time interval, to one of described cavity A feed Oxidizing and Reducing Agents,
To the another kind in the cavity B feed Oxidizing and Reducing Agents；Between the electrochemistry region A and the electrochemistry region B
Electronics export import be work normality；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel
It states cavity A and is connected to setting with oxidant feed channel, the electrochemistry region B is arranged in cavity B, the cavity B and reduction
The connection setting of agent feed channel, the cavity B are connected to setting with oxidant feed channel, and the electrochemistry region A includes alternation
Electric current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B；Reducing agent feed channel is to the cavity A
There is overlapping to the process of the cavity A feed oxidant in the process of feed reducing agent and oxidant feed channel, described
Reducing agent feed channel is to the process of the cavity B feed reducing agent and oxidant feed channel to the cavity B feed
There is overlapping in the process of oxidant；It is work that the export of electronics between the electrochemistry region A and the electrochemistry region B, which imports,
Make normality；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel
It states cavity A and is connected to setting with oxidant feed channel, the electrochemistry region B is arranged in cavity B, the cavity B and reduction
The connection setting of agent feed channel, the cavity B are connected to setting with oxidant feed channel, and the electrochemistry region A includes alternation
Electric current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B；Reducing agent feed channel is to the cavity A
There is weight to the process of the interrupted feed oxidant of the cavity A in the process of interrupted feed reducing agent and oxidant feed channel
Folded, reducing agent feed channel is to the process of the interrupted feed reducing agent of the cavity B and oxidant feed channel to institute
There is overlapping in the process for stating the interrupted feed oxidant of cavity B；Electricity between the electrochemistry region A and the electrochemistry region B
It is work normality that the export of son, which imports,.
A kind of electrochemical appliance of scheme 3., including electrochemistry region A and electrochemistry region B, the electrochemistry region A and institute
State electrochemistry region B setting in the cavity, the cavity is connected to setting with reducing agent feed channel, and the cavity and oxidant supply
Channel connection setting is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current
The area Jie electricity B, it is work normality that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity and reducing agent feed
Channel connection setting, the cavity are connected to setting with oxidant feed channel, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, the process of reducing agent feed channel feed reducing agent and institute
State the process of oxidant feed channel feed oxidant alternately, the electrochemistry region A and the electrochemistry region B it
Between electronics export import be work normality；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity and reducing agent feed
Channel connection setting, the cavity are connected to setting with oxidant feed channel, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, the process of reducing agent feed channel feed reducing agent and institute
There is overlapping in the process for stating oxidant feed channel feed oxidant, the electrochemistry region A and the electrochemistry region B it
Between electronics export import be work normality；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity and reducing agent feed
Channel connection setting, the cavity are connected to setting with oxidant feed channel, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, the feed of the interrupted feed reducing agent in reducing agent feed channel
There is overlapping, the electrochemistry region A and institute in the feed process of the interrupted feed oxidant of process and oxidant feed channel
It is work normality that the export for stating the electronics between the B of electrochemistry region, which imports,.
A kind of electrochemical appliance of scheme 4., including electrochemistry region A and electrochemistry region B, the electrochemistry region A is through also
Former agent control switch A is connected to setting with reducing agent feed channel, and the electrochemistry region A is through oxidant control switch A and oxidation
The connection setting of agent feed channel, the electrochemistry region B are connected to setting with reducing agent feed channel through reducing agent control switch B,
The electrochemistry region B is connected to setting with oxidant feed channel through oxidant control switch B, and the electrochemistry region A includes
Alternating current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B, the electrochemistry region A and the electrification
It is work normality that the export of electronics between the B of school district domain, which imports,；
Or, the electrochemistry region A is connected to setting, the electrification with reducing agent feed channel through reducing agent control switch A
School district domain A is connected to setting with oxidant feed channel through oxidant control switch A, and the electrochemistry region B is controlled through reducing agent
Switch B is connected to setting with reducing agent feed channel, and the electrochemistry region B is logical through oxidant control switch B and oxidant feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B；The reducing agent control switch A is controlled by control device and the oxidant control switch A by control device is controlled realization
The process of reducing agent feed channel feed reducing agent and the process of oxidant feed channel feed oxidant alternately into
Row, the reducing agent control switch B is controlled by control device and the oxidant control switch B is controlled by control device and realized institute
The process of the process and oxidant feed channel feed oxidant of stating reducing agent feed channel feed reducing agent alternately,
In some time interval, to one of described electrochemistry region A feed Oxidizing and Reducing Agents, to the electrochemistry region
Another kind in B feed Oxidizing and Reducing Agents；Electronics between the electrochemistry region A and the electrochemistry region B is led
Import out is work normality；
Or, the electrochemistry region A is connected to setting, the electrification with reducing agent feed channel through reducing agent control switch A
School district domain A is connected to setting with oxidant feed channel through oxidant control switch A, and the electrochemistry region B is controlled through reducing agent
Switch B is connected to setting with reducing agent feed channel, and the electrochemistry region B is logical through oxidant control switch B and oxidant feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B；The reducing agent control switch A is controlled by control device and the oxidant control switch A by control device is controlled realization
There is weight in the process of reducing agent feed channel feed reducing agent and the process of oxidant feed channel feed oxidant
It is folded, it states reducing agent control switch B and control by control device and described in the oxidant control switch B controlled by control device and to realize
There is overlapping in the process of reducing agent feed channel feed reducing agent and the process of oxidant feed channel feed oxidant；Institute
It is work normality that the export for stating the electronics between electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is connected to setting, the electrification with reducing agent feed channel through reducing agent control switch A
School district domain A is connected to setting with oxidant feed channel through oxidant control switch A, and the electrochemistry region B is controlled through reducing agent
Switch B is connected to setting with reducing agent feed channel, and the electrochemistry region B is logical through oxidant control switch B and oxidant feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B；The reducing agent control switch A is controlled by control device and the oxidant control switch A by control device is controlled realization
The interrupted feed oxidant of feed process and oxidant feed channel of the interrupted feed reducing agent in reducing agent feed channel
Feed process exist overlapping, the reducing agent control switch B by control device controlled and the oxidant control switch B by
Control device control realizes that the feed process of the interrupted feed reducing agent in reducing agent feed channel and the oxidant feed are logical
There is overlapping in the feed process of the interrupted feed oxidant in road；Electronics between the electrochemistry region A and the electrochemistry region B
Export import be work normality；
Or, the electrochemistry region A is connected to setting, the electrification with reducing agent feed channel through reducing agent control switch A
School district domain A is connected to setting with oxidant feed channel through oxidant control switch A, and the electrochemistry region B is controlled through reducing agent
Switch B is connected to setting with reducing agent feed channel, and the electrochemistry region B is logical through oxidant control switch B and oxidant feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B；It controls the reducing agent control switch A and the oxidant control switch A by control device and realizes the reducing agent control
System switch A is opened and is opened the oxidant control switch A discontinuously and make the reducing agent control switch B and the oxidation
Agent control switch B is controlled by control device realizes that the reducing agent control switch B is opened and kept the oxidant control switch B disconnected
It is continuous to open, or, controlling the reducing agent control switch A and the oxidant control switch A by control device realizes the oxygen
Agent control switch A is opened and is opened the reducing agent control switch A discontinuously and make the reducing agent control switch B and institute
Oxidant control switch B is stated to be controlled the realization oxidant control switch B unlatching by control device and control the reducing agent
Switch B is discontinuously opened, or the reducing agent control switch A and the oxidant control switch A is made to be controlled realization by control device
The reducing agent control switch A is opened and is opened the oxidant control switch A discontinuously and open the reducing agent control
The B and oxidant control switch B is closed to be controlled the realization oxidant control switch B unlatching by control device and make described go back
Former agent control switch B is discontinuously opened；The export of electronics between the electrochemistry region A and the electrochemistry region B imports
Work normality；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel, the electrochemistry region A is through oxidant control
System switch A is connected to setting with oxidant feed channel, and the electrochemistry region B is connected to setting with reducing agent feed channel, described
Electrochemistry region B is connected to setting with oxidant feed channel through oxidant control switch B, and the electrochemistry region A includes alternation
Electric current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B；Fill the oxidant control switch A by control
It sets control and realizes that the oxidant control switch A is discontinuously opened and controlled the oxidant control switch B by control device
Realize that the oxidant control switch B is discontinuously opened；Electronics between the electrochemistry region A and the electrochemistry region B
It is work normality that export, which imports,；
Or, the electrochemistry region A is connected to setting with oxidant feed channel, the electrochemistry region A is through reducing agent control
System switch A is connected to setting with reducing agent feed channel, and the electrochemistry region B is connected to setting with oxidant feed channel, described
Electrochemistry region B is connected to setting with reducing agent feed channel through reducing agent control switch B, and the electrochemistry region A includes alternation
Electric current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B；Fill the reducing agent control switch A by control
It sets control and realizes that the reducing agent control switch A is discontinuously opened and controlled the reducing agent control switch B by control device
Realize that the reducing agent control switch B is discontinuously opened；Electronics between the electrochemistry region A and the electrochemistry region B
It is work normality that export, which imports,；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel, the electrochemistry region A is through oxidant control
System switch A is connected to setting with oxidant feed channel, and the electrochemistry region B is connected to setting with oxidant feed channel, described
Electrochemistry region B is connected to setting with reducing agent feed channel through reducing agent control switch B, and the electrochemistry region A includes alternation
Electric current Jie electricity area A, the electrochemistry region B include alternating current Jie electricity area B；Fill the oxidant control switch A by control
It sets control and realizes that the oxidant control switch A is discontinuously opened and controlled the reducing agent control switch B by control device
Realize that the reducing agent control switch B is discontinuously opened；Electronics between the electrochemistry region A and the electrochemistry region B
It is work normality that export, which imports,.
A kind of electrochemical appliance of scheme 5., including electrochemistry region A and electrochemistry region B, the electrochemistry region A setting
In cavity A, the cavity A is connected to setting with reducing agent feed channel through reducing agent control switch A, and the cavity A is through aoxidizing
Agent control switch A is connected to setting with oxidant feed channel, and the electrochemistry region B is arranged in cavity B, the cavity B warp
Reducing agent control switch B is connected to setting with reducing agent feed channel, and the cavity B is supplied through oxidant control switch B and oxidant
Channel connection setting is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternation electricity
The area Liu Jie electricity B, it is work normality that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is supplied through reducing agent control switch A and reducing agent
Channel connection setting is sent, the cavity A is connected to setting, the electrochemistry with oxidant feed channel through oxidant control switch A
Region B is arranged in cavity B, and the cavity B is connected to setting, the chamber with reducing agent feed channel through reducing agent control switch B
Body B is connected to setting with oxidant feed channel through oxidant control switch B, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B；The reducing agent control switch A is controlled and institute by control device
It states oxidant control switch A and is controlled the process for realizing reducing agent feed channel feed reducing agent and the oxygen by control device
Alternately, the reducing agent control switch B is controlled and described the process of agent feed channel feed oxidant by control device
Oxidant control switch B is controlled the process and the oxidation for realizing reducing agent feed channel feed reducing agent by control device
The process of agent feed channel feed oxidant alternately, in some time interval, aoxidizes the electrochemistry region A feed
One of agent and reducing agent, to the another kind in the electrochemistry region B feed Oxidizing and Reducing Agents；The electrification school district
It is work normality that the export of electronics between domain A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is supplied through reducing agent control switch A and reducing agent
Channel connection setting is sent, the cavity A is connected to setting, the electrochemistry with oxidant feed channel through oxidant control switch A
Region B is arranged in cavity B, and the cavity B is connected to setting, the chamber with reducing agent feed channel through reducing agent control switch B
Body B is connected to setting with oxidant feed channel through oxidant control switch B, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B；The reducing agent control switch A is controlled and institute by control device
It states oxidant control switch A and is controlled the process for realizing reducing agent feed channel feed reducing agent and the oxygen by control device
There is overlapping in the process of agent feed channel feed oxidant, the reducing agent control switch B is controlled and described by control device
Oxidant control switch B is controlled the process and the oxidation for realizing reducing agent feed channel feed reducing agent by control device
There is overlapping in the process of agent feed channel feed oxidant；Electricity between the electrochemistry region A and the electrochemistry region B
It is work normality that the export of son, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is supplied through reducing agent control switch A and reducing agent
Channel connection setting is sent, the cavity A is connected to setting, the electrochemistry with oxidant feed channel through oxidant control switch A
Region B is arranged in cavity B, and the cavity B is connected to setting, the chamber with reducing agent feed channel through reducing agent control switch B
Body B is connected to setting with oxidant feed channel through oxidant control switch B, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B；The reducing agent control switch A is controlled and institute by control device
It states oxidant control switch A and is controlled the feed process for realizing the interrupted feed reducing agent in reducing agent feed channel by control device
There is overlapping with the feed process of the interrupted feed oxidant in oxidant feed channel, the reducing agent control switch B is controlled
Device control processed and the oxidant control switch B are controlled by control device realizes reducing agent feed channel discontinuously for returning
There is overlapping in the feed process of the interrupted feed oxidant of the feed process of former agent and oxidant feed channel；The electrochemistry
It is work normality that the export of electronics between region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is supplied through reducing agent control switch A and reducing agent
Channel connection setting is sent, the cavity A is connected to setting, the electrochemistry with oxidant feed channel through oxidant control switch A
Region B is arranged in cavity B, and the cavity B is connected to setting, the chamber with reducing agent feed channel through reducing agent control switch B
Body B is connected to setting with oxidant feed channel through oxidant control switch B, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B；Control the reducing agent control switch A and the oxidant
Switch A is controlled by control device realizes that the reducing agent control switch A is opened and opened the oxidant control switch A discontinuously
And it controls the reducing agent control switch B and the oxidant control switch B by control device and realizes the reducing agent control
System switch B is opened and is opened the oxidant control switch B discontinuously, or, making the reducing agent control switch A and the oxidation
Agent control switch A is controlled by control device realizes that the oxidant control switch A is opened and kept the reducing agent control switch A disconnected
It is continuous to open and the reducing agent control switch B and the oxidant control switch B is made to be controlled the realization oxygen by control device
Agent control switch B is opened and is opened the reducing agent control switch B discontinuously, or makes the reducing agent control switch A and institute
Oxidant control switch A is stated to be controlled the realization reducing agent control switch A unlatching by control device and control the oxidant
Switch A discontinuously opens and makes the reducing agent control switch B and the oxidant control switch B to be controlled realization by control device
The oxidant control switch B is opened and is opened the reducing agent control switch B discontinuously；The electrochemistry region A and described
It is work normality that the export of electronics between the B of electrochemistry region, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel
It states cavity A and is connected to setting with oxidant feed channel through oxidant control switch A, the electrochemistry region B is arranged in cavity B
Interior, the cavity B is connected to setting with reducing agent feed channel, and the cavity B is logical through oxidant control switch B and oxidant feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B, the oxidant control switch A are controlled interrupted unlatching by control device, and the oxidant control switch B is by control device control
System is discontinuously opened；It is work normality that the export of electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with oxidant feed channel
It states cavity A and is connected to setting with reducing agent feed channel through reducing agent control switch A, the electrochemistry region B is arranged in cavity B
Interior, the cavity B is connected to setting with oxidant feed channel, and the cavity B is logical through reducing agent control switch B and reducing agent feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B, the reducing agent control switch A are controlled interrupted unlatching by control device, and the reducing agent control switch B is by control device control
System is discontinuously opened；It is work normality that the export of electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel
It states cavity A and is connected to setting with oxidant feed channel through oxidant control switch A, the electrochemistry region B is arranged in cavity B
Interior, the cavity B is connected to setting with oxidant feed channel, and the cavity B is logical through reducing agent control switch B and reducing agent feed
Road connection setting, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes that alternating current connects electricity
Area B, the oxidant control switch A are controlled interrupted unlatching by control device, and the reducing agent control switch B is by control device control
System is discontinuously opened；It is work normality that the export of electronics between the electrochemistry region A and the electrochemistry region B, which imports,.
A kind of electrochemical appliance of scheme 6., including electrochemistry region A and electrochemistry region B, the electrochemistry region A and institute
State electrochemistry region B setting in the cavity, the cavity is connected to setting, institute with reducing agent feed channel through reducing agent control switch
It states cavity and is connected to setting with oxidant feed channel through oxidant control switch, the electrochemistry region A includes that alternating current connects
Electric area A, the electrochemistry region B include alternating current Jie electricity area B, the electrochemistry region A and the electrochemistry region B it
Between electronics export import be work normality；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity is controlled through reducing agent
Switch is connected to setting with reducing agent feed channel, and the cavity is connected to oxidant feed channel through oxidant control switch and sets
It sets, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, described
Reducing agent control switch is controlled by control device and the oxidant control switch is controlled by control device and realizes the reducing agent
The process of feed channel feed reducing agent and the process of oxidant feed channel feed oxidant alternately, the electrification
It is work normality that the export of electronics between school district domain A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity is controlled through reducing agent
Switch is connected to setting with reducing agent feed channel, and the cavity is connected to oxidant feed channel through oxidant control switch and sets
It sets, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, described
Reducing agent control switch is controlled by control device and the oxidant control switch is controlled by control device and realizes the reducing agent
There is overlapping, the electrification in the process of feed channel feed reducing agent and the process of oxidant feed channel feed oxidant
It is work normality that the export of electronics between school district domain A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity is controlled through reducing agent
Switch is connected to setting with reducing agent feed channel, and the cavity is connected to oxidant feed channel through oxidant control switch and sets
It sets, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, described
Reducing agent control switch is controlled by control device and the oxidant control switch is controlled by control device and realizes the reducing agent
The feed process of the interrupted feed oxidant of feed process and oxidant feed channel of the interrupted feed reducing agent in feed channel
There are overlapping, it is work normality that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity is controlled through reducing agent
Switch is connected to setting with reducing agent feed channel, and the cavity is connected to oxidant feed channel through oxidant control switch and sets
It sets, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B；Make institute
Reducing agent control switch is stated to be controlled realization unlatching by control device and control the oxidant control switch in fact by control device
It now discontinuously opens, or so that the reducing agent control switch control realization by control device and discontinuously open and make oxidant control
Switch is controlled realization by control device and is opened；The export of electronics between the electrochemistry region A and the electrochemistry region B is led
Enter for the normality that works.
A kind of electrochemical appliance of scheme 7., including electrochemistry region A and electrochemistry region B, the electrochemistry region A with also
Former agent feed channel A connection setting, the electrochemistry region A are connected to setting, the electrochemistry region with oxidant feed channel A
B is connected to setting with reducing agent feed channel B, and the electrochemistry region B is connected to setting with oxidant feed channel B, goes back described
Former agent feed channel A or on oxidant feed channel A be arranged control switch A, reducing agent feed channel B or
Control switch B is set on oxidant feed channel B, and the electrochemistry region A includes alternating current Jie electricity area A, the electricity
Chemical regions B includes alternating current Jie electricity area B, the export of the electronics between the electrochemistry region A and the electrochemistry region B
Importing is work normality；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel A, the electrochemistry region A and oxidant are supplied
Channel A connection setting is sent, the electrochemistry region B is connected to setting, the electrochemistry region B and oxygen with reducing agent feed channel B
Agent feed channel B connection setting, in reducing agent feed channel A or the setting control on oxidant feed channel A
Switch A, in the reducing agent feed channel B or setting control switch B on oxidant feed channel B, the electrochemistry
Region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, the control switch A and institute
It states control switch B and is controlled alternately unlatching by control device, the electronics between the electrochemistry region A and the electrochemistry region B
Export import be work normality；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel A, the electrochemistry region A and oxidant are supplied
Channel A connection setting is sent, the electrochemistry region B is connected to setting, the electrochemistry region B and oxygen with reducing agent feed channel B
Agent feed channel B connection setting, in reducing agent feed channel A or the setting control on oxidant feed channel A
Switch A, in the reducing agent feed channel B or setting control switch B on oxidant feed channel B, the electrochemistry
Region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, the control switch A and institute
Control switch B is stated to be controlled in the presence of overlapping unlatching, between the electrochemistry region A and the electrochemistry region B by control device
It is work normality that the export of electronics, which imports,；
Or, the electrochemistry region A is connected to setting with reducing agent feed channel A, the electrochemistry region A and oxidant are supplied
Channel A connection setting is sent, the electrochemistry region B is connected to setting, the electrochemistry region B and oxygen with reducing agent feed channel B
Agent feed channel B connection setting, in reducing agent feed channel A or the setting control on oxidant feed channel A
Switch A, in the reducing agent feed channel B or setting control switch B on oxidant feed channel B, the electrochemistry
Region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B；Make the control switch A by
Control device control, which is realized, to be continued reducing agent described in feed to the electrochemistry region A and discontinuously supplies the electrochemistry region A
It send the oxidant and the control switch B is made to be controlled realization by control device and feed institute is continued to the electrochemistry region B
It states reducing agent and to oxidant described in the interrupted feed of electrochemistry region B, or controls the control switch A by control device
Realization continues oxidant described in feed to the electrochemistry region A and to reducing agent described in the interrupted feed of electrochemistry region A
And so that the control switch B is controlled realization by control device and oxidant described in feed and right is continued to the electrochemistry region B
Reducing agent described in the interrupted feed of electrochemistry region B, or the control switch A is made to be controlled realization to the electricity by control device
Chemical regions A continues reducing agent described in feed and to oxidant agent described in the interrupted feed of electrochemistry region A and makes described
Control switch B is controlled realization by control device and continues oxidant described in feed to the electrochemistry region B and to the electrochemistry
The export of reducing agent described in the interrupted feed of region B, the electronics between the electrochemistry region A and the electrochemistry region B imports
For the normality that works.
A kind of electrochemical appliance of scheme 8., including electrochemistry region A and electrochemistry region B, the electrochemistry region A setting
In cavity A, the cavity A is connected to setting with reducing agent feed channel A, and the cavity A is connected to oxidant feed channel A
Setting, the electrochemistry region B are arranged in cavity B, and the cavity B is connected to setting, the cavity with reducing agent feed channel B
B is connected to setting with oxidant feed channel B, is arranged in reducing agent feed channel A or on oxidant feed channel A
Control switch A, in the reducing agent feed channel B or setting control switch B on oxidant feed channel B, the electricity
Chemical regions A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, the electrification school district
It is work normality that the export of electronics between domain A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel A
State cavity A and be connected to setting with oxidant feed channel A, the electrochemistry region B is arranged in cavity B, the cavity B with also
Former agent feed channel B connection setting, the cavity B is connected to setting with oxidant feed channel B, in reducing agent feed channel
Control switch A is arranged in A on oxidant feed channel A, supplies in reducing agent feed channel B or in the oxidant
Setting control switch B on the B of channel is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes
Alternating current Jie electricity area B, the control switch A and the control switch B are controlled by control device and are alternately opened, the electrochemistry
It is work normality that the export of electronics between region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel A
State cavity A and be connected to setting with oxidant feed channel A, the electrochemistry region B is arranged in cavity B, the cavity B with also
Former agent feed channel B connection setting, the cavity B is connected to setting with oxidant feed channel B, in reducing agent feed channel
Control switch A is arranged in A on oxidant feed channel A, supplies in reducing agent feed channel B or in the oxidant
Setting control switch B on the B of channel is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes
Alternating current Jie electricity area B, the control switch A and the control switch B are controlled by control device and are opened in the presence of overlapping, the electricity
It is work normality that the export of electronics between chemical regions A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is connected to setting, institute with reducing agent feed channel A
State cavity A and be connected to setting with oxidant feed channel A, the electrochemistry region B is arranged in cavity B, the cavity B with also
Former agent feed channel B connection setting, the cavity B is connected to setting with oxidant feed channel B, in reducing agent feed channel
Control switch A is arranged in A on oxidant feed channel A, supplies in reducing agent feed channel B or in the oxidant
Setting control switch B on the B of channel is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes
Alternating current Jie electricity area B；So that the control switch A is controlled realization by control device and reduction described in feed is continued to the cavity A
Agent and to oxidant described in the interrupted feed of cavity A and also make the control switch B by control device controlled realization to described
Cavity B continues reducing agent described in feed and to oxidant described in the interrupted feed of cavity B, or keeps the control switch A controlled
Device processed control realize oxidant described in feed is continued to the cavity A and to reducing agent described in the interrupted feed of cavity A and
And so that the control switch B is controlled realization by control device and oxidant described in feed is continued to the cavity B and to the cavity B
Reducing agent described in interrupted feed, or so that the control switch A is controlled realization by control device and the cavity A is continued described in feed
Reducing agent and to oxidant agent described in the interrupted feed of cavity A and the control switch B is made to be controlled realization by control device
Oxidant described in feed is continued to the cavity B and to reducing agent described in the interrupted feed of cavity B；The electrochemistry region A
It is work normality that the export of electronics between the electrochemistry region B, which imports,.
A kind of electrochemical appliance of scheme 9., including electrochemistry region A and electrochemistry region B, the electrochemistry region A with also
Former agent is connected to setting, the mixture of the electrochemistry region B and reducing agent and oxidant with the mixture feed channel of oxidant
The connection setting of feed channel, the electrochemistry region A include alternating current Jie electricity area A, and the electrochemistry region B includes alternation electricity
The area Liu Jie electricity B, it is work normality that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is connected to setting, the electrochemistry with the mixture feed channel of reducing agent and oxidant
Region B is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, and mixture feed channel continuous feeding mixture is described
It is work normality that the export of electronics between electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is connected to setting, the electrochemistry with the mixture feed channel of reducing agent and oxidant
Region B is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, and the interrupted feed mixture in mixture feed channel is described
It is work normality that the export of electronics between electrochemistry region A and the electrochemistry region B, which imports,.
A kind of electrochemical appliance of scheme 10., including electrochemistry region A and electrochemistry region B, the electrochemistry region A are set
It sets in cavity A, the cavity A is connected to setting, the electrochemistry region B with the mixture feed channel of reducing agent and oxidant
It is arranged in cavity B, the cavity B is connected to setting, the electrification school district with the mixture feed channel of reducing agent and oxidant
Domain A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, the electrochemistry region A and
It is work normality that the export of electronics between the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the mixture feed of the cavity A and reducing agent and oxidant
Channel connection setting, the electrochemistry region B are arranged in cavity B, the mixture confession of the cavity B and reducing agent and oxidant
Channel connection setting is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current
The area Jie electricity B, mixture feed channel continuous feeding mixture, between the electrochemistry region A and the electrochemistry region B
Electronics export import be work normality；
Or, the electrochemistry region A is arranged in cavity A, the mixture feed of the cavity A and reducing agent and oxidant
Channel connection setting, the electrochemistry region B are arranged in cavity B, the mixture confession of the cavity B and reducing agent and oxidant
Channel connection setting is sent, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current
The area Jie electricity B, the interrupted feed mixture in mixture feed channel, between the electrochemistry region A and the electrochemistry region B
Electronics export import be work normality.
A kind of electrochemical appliance of scheme 11., including electrochemistry region A and electrochemistry region B, the electrochemistry region A and
In the cavity, the cavity is connected to setting with the mixture feed channel of reducing agent and oxidant for the electrochemistry region B setting,
The electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, the electricity
It is work normality that the export of electronics between chemical regions A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity and reducing agent and oxygen
The mixture feed channel of agent is connected to setting, and the electrochemistry region A includes alternating current Jie electricity area A, the electrification school district
Domain B includes alternating current Jie electricity area B, mixture feed channel continuous feeding mixture, the electrochemistry region A and institute
It is work normality that the export for stating the electronics between the B of electrochemistry region, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity and reducing agent and oxygen
The mixture feed channel of agent is connected to setting, and the electrochemistry region A includes alternating current Jie electricity area A, the electrification school district
Domain B includes alternating current Jie electricity area B, the interrupted feed mixture in mixture feed channel, the electrochemistry region A and institute
It is work normality that the export for stating the electronics between the B of electrochemistry region, which imports,.
A kind of electrochemical appliance of scheme 12., including electrochemistry region A and electrochemistry region B, the electrochemistry region A warp
Mixture control switch A is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region B is through mixing
Object control switch B is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes alternation electricity
The area Liu Jie electricity A, the electrochemistry region B include alternating current Jie electricity area B, the electrochemistry region A and the electrochemistry region B
Between electronics export import be work normality；
Or, the electrochemistry region A connects through the mixture feed channel of mixture control switch A and reducing agent and oxidant
Logical setting, the electrochemistry region B are connected to the mixture feed channel of reducing agent and oxidant through mixture control switch B and set
It sets, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, described
Mixture control switch A is controlled by control device realizes mixture feed channel continuous feeding mixture, the mixture
Control switch B by control device controlled realize mixture feed channel continuous feeding mixture, the electrochemistry region A and
It is work normality that the export of electronics between the electrochemistry region B, which imports,；
Or, the electrochemistry region A connects through the mixture feed channel of mixture control switch A and reducing agent and oxidant
Logical setting, the electrochemistry region B are connected to the mixture feed channel of reducing agent and oxidant through mixture control switch B and set
It sets, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes alternating current Jie electricity area B, described
Mixture control switch A is controlled by control device realizes the interrupted feed mixture in mixture feed channel, the mixture
Control switch B by control device controlled realize the interrupted feed mixture in mixture feed channel, the electrochemistry region A and
It is work normality that the export of electronics between the electrochemistry region B, which imports,.
A kind of electrochemical appliance of scheme 13., including electrochemistry region A and electrochemistry region B, the electrochemistry region A are set
It sets in cavity A, the cavity A is connected to the mixture feed channel of reducing agent and oxidant through mixture control switch and sets
It sets, the electrochemistry region B is arranged in cavity B, and the cavity B is mixed through mixture control switch and reducing agent and oxidant
The connection setting of object feed channel is closed, the electrochemistry region A includes alternating current Jie electricity area A, and the electrochemistry region B includes handing over
Time-dependent current Jie electricity area B, it is work normality that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is through mixture control switch and reducing agent and oxygen
The mixture feed channel of agent is connected to setting, and the electrochemistry region B is arranged in cavity B, and the cavity B is through mixture control
System switch is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes that alternating current connects
Electric area A, the electrochemistry region B include alternating current Jie electricity area B, and the mixture control switch is controlled realization by control device
Mixture feed channel continuous feeding mixture, electronics between the electrochemistry region A and the electrochemistry region B
It is work normality that export, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A through mixture control switch A and reducing agent and
The mixture feed channel of oxidant is connected to setting, and the electrochemistry region B is arranged in cavity B, and the cavity B is through mixture
Control switch B is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes alternating current
The area Jie electricity A, the electrochemistry region B include alternating current Jie electricity area B, and the mixture control switch A is controlled by control device
Realize mixture feed channel continuous feeding mixture, the mixture control switch B is controlled by control device realizes institute
Mixture feed channel continuous feeding mixture is stated, the electronics between the electrochemistry region A and the electrochemistry region B is led
Import out is work normality；
Or, the electrochemistry region A is arranged in cavity A, the cavity A is through mixture control switch and reducing agent and oxygen
The mixture feed channel of agent is connected to setting, and the electrochemistry region B is arranged in cavity B, and the cavity B is through mixture control
System switch is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes that alternating current connects
Electric area A, the electrochemistry region B include alternating current Jie electricity area B, and the mixture control switch is controlled realization by control device
The interrupted feed mixture in mixture feed channel, electronics between the electrochemistry region A and the electrochemistry region B
It is work normality that export, which imports,；
Or, the electrochemistry region A is arranged in cavity A, the cavity A through mixture control switch A and reducing agent and
The mixture feed channel of oxidant is connected to setting, and the electrochemistry region B is arranged in cavity B, and the cavity B is through mixture
Control switch B is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes alternating current
The area Jie electricity A, the electrochemistry region B include alternating current Jie electricity area B, and the mixture control switch A is controlled by control device
Realize the interrupted feed mixture in mixture feed channel, the mixture control switch B is controlled by control device realizes institute
The interrupted feed mixture in mixture feed channel is stated, the electronics between the electrochemistry region A and the electrochemistry region B is led
Import out is work normality.
A kind of electrochemical appliance of scheme 14., including electrochemistry region A and electrochemistry region B, the electrochemistry region A and
The electrochemistry region B is arranged in the cavity, mixture of the cavity through mixture control switch Yu reducing agent and oxidant
The connection setting of feed channel, the electrochemistry region A include alternating current Jie electricity area A, and the electrochemistry region B includes alternation electricity
The area Liu Jie electricity B, it is work normality that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity is controlled through mixture
Switch is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, and the mixture control switch is controlled by control device realizes institute
Mixture feed channel continuous feeding mixture is stated, the electronics between the electrochemistry region A and the electrochemistry region B is led
Import out is work normality；
Or, the electrochemistry region A and electrochemistry region B setting is in the cavity, the cavity is controlled through mixture
Switch is connected to setting with the mixture feed channel of reducing agent and oxidant, and the electrochemistry region A includes that alternating current connects electricity
Area A, the electrochemistry region B include alternating current Jie electricity area B, and the mixture control switch is controlled by control device realizes institute
The interrupted feed mixture in mixture feed channel is stated, the electronics between the electrochemistry region A and the electrochemistry region B is led
Import out is work normality.
Scheme 15. is in 1 to 8 on the basis of either a program, further selectively in the reducing agent and the oxidation
Inert substance and/or dead band duration are inserted between agent.
Scheme 16. is in scheme 1 to 15 on the basis of either a program, further selectively by the electrochemistry region A
In the electric field with the setting of power supply electric communication or electrochemistry region A setting, and/or, the electrochemistry region B and power supply are electric
Learn connection setting or electrochemistry region B setting in the electric field；Or, the electrochemistry region A and electrochemistry region B
Between be arranged capacitor, DC power supply, AC power source, alternating source, inductor conductor, inductance coil, charged particle pump, phase transition
Device, reversing switch circuit, rectifier, electric field, oscillating circuit, motor, reversible electric machine, the motor with additional rotation inertia or its
Two conjunctions, its three conjunction, its four conjunction, its five conjunction, its six conjunction, its seven conjunction, its eight conjunction, its
Nine conjunctions, its ten conjunction, its 11 conjunction, the conjunction of its ten binomial, its 13 conjunction, its 14 conjunction, its ten
Five conjunctions.
Scheme 17. on the basis of either a program, further selectively makes the electrochemistry region A in scheme 1 to 16
There is non-electronic conducting electrical relation between the electrochemistry region B, or, the electrochemistry region A is empty through insulation, isolation
Between, in electrolyte, dielectric, capacitor, plasma, ionic liquid, ionized gas, solion and electronic conduction area at least
It is a kind of that there is non-electronic conducting electrical relation with the electrochemistry region B.
Scheme 18. on the basis of either a program, further selectively makes the electrochemistry region A in scheme 1 to 17
Rotation setting, the electrochemistry region B rotation setting.
Aforementioned schemes of the present invention are selectively chosen and are inserted into inert substance between the reducing agent and the oxidant
And/or dead band duration.
In the present invention, it is negative to be selectively chosen the setting on the circuit of the electronics export importing in the electrochemistry region
Load, terminal are electrically connected structure and/or setting power supply.
In the present invention, so-called " inductor conductor " refers to all externally output magnetic force energy and leading from outer absorption magnetic force energy
Body.Such as transformer coil, electrical-coil, conductor bars for dynamoelectric machines etc..
In the present invention, so-called " phase converter " is the direction vector and its voltage for instigating electric current (or charged particle stream)
Angled device, the circuit for example including capacitor, the circuit including inductance and including capacitor also include inductance circuit
Deng.
In the present invention, the principle of electrochemical appliance disclosed in this invention is carried out as described below:
Through detailed analysis, it can be found that there is the basic logic of universality using the process of redox reaction power generation, specifically
Be analyzed as follows: the process to be generated electricity using redox reaction, is exported from reducing agent by electronics, forms reducing agent cation, then
By electronics derived from institute imported into reducing agent cation and oxidant coexistence make three react generate the reducing agent and
The product of the oxidizing reduction reaction externally exports electric energy on the path that electronics export and electronics import.In tradition
In hydrogen-oxygen fuel cell, such as PEMFC, under the effect of the catalyst, hydrogen molecule is separated into proton and electronics, and proton is made to pass through matter
Proton exchange enters the oxygen side with catalyst, and electronics is loaded from hydrogen side and imported into proton and what oxygen coexisted has catalyst
Oxygen side, proton (H+), oxygen (O2) and electronics (e-) reaction generation water.This means that the process to be generated electricity using redox reaction
With following basic logic: electronics is made into reducing agent positively ionized from reducing agent export, then by electronics imported into reducing agent just from
The coexistence of son and oxidant makes reducing agent cation, oxidant and electronics three react the generation reducing agent and the oxidation
The product of agent redox reaction, this overall process is external output electric energy, and the output of electric energy is leading by electronics
Realization is imported out.This basic logic is it is meant that we can not be by the constraint of conventional fuel cell concrete form, as long as full
The requirement of this basic logic of foot, so that it may externally export electric energy using the redox reaction of Oxidizing and Reducing Agents.And this
The basic process of the disclosed device of invention is exactly so that reducing agent is formed reducing agent cation from electrochemistry region A export electronics,
Electronics is imported to the electrochemistry region B, then electronics is made to imported into the electrochemistry region A from the electrochemistry region B, in institute
It states electrochemistry region A electronics, oxidant and the reducing agent cation three to coexist, in the electrochemistry region B electronics, oxidation
Agent and the reducing agent cation three coexist, to make electronics and Oxidizing and Reducing Agents cation three reacts generation
The product of the oxidant and the reducing agent redox reaction, and then there are no lead the reducing agent cation in fact
It is externally defeated also under the premise of there is no by necessity derived from other non-electronic charged particles under the premise of necessity out
Electric energy out.
Disclosed in this invention include reducing agent, oxidant alternating action device principle it is as follows: utilize electrochemistry
Region A alternately contacts or makes reducing agent and oxidant alternately to contact with electrochemistry region A with reducing agent and oxidant, utilizes electricity
Chemical regions B is alternately contacted with Oxidizing and Reducing Agents or is contacted Oxidizing and Reducing Agents alternately with electrochemistry region B, is made also
Former agent generates positive charged particle and electronics in the electrochemistry region A, and electronics is made to export to the electricity from the electrochemistry region A
Chemical regions B, the oxidant described in the electrochemistry region B coexist with electronics, make the reducing agent in the electrochemistry region B
The positive charged particle and electronics are generated, so that electronics is imported into the electrochemistry region A from the electrochemistry region B, described
Positive charged particle, the oxidant described in the A of electrochemistry region and electron reaction generate the reducing agent and the oxidant reaction
Product, positive charged particle, the oxidant described in the electrochemistry region B and electron reaction generate the reducing agent and
The product of the oxidant reaction is led using the export of the electronics between the electrochemistry region A and the electrochemistry region B
Enter realize output electric energy and/or absorb electric energy, so recycle, realization continue working process (from the electrochemistry region A to
When the electrochemistry region B imports electronics, in some cases, electronics is generated in the electrochemistry region B and oxidant reaction
Negative charged particles C, the negative charged particles C generate the reduction in the electrochemistry region B and the positive charged particle reaction
The product that agent and the oxidant react utilizes the electronics between the electrochemistry region A and the electrochemistry region B
Export import realize output electric energy and/or absorb electric energy, so recycle, realization continue working process).Realizing this electrification
It during, is selectively chosen, the electrochemistry region A, external circuit, capacitor and the electrochemistry region B are constituted back
Road and/or the electrochemistry region A, external circuit, non-electronic charged particle oscillation area and the electrochemistry region B are constituted back
Road.In this device, electro ultrafiltration can be implemented to the electrochemistry region A and electrochemistry region B, electro ultrafiltration can be controlled
The export and/or importing of system and strengthening electronic, thus it is possible to prevente effectively from reducing agent and oxidant mixing directly aoxidize
Reduction reaction improves safety, reliability and efficiency.It, can also be in the electrochemistry region A and the electricity in this device
First implement electro ultrafiltration to it before chemical regions B and material effect, purpose is also that reducing agent and oxidant is avoided to mix directly
Redox reaction occurs, improves safety, reliability and efficiency.
Disclosed in this invention include reducing agent and oxidant mixture effect device principle it is as follows: utilize electricity
Chemical regions A contacts with the mixture of reducing agent and oxidant or makes the mixture of reducing agent and oxidant and electrochemistry region A
Contact, contacted or made with the mixture of reducing agent and oxidant using electrochemistry region B the mixture of reducing agent and oxidant and
Electrochemistry region B contact, makes electronics export to the electrochemistry region B from the electrochemistry region A, and then make using electro ultrafiltration
The reducing agent forms positive charged particle in the electrochemistry region A, from the electrochemistry region B to the electrochemistry region A
Electronics is imported, the reducing agent generates the positive charged particle in the electrochemistry region B, described in the electrochemistry region A
Positive charged particle, the oxidant and electron reaction generate the reducing agent and the oxidant reaction product, in the electricity
Positive charged particle, the oxidant described in chemical regions B and electron reaction generate the reducing agent and the oxidant reaction is raw
At object, electricity is absorbed on the channel of electronics export and/or importing between the electrochemistry region A and the electrochemistry region B
Can and/or output electric energy, so recycle, realization continue working process (in some cases, from the electrochemistry region A to
The electrochemistry region B imports the oxidant and electron reaction when electronics and generates negative charged particles C, from the electrochemistry region
B generates negative charged particles C to oxidant described in the electrochemistry region A and electron reaction, described in the electrochemistry region A just
Charged particle and negative charged particles C reaction generate the reaction product of the reducing agent and the oxidant, in the electricity
Positive charged particle described in chemical regions B and negative charged particles C reaction generate the reaction of the reducing agent and the oxidant
Product, between the electrochemistry region A and the electrochemistry region B electronics export and/or import channel on absorb
Electric energy and/or output electric energy, so recycle, realization continues working process).It is alternative in realizing this electrochemical process
Ground selection, the electrochemistry region A, external circuit, capacitor and the electrochemistry region B constitute circuit and/or the electrochemical school district
Domain A, external circuit, non-electronic charged particle oscillation area and the electrochemistry region B constitute circuit.It is effective in this device
Ground avoids the reducing agent and the oxidant from mixing redox reaction directly occurs, can in the electrochemistry region A and
The electrochemistry region B first implements electro ultrafiltration to it with before material effect.
Disclosed in this invention include reducing agent and oxidant the principle of device that discontinuously acts on of mixture it is as follows: remove
Outside the influence discontinuously acted on, the principle of the present apparatus and the principle of the device for the mixture effect for including reducing agent and oxidant are complete
It is identical, and interrupted function is that can be better protected from or eliminate reducing agent described in mixture and the oxidant in electricity
It is anti-that redox is directly carried out in the case where pole participation (the i.e. described electrochemistry region A and/or the electrochemistry region B are participated in)
The ability of output electric energy should be lost, and then improves the efficiency of device disclosed in this invention, such as following reducing agents and oxidant are mixed
It closes object discontinuously to act on shown in working principle diagram, under the influence of mixture discontinuously acts on, a certain electrode may be implemented and only exist also
Former agent (except non-electronic charged particle) functions, and another electrode only exist oxidant (except non-electronic charged particle) with
Its state acted on, or the high concentration object (except non-electronic charged particle) for realizing that a certain electrode only exists reducing agent are made with it
With, and another electrode only exists the state that the high concentration object (except non-electronic charged particle) of oxidant functions, either
Any state among these is all conducive to the efficiency for promoting electrochemical reaction.Certainly as described above, being selectively chosen makes
Step is imported with the export of external means (such as foreign current, external electrical field etc.) control electronics, promotes the effect of electrochemical reaction
Rate.Similarly, it in realizing this electrochemical process, is selectively chosen, the electrochemistry region A, external circuit, capacitor and institute
It states electrochemistry region B and constitutes circuit and/or the electrochemistry region A, external circuit, non-electronic charged particle oscillation area and described
Electrochemistry region B constitutes circuit.
In the present invention, the partial circuit working principle of the electrical return of disclosed device is to utilize non-electronic band electrochondria
Sub reciprocating vibration in the electrolyte, which is realized alternation conducting and/or stood facing each other using non-electronic charged particle with electronics, realizes that alternation is led
It is logical, and then interior circuit and external circuit is made to form closed circuit, realize electrochemical process.
In the present invention, it is that work is normal that the export of the electronics between the electrochemistry region A and the electrochemistry region B, which imports,
State.
In the present invention, so-called " export of the electronics between the electrochemistry region A and the electrochemistry region B is imported
For the normality that works " refer to electronics from the electrochemistry region A to the electrochemistry region B and electronics from the electrochemistry region B
It is imported to the export of the electrochemistry region A to continue working process, i.e., electrochemical appliance disclosed in this invention is in work shape
When state, electronics is imported from electrochemistry region A export electronics, Xiang Suoshu electrochemistry region B, is led from the electrochemistry region B
Out electronics and to the electrochemistry region A import electronics be a kind of lasting course of work.In other words, the electrochemistry region
The A and electrochemistry region the B corresponding and described electrochemistry region A and electrochemistry region B and alternation electricity with alternating current
Stream is opposite to should be the process of continuing working.
In the present invention, when the reducing agent and the oxidant are certain two kinds of predetermined substance, electrochemical reaction is being realized
In the process, having the reaction of the third substance participation cyclicity, (so-called cyclicity reaction, which refers to, generates certain at an electrode
Substance, and the reaction that this substance is consumed at another electrode), such as the reducing agent is methanol, the oxidant is
When oxygen, in acid condition, water is had as the third substance and participates in cyclicity reaction, is i.e. water produces at the electrode for absorbing electronics
It is raw, and be consumed at the electrode of output electronics, and under alkaline condition, hydroxyl, which is had, as the third substance participates in recycling
Property reaction, hydroxyl absorb electronics electrode at generate, output electronics electrode at be consumed.For example, methanol fuel is electric
The electrochemical reaction process concrete condition in pond is as follows:
Overall reaction under alkaline condition: 2CH3OH+3O2+4OH-=2CO3 2-+6H2O
Anode reaction: O2+4e-+2H2O=4OH-
Negative reaction: CH3OH-6e-+8OH-=CO3 2-+6H2O
Overall reaction in acid condition: 2CH3OH+3O2=2CO2+4H2O
Anode reaction: O2+4e-+4H+=2H2O
Negative reaction: CH3OH-6e-+H2O=6H++CO2
For another example the electrochemical reaction process concrete condition of methane fuel cell is as follows:
Overall reaction under alkaline condition: CH4+2O2+2OH-=CO3 2-+3H2O
Anode reaction: 2O2+8e-+4H2O=8OH-
Negative reaction: CH4-8e-+10OH-=CO3 2-+7H2O
Overall reaction in acid condition: CH4+2O2=CO2+2H2O
Anode reaction: 2O2+8e-+8H+=4H2O
Negative reaction: CH4-8e-+2H2O=8H++CO2
In the present invention, according to device disclosed in this invention, substance and electrode (such as electrochemistry region A or electrochemical school district
Domain B) effect prior to electricity and the effect of electrode, the due electrochemical process of the present invention may be implemented in this form completely, but
It is that reducing agent and oxidant will appear exist simultaneously at same electrode (especially with reducing agent and oxidation in many cases
When the mixture of agent), if this state is precisely that startup stage or electrode did not had in the period of electro ultrafiltration, at this moment reducing agent
And the conversion process between redox reaction forfeiture and electric energy can directly occur for oxidant, in order to avoid this state generates,
Be selectively chosen in advance to electrode implement electro ultrafiltration, and it is so-called " to participate in electrochemical reaction region apply electro ultrafiltration,
So that participate in electrochemical reaction substance be difficult to directly carry out redox reaction " purpose be that this.
In the present invention, under certain temperature and/or pressure, so-called electrochemistry region A, which is selectively chosen, to be set as not
Conductive region including catalyst, because it is anti-can still to carry out electrochemistry without using catalyst under certain temperature and/or pressure
It answers.
In the present invention, under certain temperature and/or pressure, so-called electrochemistry region B, which is selectively chosen, to be set as not
Conductive region including catalyst, because it is anti-can still to carry out electrochemistry without using catalyst under certain temperature and/or pressure
It answers.
In the present invention, so-called catalytic domain is selectively chosen under certain temperature and/or pressure and is set as not including urging
The region of agent, because high temperature and pressure is also a kind of catalytic process for promoting reaction.
In the present invention, it is selectively chosen to the electrochemistry region (such as electrochemistry region A or electrochemistry region B)
Apply electro ultrafiltration, to realize the electro ultrafiltration to the electrochemistry region prior to mutual between substance and the electrochemistry region
Effect, and then reducing agent and oxidant is reduced or avoided and directly carries out the case where redox reaction loses output electric energy.
It is non-electronic having including the electrochemistry region A through electronic conduction area and the electrochemistry region B in the present invention
In the device that electrical relation is connected, it is selectively chosen one made in the electrochemistry region A and the electrochemistry region B
Through capacitor or through non-electronic conducting area (such as the electrolyte such as proton exchange membrane) again through external circuit and another electric communication, so
Normality work may be implemented.
In the present invention, so that charged particle is stored in the means in electrochemistry region as realizing, be selectively chosen and pass through
The alternating of the contact of two kinds of metabolies and electric current that make electrochemistry region and participation electrochemical reaction changes to realize, also optional
Select to selecting property to make that two kinds of substances for participating in electrochemical reaction alternately contacts with electrochemistry region and the alternating of electric current changes
It realizes, however the non-electronic charged particle between two electrodes of electrochemical reaction (such as electrochemistry region A and electrochemistry region B)
Conducting may or may not then exist.
In the present invention, charged particle is set to be stored in the means in electrochemistry region as realizing, being selectively chosen makes electricity
The mixture contact of two kinds of substances of chemical regions and participation electrochemical reaction and the alternating of electric current change to realize, may be selected
Property select to make electrochemistry region and participate in the mixture makes discontinuous contact of two kinds of substances of electrochemical reaction and the alternating of electric current
Variation is to realize, however the non-electronic band between two electrodes of electrochemical reaction (such as electrochemistry region A and electrochemistry region B)
The conducting of charged particle may or may not then exist.
In the present invention, it is that the Q generated at P is instigated to be stored in institute that the so-called Q for making the generation at P, which is stored at the P,
The electrode zone represented at P is stated, including the Q to be unnecessarily transmitted to the electrode zone polarity with representative at the P
The process of opposite electrode zone.
In the present invention, in realizing the chemical energy device for converting electric energy, need for certain charged particle to be stored in a certain
It is waited in region and participates in reaction in the next step, it is to instigate to produce at P that the so-called Q for making the generation at P, which is stored at the P,
Raw Q is stored in the electrode zone represented at the P, including being unnecessarily transmitted to the Q and representative at the P
The process of the opposite polarity electrode zone of electrode zone.
In the present invention, the reducing agent used in the electrochemical appliance and oxidant are with the reducing agent and the oxidation
In the presence of the form of the mixture of agent, rubbing with the reducing agent and the oxidant further can be selectively selected
You exist than the form of mixture, or to deposit in the form of the mixture of the explosion limit reducing agent below and the oxidant
, or to exist in the form of the mixture of the local explosion limit reducing agent below and the oxidant, or with pole of exploding
The form of the mixture of above reducing agent of limit and the oxidant exists, or with described in more than local explosion limit also
The form of the mixture of former agent and the oxidant exists.
In the present invention, the mixture of so-called reducing agent and oxidant further can selectively select to be set as reducing agent and
Molar mixture, the explosion limit reducing agent below and the mixture of oxidant, local explosion limit of oxidant are below
It is more than the mixture of more than mixture of reducing agent and oxidant, explosion limit reducing agent and oxidant or local explosion limit
Reducing agent and oxidant mixture.
In the present invention, so-called molar mixture refers to that the molar concentration rate of mixture is positive and negative in chemical reaction molar ratio
Mixture within 10%.
In the present invention, the export importing of the electronics of the electrochemistry region A and the electrochemistry region B refers to not include electricity
The appearance and accumulation of electronics in sub- separation process.
In the present invention, the export of the electronics of the electrochemistry region A is imported to continue working process.
In the present invention, the export of the electronics of the electrochemistry region B is imported to continue working process.
In the present invention, electrochemistry region A state corresponding with alternating electromotive force and alternating current is to continue working
Process.
In the present invention, electrochemistry region B state corresponding with alternating electromotive force and alternating current is to continue working
Process.
The electrochemical appliance disclosed in this invention is corresponding with alternating electromotive force and alternating current, i.e. electrochemistry region
It is corresponding with alternating electromotive force and alternating current.
In the present invention, relationship is connected for the electricity that non-electronic charged particle is formed, is selectively chosen through non-electronic
Relationship is connected in the direct electricity that charged particle is formed, and relationship, warp is connected in the electricity formed through non-electronic charged particle reciprocating vibration
One of electricity conducting relationship that capacitance relation is formed, secondly conjunction or thirdly conjunction.
In the present invention, relationship is connected for the electricity that non-electronic charged particle is formed, is selectively chosen including through exhausted
The electrical relation that alternating current can be made to be connected of edge body, dielectric and the conducting body isolation of non-electronic charged particle.
In the present invention, in the device between two electrodes (such as electrochemistry region A and electrochemistry region B) there are electrolyte,
Being selectively chosen makes non-electronic charged particle that can both pass through electrolyte, reaches another electrode from an electrode, can also be
Reciprocating vibration realizes the effect of alternating current conducting in electrolyte.
In the present invention, electrochemistry region corresponding with alternating electromotive force and alternating current is essence feature of the invention,
In the present invention, two kinds of substances due to participating in electrochemical reaction exist with same electrochemistry region to be contacted, and electrochemistry region
Corresponding with alternating electromotive force and alternating current, i.e., the electromotive force in the electrochemistry region in the present invention is alternating electromotive force, is absorbed
And/or the electric current of output electric energy is alternating current, and this is through the lasting sex work normality of whole work process, it is this to hold
Continuous sex work normality eliminates the necessity of non-electronic charged particle transmission between two electrodes, therefore no matter makes to be in electricity between two electrodes
Sub- state of isolation, non-electronic charged particle state of isolation have the shape for the electrolyte that non-electronic charged particle is connected between two electrodes
State is in other states, as long as can be realized the Oscillating flow of electronics, can work normally.There is electricity between two electrodes
In the device for solving matter, non-electronic charged particle can both pass through electrolyte, reach another electrode from an electrode, can also be electrolysed
Reciprocating vibration realizes the effect of alternating current conducting in matter.This provides brand-new approach for the manufacture and use of fuel cell.
In the present invention, the alternation of electric current and substance replace and the effect of the alternation and mixture of substances of electric current is formed by
Alternation process is a kind of lasting course of work, is a kind of work normality, and its purpose is to eliminate non-electronic band
Charged particle two interelectrode transmitting necessity, to promote the science that chemical energy exchanges the electrochemical appliance of electric energy for, in turn
Promote service life, reliability, low cost and the efficiency of electrochemical appliance corresponding with device disclosed in this invention.This electricity
The purpose of principle and purpose of chemical devices and conventional fuel cell are catalyst regeneration is temporary to exchange Oxidizing and Reducing Agents
Feed channel, which forms the principle of temporary electrode change in polarity and purpose, has essential distinction, also and to prevent, weaken and remove
The principle and purpose of the frequently pole-reversing electroosmosis of electrode attachment have essential distinction.
In the present invention, from a certain region export electronic processes duration with to this region import electronic processes duration it
Than between 1/6 and 6, between 1/5 and 5, between 1/4 and 4, between 1/3 and 3, between 1/2.5 and 2.5,1/2
And between 2, between 1/1.5 and 1.5, between 1/1.3 and 1.3, between 1/1.2 and 1.2 or 1/1.1 and 1.1 it
Between, or it is equal with the duration of electronic processes is imported to this region from the duration of a certain region export electronic processes.
In the present invention, during the export of electronics imports, electro ultrafiltration can be used；Or, the export in electronics imports
During, it is selectively chosen using capacitor, DC power supply, AC power source, alternating source, inductor conductor, inductor wire
Circle, motor, reversible electric machine, has charged particle pump, phase converter, reversing switch circuit, rectifier, electric field, oscillating circuit
The motor of additional rotation inertia or its two conjunction, its three conjunction, its four conjunction, its five conjunction, its six conjunction, its
Seven conjunctions, its eight conjunction, its nine conjunction, its ten conjunction, its 11 conjunction, the conjunction of its ten binomial, its 13
Conjunction, its 14 conjunction, its 15 conjunction.
In the present invention, during exporting electric energy and/or absorbing electric energy, selectively selection uses electro ultrafiltration；Or,
During exporting electric energy and/or absorbing electric energy, selectively selection uses capacitor, DC power supply, AC power source, alternation electricity
Source, inductor conductor, inductance coil, charged particle pump, phase converter, reversing switch circuit, rectifier, electric field, oscillating circuit,
Motor, reversible electric machine, the motor with additional rotation inertia or its two conjunction, its three conjunction, its four conjunction, its five
Conjunction, its six conjunction, its seven conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11 conjunction, its ten
The conjunction of binomial, its 13 conjunction, its 14 conjunction, its 15 conjunction.
In the present invention, the purpose of so-called " during exporting electric energy and/or absorbing electric energy, using electro ultrafiltration " is benefit
The process of output electric energy is controlled or strengthened with electro ultrafiltration and/or absorbs the process of electric energy, in this way can with the efficiency of lifting process and
Safety, such as an electrochemical process may take a long time to complete, but if can be made using electric process
The reaction rate of the slower procedure segment of electrochemical reaction rates is promoted, and then is improved efficiency.
In the present invention, so-called electro ultrafiltration, which refers to, makes it to charged particle (such as electronics) application using electric field, electric current etc.
The effect for being subjected to displacement and/or flowing.
In the present invention, it is more big more be conducive to electricity that the electrochemistry region A and the electrochemistry region B are formed by capacitance
The promotion of density is chemically reacted, therefore when being electrochemically reacted using device disclosed in this invention, the electrification should be made
Capacitance between school district domain A and the electrochemistry region B increases as much as possible.
It, can be described in order to increase the capacitance between the electrochemistry region A and the electrochemistry region B in the present invention
Plasma, ionic liquid, ionized gas or solion are set between electrochemistry region A and the electrochemistry region B, and made
Ion vibrates between the electrochemistry region A and the electrochemistry region B, and/or oscillates around in the electrochemistry region A
And oscillated around in the electrochemistry region B, to realize the electricity between increasing the electrochemistry region A and electrochemistry region B
The purpose of capacity.
In the present invention, the bigger between the electrochemistry region A and the electrochemistry region B be formed by capacitance the more advantageous
In the promotion of electrochemical reaction density, therefore when being electrochemically reacted using device disclosed in this invention, should make described
Capacitance between electrochemistry region A and the electrochemistry region B increases as much as possible.
In the present invention, to realize that specific charged particle is stored in electrochemistry region, need to join the electrochemistry region
Alternate change physical environment or make the electrochemistry region between the different material of electrochemical reaction and participate in electrochemical reaction
The mixture of different material contacts, and is just able to achieve.Fundamentally, as long as the electrochemistry region is made to participate in electrochemical reaction
Different material between alternate change physical environment or make the electrochemistry region and participate in the mixed of the different material of electrochemical reaction
Object contact is closed, can be achieved with the purpose that the specific charged particle is stored in electrochemistry region, no matter the electrochemistry region has
There are two types of the conductive channel of charged particle, (such as one of is proton conductive channel, i.e. there is conducting certain band between two electrodes
The electrolyte of charged particle, another kind be electronic conduction channel) or the electrochemistry region there was only electronic conduction channel, change sentence
It talks about, as long as making the electrochemistry region alternate change physical environment or described between the different material for participating in electrochemical reaction
Electrochemistry region is contacted with the mixture for the different material for participating in electrochemical reaction, can be achieved with the specific charged particle storage
Participate in the purpose that electrochemical reaction is realized in reaction in electrochemistry region and in the next step, no matter two electrodes (such as electrochemistry
Region A and electrochemistry region B) between whether there is electrolyte.
In the present invention, in electrochemistry region, tool there are two types of the conductive channel of charged particle, (such as lead for proton by one of which
, i.e. there is the electrolyte that specific charged particle is connected between two electrodes in circulation passage, another kind is electronic conduction channel) electrochemistry dress
In setting, alternate change physical environment or made described between the different material for participating in electrochemical reaction by making the electrochemistry region
Electrochemistry region is contacted with the mixture for the different material for participating in electrochemical reaction, can be achieved to eliminate from the electrochemistry region
The necessity for removing the non-electronic charged particle generated in the electrochemistry region, can also realize that non-electronic charged particle is stored in
The electrochemistry region and the purpose for participating in reaction realization electrochemical reaction in the next step.The alternate change of physical environment or
The electrochemistry region and the mixture for the different material for participating in electrochemical reaction are contacted, can make to be stored in the electrochemical school district
Non-electronic charged particle in domain participates in reacting in the next step, realizes electrochemical process, therefore from the electrochemical school district
The necessity that non-electronic charged particle is exported in domain completely disappears.The case where necessity derived from non-electronic charged particle disappears
Under, although some non-electronic charged particle that ought to be stored in the electrochemistry region is exported, also have non-electronic
Charged particle is stored in the electrochemistry region and waits next reaction step, in other words, if the electrochemistry region
The alternate change physical environment between the different material for participating in electrochemical reaction, or it is mixed with the different material of participation electrochemical reaction
Object contact is closed, although there are electrolyte between two electrodes (such as electrochemistry region A and electrochemistry region B), is also had non-electronic
Charged particle is stored in the electrochemistry region and participation reaction in the next step is waited to realize electrochemical reaction process.
Electrochemical appliance disclosed in this invention, it is negative there are electrolyte can be reduced in the case where electrolyte between two electrodes
Lotus extends its service life and is conducive to the balance and stability operation of system.
In the present invention, in the device that electrochemistry region only has electronic conduction channel (the i.e. described electrochemistry region A with it is described
Interior circuit or external circuit between the B of electrochemistry region are in electronics and non-electronic charged particle state of isolation), the electrochemistry region
Alternate change physical environment and the electrochemistry region and participation electrochemical reaction between the different material for participating in electrochemical reaction
Different material mixture contact, so that non-electronic charged particle is stored in the electrochemistry region, physical environment changes
Becoming or contacting the electrochemistry region with the mixture for the different material for participating in electrochemical reaction can make to be stored in the electrification
The non-electronic charged particle in school district domain participates in reaction in the next step and realizes electrochemical process, that is, eliminates from electrochemical school district
Domain removes the necessity of non-electronic charged particle.Express herein, in conventional electrochemical device, electrochemistry region (i.e. electrode) extremely
It less include two kinds of charged particle conductings, such as an electronic conduction channel, a proton conductive channel.
For electrochemical appliance disclosed in this invention in specific work process, the different step that the export of electronics imports can be with
The case where in the presence of output electric energy and absorbing electric energy, but its summation is output electric energy.
Electrochemical appliance disclosed in this invention self-evidently includes the participation of substance.
Electrochemical appliance disclosed in this invention is in use, oxidant alternative selection is set as: oxygen, compression are empty
Gas, oxygen, liquid oxygen, air, liquefied air, fluorine, chlorine, bromine, iodine, ozone, nitric acid, the concentrated sulfuric acid, hypochlorous acid, chromic acid, Peracetic acid,
Perchloric acid, chlorate, nitrate, permanganate, perchlorate, bichromate, Calcium perchlorate, ammonium perchlorate, sodium perchlorate, height
Potassium chlorate, lithium perchlorate, magnesium perchlorate, barium perchlorate, perchloric acid strontium, silver perchlorate, ammonium chlorate, sodium chlorate, potassium chlorate, chloric acid
Magnesium, calcium chlorate, copper chlorate, zinc chlorate, chloric acid thallium, silver chlorate, potassium permanganate, acerdol, barium permanganate, lithium nitrate, nitric acid
Sodium, potassium nitrate, calcium nitrate, cesium nitrate, beryllium nitrate, potassium bromate, zinc bromate, ammonium periodate, calcium iodate, iron iodate, sodium dichromate,
Potassium bichromate, iron chloride, ammonium ceric nitrate, sodium hypochlorite, SODIUM PERCARBONATE, sodium perborate, calcium hypochlorite, sodium dichloro cyanurate,
Copper oxide, di-iron trioxide, sodium peroxide, manganese dioxide, nitrogen dioxide, potassium peroxide, magnesium dioxide, calcium dioxide, peroxide
Change hydrogen, chromium trioxide, strontium dioxide, sodium dioxide, silver oxide, acetone, acrylonitrile, benzaldehyde, dibenzoyl peroxide, benzene
Quinone, carbon tetrabromide are set as chloramines etc.；Reducing agent alternative selection is set as: hydrogen, alkane, alkene, alkynes, aromatic hydrocarbon,
Halogenated hydrocarbons, alcohol compound, phenolic compound, aldehyde compound, ketone compounds, hydroxyl acid compounds, ester type compound,
Sodium, aluminium, zinc, lithium, potassium, magnesium, manganese, carbon, calcium, barium, vanadium, chromium, iron, cobalt, copper, boron, silicon, phosphorus, tin, mercury, lead, carbon dust, coal dust end,
Sulphur, lithium aluminium hydride reduction, diethyl aluminium hydride sodium, sodium borohydride, potassium borohydride, carbon monoxide, hydrogen sulfide, hydrazine, ammonia, hydrogen chloride,
Hydrogen iodide, sulfur dioxide, hydrogen peroxide, vulcanized sodium, stannous chloride, formaldehyde, sulfurous acid, sulfuric acid, oxalic acid, ethyl alcohol, sodium sulfite,
Sodium hydrogensulfite, ferrous sulfate, methanol, natural gas, coal gas, methane, coke, diesel oil, dimethyl ether, kerosene, gasoline, hydrogen one aoxidize
Carbon mix is set as heavy oil etc..
In the present invention, electrochemical action may be present between the reducing agent and the oxidant.
In the present invention, the reducing agent and the oxidant, can under conditions of electrochemical appliance disclosed in this invention
Electrochemical reaction occurs.
In the present invention, the reducing agent is simple substance, compound or mixture, and ion or solion are not belonging to the reduction
Agent.
In the present invention, the oxidant is simple substance, compound or mixture, and ion or solion are not belonging to the oxidation
Agent.
Electrochemical appliance disclosed in this invention is in the nature chemical energy device for converting electric energy.
It is so-called " during electronics exports and/or imports, to use capacitor, DC power supply, alternating current in the present invention
Source, alternating source, inductor conductor, inductance coil, charged particle pump, phase converter, reversing switch circuit, rectifier, electric field,
Oscillating circuit, motor, reversible electric machine, the motor with additional rotation inertia or its two conjunction, its three conjunction, its four it
Conjunction, its five conjunction, its six conjunction, its seven conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11
Conjunction, its ten binomial conjunction, its 13 conjunction, its 14 conjunction, its 15 conjunction " purpose be by electro ultrafiltration control
The export of system and/or strengthening electronic imports.
It is so-called " during electronics exports and/or imports, to use capacitor, DC power supply, alternating current in the present invention
Source, alternating source, inductor conductor, inductance coil, charged particle pump, phase converter, reversing switch circuit, rectifier, electric field,
Oscillating circuit, motor, reversible electric machine, the motor with additional rotation inertia or its two conjunction, its three conjunction, its four it
Conjunction, its five conjunction, its six conjunction, its seven conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11
Conjunction, its ten binomial conjunction, its 13 conjunction, its 14 conjunction, its 15 conjunction " purpose be by electro ultrafiltration control
The export of system and/or strengthening electronic imports, and control and/or the export of strengthening electronic importing can effectively avoid reducing agent and oxidation
Redox reaction directly occurs for agent mixing, improves safety, reliability and efficiency, and control and/or strengthening electronic are led
Safety, reliability and the effect that can be effectively promoted using reducing agent and oxidant existing device as a mixture are imported out
Rate.
In the present invention, " during electronics exports and/or imports, capacitor, DC power supply, AC power source, alternation are used
Power supply, inductor conductor, inductance coil, charged particle pump, phase converter, reversing switch circuit, rectifier, electric field, oscillation electricity
Road, motor, reversible electric machine, the motor with additional rotation inertia or its two conjunction, its three conjunction, its four conjunction, its
Five conjunctions, its six conjunction, its seven conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11 conjunction,
The purpose of the conjunction of its ten binomial, its 13 conjunction, its 14 conjunction, its 15 conjunction " be by electro ultrafiltration control and/
Or the export of strengthening electronic imports.A certain step in this control process is power consumption, but whole process is power supply.
Electrochemical appliance of the present invention " is exported and/or is led in electronics when using the mixture of reducing agent and oxidant
During entering, pumped using capacitor, DC power supply, AC power source, alternating source, inductor conductor, inductance coil, charged particle,
Phase converter, reversing switch circuit, rectifier, electric field, oscillating circuit, motor, reversible electric machine, with additional rotation inertia
Motor or its two conjunction, its three conjunction, its four conjunction, its five conjunction, its six conjunction, its seven conjunction, its eight
The conjunction of item, its nine conjunction, its ten conjunction, its 11 conjunction, the conjunction of its ten binomial, its 13 conjunction, its 14
Conjunction, its 15 conjunction " purpose be not only to control by electro ultrafiltration and/or the export of strengthening electronic imports, and be logical
The export for crossing strengthening electronic imports the effective means for preventing reducing agent and oxidant from directly carrying out redox reaction.This control
A certain step in the process is power consumption, but whole process is power supply.
In the present invention, " during electronics exports and/or imports, capacitor, DC power supply, AC power source, alternation are used
Power supply, inductor conductor, inductance coil, charged particle pump, phase converter, reversing switch circuit, rectifier, electric field, oscillation electricity
Road, motor, reversible electric machine, the motor with additional rotation inertia or its two conjunction, its three conjunction, its four conjunction, its
Five conjunctions, its six conjunction, its seven conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11 conjunction,
The purpose of the conjunction of its ten binomial, its 13 conjunction, its 14 conjunction, its 15 conjunction " is not only through electro ultrafiltration control
The export of system and/or strengthening electronic imports, and is to prevent reducing agent and oxidant direct by the export importing of strengthening electronic
Carry out the effective means of redox reaction.A certain step in this control process is power consumption, but whole process is power supply
's.
It in the present invention, further can selectively select that catalyst corresponding with the reducing agent is made to be set as catalyst A, with
It is different that the corresponding catalyst of the oxidant is set as catalyst B, the catalyst A and the catalyst B, in this case,
Catalyst in the electrochemistry region, which is selectively chosen, is set as the random mixed of the catalyst A and catalyst B
Select the catalyst A for being set as contacting near catalytic domain with closing the catalyst choice in object or the electrochemistry region
The band electrochondria between the catalyst A and the catalyst B can be increased with the mixture of the catalyst B in order to improve efficiency
The mobility of son.
In the present invention, the purpose for being inserted into the inert substance is to evade the reducing agent and the oxidant described
Exist while at electrochemistry region, or the reduction reducing agent and the oxidant exist simultaneously at the electrochemistry region
Chance.
In the present invention, the electrochemistry region A alternative selects one of the electrode for being set as electrochemical reaction or electrode
Point, the electrochemistry region B alternative selection is set as the electrode of electrochemical reaction or a part of electrode.
It, can be according to the operating temperature of the property and the electrochemistry region of the reducing agent and the oxidant in the present invention
Select different catalyst.
In the present invention, Xiang Suoshu electrochemistry region import concentration proportion in the local explosion limit reducing agent below and
The mixture of the oxidant may include fire retardant, such as nitrogen, carbon dioxide etc. are added in the mixture of hydrogen and oxygen.
In the present invention, in the device that the electrochemistry region is under set temperature, the set temperature can be set as high
In equal to 100 DEG C.
In the present invention, in the device that the electrochemistry region is under set temperature, the set temperature can be set as low
In equal to 90 DEG C.
In the present invention, the reducing agent and the oxidant are to refer to that electrochemical reaction occurs in the electrochemistry region
Substance.
In the present invention, it can react after the reducing agent and oxidant absorption electric energy and generate compound, or right
It can react after outer feed electric energy and generate compound.
In the present invention, in the device for including AC power source, the reaction of the reducing agent and the oxidant can be suction
The reaction for receiving electric energy is also possible to export the reaction of electric energy, but generally exports electric energy.
In the present invention, in the device for including alternating source, the reaction of the reducing agent and the oxidant can be suction
The reaction for receiving electric energy is also possible to export the reaction of electric energy, but generally exports electric energy.
In the present invention, eliminating from the necessity that electrochemistry region removes non-electronic charged particle means only to need to remove electricity
Son, rather than electronics charged particle (such as proton) can store in the electrochemistry region that it is generated and the participation electricity during next
Chemical reaction, it means that It is not necessary to the interior circuit or outer that centainly there is non-electronic charged particle channel to constitute between two electrodes
Circuit, it is only necessary to which electrochemical process can be realized in electronic conduction circuit, in this device, is selectively chosen electricity in it
The conducting on road is that the reciprocating vibration of charged particle in capacitor and/or its internal part by being formed between its internal part is realized
, and using external circuit output electric energy and/or absorb electric energy.
In the present invention, eliminating from the necessity that electrochemistry region removes two kinds of charged particles means only to need to remove electricity
Son, and another charged particle (such as proton) can store in the electrochemistry region that it is generated and the participation electricity during next
Chemical reaction, it means that It is not necessary to the interior circuit or outer that centainly there is non-electronic charged particle channel to constitute between two electrodes
Circuit, it is only necessary to which electrochemical process can be realized in electronic conduction circuit, and in this device, the conducting of interior circuit is to pass through
The reciprocating vibration of charged particle is realized in the capacitor and/or its internal part formed between its internal part, and utilizes dispatch from foreign news agency
Road exports electric energy and/or absorbs electric energy.
In the present invention, the export importing of electronics is a kind of work normality, and the export importing of so-called electronics refers to through external circuit
The export of the electronics carried out imports.
In the present invention, the electrochemistry region A, which is selectively chosen, is set as three-diemsnional electrode.
In the present invention, the electrochemistry region B, which is selectively chosen, is set as three-diemsnional electrode.
In the present invention, such as refer to J feed channel for J and K as synonym, J feed channel and the setting of K regional connectivity
Interior substance can contact the structural relation of setting with the region K.
In the present invention, such as using J and K as synonym, the region K is arranged in the cavity, and J feed channel is connected to the cavity
The structural relation for referring to that the substance in J feed channel can contact setting with the region K is set.
In the present invention, such as there is non-electronic conducting electrical relation using Y and X as synonym, Y and X, the electronics of the Y is led
The form of presentation imported out refers to that the Y, the X and electronics export import the composition that circuit three is same closed circuit
Part is selectively chosen electronics export importing circuit being set as external circuit, and non-electronic conducting electrical relation is formed
Circuit be set as interior circuit.
In the present invention, such as using U, W and V as synonym, U has non-electronic conducting electrical relation through W and V, and electronics is in institute
The form of presentation for exporting importing between U and the V is stated, refers to that the U, the W, the V and electronics export import circuit
It is the component part of same closed circuit, is selectively chosen and electronics export importing circuit is set as external circuit, and will be non-
Electronic conduction electrical relation is formed by circuit and is set as interior circuit.
In the present invention, the area Jie electricity that so-called " area alternating current Jie electricity " refers to alternating current is selectively chosen and sets
For a part of relative subject, also alternative selection is set as the conduction region contacted with relative subject, is also selectively chosen
It is set as the conduction region that there is capacitance relation with relative subject.It includes that the area alternating current Jie electricity is this that so-called relative subject, which is exactly in A,
A in description.
In the present invention, so-called " alternating electromotive force " refers to that the changed electromotive force of electromotive force, such as direction become
The changed electromotive force of electromotive force or size of change.
In the present invention, so-called " alternating current " refers to the changed electric current of electric current, such as the changed electricity in direction
Stream, the changed electric current of size or alternating current.
In the present invention, so-called " alternating current " is selectively chosen the electric current for being set as the variation of electric current generating period,
Such as electric current or alternating current that electric current, the size generating period of direction generating period variation change.
In the present invention, so-called alternating current refers to the alternating current changed by sinusoidal rule.
In the present invention, so-called AC power source refers to the alternating source that electric current is changed by sinusoidal rule.
In the present invention, there is so-called A and B non-electronic conducting electrical relation to refer to having on interior circuit between A and B
Non-electronic conducting electrical relation, and its external circuit is selectively chosen electronic conduction relationship；Or, so-called A and B has non-electrical
Son conducting electrical relation, which refers to, has non-electronic conducting electrical relation on external circuit between A and B, and its interior circuit may be selected
Select electronic conduction relationship to property.
In the present invention, it is so-called " the electrochemistry region A through insulation, isolation space, electrolyte, dielectric, capacitor,
At least one of plasma, ionic liquid, ionized gas, solion and electronic conduction area and the electrochemistry region B
With non-electronic conducting electrical relation " it include the electrochemistry region A and the electrochemistry region B through electronic conduction area, insulation
The non-electronic conducting electrical relation that two solion ponds of body, dielectric and/or ion conducting body isolation have.In this device
In, be selectively chosen make at least one in the electrochemistry region A and the electrochemistry region B with capacitive region and/or
Non-electronic charged particle transmitter forms electrical relation.
In the present invention, so-called " electronic conduction area " refers to that conduct electrons are not turned on the region of non-electronic charged particle, can
Selectively selection is set as metallic conductor area, carbon conductor region etc..
In the present invention, so-called " non-electronic charged particle transmitter " refer to non-conducting electronics but proton conducting or it is specific from
The substance of son, i.e. electrolyte in conventional electrochemical device, can be according to the electrochemical properties of the reducing agent and the oxidant
Non-electronic charged particle transmitter is selected, such as when the reducing agent is H2, the oxidant is O2When, the non-electronic electrification
Particle conduction object alternative selects proton exchange membrane.
In the present invention, select electronic conduction area shape when, should for the purpose of increasing its capacitance with neighbors into
Row selection.
In the present invention, so-called " non-electronic conducting electrical relation " refers to the electricity formed through the charged particle other than electronics
Conducting relationship or the electricity to be formed conducting relationship of standing facing each other through electronics, for example, relationship, non-electronic electrification is connected in the electricity that capacitor is formed
The electricity conducting relationship etc. that particle reciprocating vibration is formed.
In the present invention, so-called electrochemistry region A, so-called electrochemistry region B are equal with electrode.
In the present invention, the region that electronics export imports is equal with electrode.
It in the present invention, is selectively chosen, there is dielectric capacitance relationship between electrode.
It in the present invention, is selectively chosen, the electrochemistry region A and the electrochemistry region B have dielectric capacitance
Relationship, dielectric can be gas, liquid, solid or vacuum.
In the present invention, so-called dielectric capacitance relationship refers to the capacitance relation through dielectric formation, and dielectric can be
Gas, liquid, solid or vacuum.
In the present invention, so-called " capacitor " be selectively chosen be set as electrolytic capacitor, super capacitor, electric double layer capacitance,
All capacitors such as pseudo capacitance, fake capacitance.
In the present invention, so-called " reversible electric machine " refers to the motor that can mutually convert between motor and generator,
For example, the motor that can be generated electricity when exportable rotary power, rotation when power supply.
In the present invention, it is selectively chosen and uses circumferential magnetic monopole direct current using DC reversible electromotor or selectivity selection
Reversible electric machine.
In the present invention, when the purpose using reversible electric machine is the power supply using reversible electric machine when exportable power reception power
The characteristics of can generating electricity, realizes the reinforcing and control imported to electronics export with electrode cooperating, and then realizes to electrochemistry mistake
The optimization of journey.
It in the present invention, is selectively chosen, so that reversible electric machine movement power generation is implemented electro ultrafiltration to electrode, when the electricity of electrode
When kinetic potential reaches setting degree, electrode, which powers to reversible electric machine, pushes reversible electric machine movement, sets when the electromotive force of electrode is reduced to
When determining degree, reversible electric machine implements electro ultrafiltration to electrode using the kinetic energy power generation of itself and its STATEMENT OF FEDERALLY SPONSORED, so again and again
Carry out cyclic process；In circulation, electrode recycles entirety and is to provide electric energy in the presence of the process for providing electric energy with absorbing electric energy；
It is selectively chosen, control device is set between reversible electric machine and electrode；Be selectively chosen, load with reversible electric machine,
Electrode is arranged in series, or load is arranged in parallel with reversible electric machine.
It in the present invention, is selectively chosen, so that reversible electric machine movement power generation is implemented electro ultrafiltration to electrode, when electrode is in electricity
When electromotive force reaches setting degree under the action of chemical reaction and/or reversible electric machine, electrode is in electrochemical reaction and/or accumulation electricity
It powers under the action of lotus to reversible electric machine and pushes reversible electric machine movement, it is reversible when the electromotive force of electrode is reduced to setting degree
Motor implements electro ultrafiltration to electrode using the kinetic energy power generation of itself and its STATEMENT OF FEDERALLY SPONSORED, so carries out cyclic process again and again；
In circulation, electrode recycles entirety and is to provide electric energy in the presence of the process for providing electric energy with absorbing electric energy；Optionally select
It selects, control device is set between reversible electric machine and electrode；It being selectively chosen, load is arranged in series with reversible electric machine, electrode,
Or load is arranged in parallel with reversible electric machine.
It in the present invention, is selectively chosen, makes electrode move reversible electric machine reversible electric machine power supply, when the electricity of electrode
When kinetic potential is reduced to setting degree, reversible electric machine implements electro ultrafiltration to electrode using the kinetic energy power generation of itself and its STATEMENT OF FEDERALLY SPONSORED, when
When the electromotive force of electrode reaches setting degree, electrode, which powers to reversible electric machine, pushes reversible electric machine movement, so again and again
Carry out cyclic process；In circulation, electrode recycles entirety and is to provide electric energy in the presence of the process for providing electric energy with absorbing electric energy；
It is selectively chosen, control device is set between reversible electric machine and electrode；Be selectively chosen, load with reversible electric machine,
Electrode is arranged in series, or load is arranged in parallel with reversible electric machine.
It in the present invention, is selectively chosen, makes electrode under the action of electrochemical reaction and/or stored charge to reversible
Motor power supply moves reversible electric machine, and when the electromotive force of electrode is reduced to setting degree, reversible electric machine utilizes itself and its connection
The kinetic energy power generation of moving part to electrode implement electro ultrafiltration, when electrode under the action of electrochemical reaction and/or reversible electric machine electromotive force
When reaching setting degree, electrode pushes reversible electricity to reversible electric machine power supply under the action of electrochemical reaction and/or stored charge
Machine movement, so carries out cyclic process again and again；In circulation, there is the process for providing electric energy and absorbing electric energy in electrode, but
Circulation is whole to be to provide electric energy；It is selectively chosen, control device is set between reversible electric machine and electrode；Optionally
Selection, load are arranged in series with reversible electric machine, electrode, or load is arranged in parallel with reversible electric machine.
In the present invention, so-called " electrolyte " refer to all be arranged between two electrode of electrochemical appliance only allow it is specific
The substance that charged particle passes through but electronics is not allowed to pass through can be solid, liquid or membranous body etc., such as the proton of PEMFC
Film and solid oxide electrolyte etc..
In the present invention, so-called " being inserted into inert substance between the reducing agent and the oxidant " refers to goes back described
Former agent is contacted with electrochemistry region and the oxidant contacted with this electrochemistry region between make inert substance and this electrochemical school district
Domain contact, the purpose is to keep the boundary between the electrochemical reaction of the reducing agent and the electrochemical reaction of the oxidant more clear
It is clear.
In the present invention, so-called " dead band duration is inserted between the reducing agent and the oxidant " refers to goes back described
Former agent is contacted with electrochemistry region and the oxidant contacted with this electrochemistry region between be arranged dead band duration, the purpose is to keep away
Exempt from the reducing agent and oxidant mixing, makes the electrochemical process of the reducing agent and the electrochemical process of the oxidant
Between boundary it is apparent, so-called dead band duration refers to the time interval of setting, and specific duration is according to the reducing agent and institute
State the property of oxidant, the temperature in electrochemistry region and catalyst whether there is or not and stopping of needing of the reducing agent and the oxidant
Time etc. is stayed to determine.
In the present invention, so-called " inert substance " refers to the object not reacted with the reducing agent and the oxidant
Matter.
In the present invention, so-called " electrochemistry region " refers to that the region of electrochemical reaction can occurs in all, for example including
Catalyst, ultra microstructure and/or region (such as electrode in fuel cell etc.) at a set temperature, then for example in setting temperature
Metallic region under degree.
It is so-called to refer to " including catalyst, ultra microstructure and/or electrochemistry region at a set temperature " in the present invention
The electrochemistry region or including catalyst or including ultra microstructure or under the set temperature or the electrification
School district domain includes two or three in these three conditions.
In the present invention, so-called " ultra microstructure " refers to the microcosmic knot that can cause electrochemical reaction under setting condition
Structure.
In the present invention, so-called " local explosion limit " refers under conditions of the electrochemistry region, the reducing agent
The concentration ratio that cannot be exploded with the oxidant.
In the present invention, include the catalyst device in, the catalyst be set as include noble metal catalyst, or
The catalyst be set as include rare earth element catalyst.
In the present invention, so-called interpolar spacer refers to make to have required for non-electronic conducting electrical relation between electrode
Substance (including vacuum), for example, electrolyte, dielectric etc..
In the present invention, the selection of interpolar spacer alternative is set as insulation, isolation space, electrolyte, dielectric, electricity
At least one of appearance, plasma, ionic liquid, ionized gas, solion and electronic conduction area.
In the present invention, so-called interpolar spacer, which is selectively chosen, is set as interior circuit, is also selectively chosen and sets
For external circuit.
In the present invention, so-called electro ultrafiltration is a kind of selectivity selection.
In the present invention, so-called " non-electronic charged particle " refers to the charged particle other than electronics, such as proton or ion.
In the present invention, so-called " motor with additional rotation inertia " refers to the requirement with basis to rotary inertia,
The motor of additional setting rotary inertia.
In the present invention, after a certain component names plus the letter such as so-called " A ", " B " is merely to distinguish two or several
The identical component of title or substance.
In the present invention, necessary portion should be set in necessary place according to electricity field, the well-known technique of electrochemical field
Part, unit or system etc..
Beneficial effects of the present invention are as follows: electrochemical appliance disclosed in this invention will termination traditional chemical energy electric energy conversion
Electrochemical appliance with the history for existing for necessary condition of electrolyte (such as proton exchange membrane and solid oxide electrolyte etc.),
This kind of device that terminates also can not securely and reliably be used to the history of oxidant reduction agent composition, for efficient, long-life, low cost
The industrialization of chemical energy electric energy conversion electrochemical appliance provide new approach, and engine will be redefined.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the embodiment of the present invention 1；
Fig. 2 is the structural schematic diagram of the embodiment of the present invention 2；
Fig. 3 is the structural schematic diagram of the embodiment of the present invention 3；
Fig. 4 is the structural schematic diagram of the embodiment of the present invention 4；
Fig. 5 is the structural schematic diagram of the embodiment of the present invention 5；
Fig. 6 is the structural schematic diagram of the embodiment of the present invention 6；
Fig. 7 is the structural schematic diagram of the embodiment of the present invention 7；
Fig. 8 is the structural schematic diagram of the embodiment of the present invention 8；
Fig. 9 is the structural schematic diagram of the embodiment of the present invention 9；
Figure 10 is the structural schematic diagram of the embodiment of the present invention 10；
Figure 11 is the structural schematic diagram of the embodiment of the present invention 11；
Figure 12 is the structural schematic diagram of the embodiment of the present invention 12；
Figure 13 is the structural schematic diagram of the embodiment of the present invention 13；
Figure 14 is the structural schematic diagram of the embodiment of the present invention 14；
Figure 15-1 is the schematic diagram of the embodiment of the present invention 15；
Figure 15-2 is the schematic diagram of the embodiment of the present invention 16；
Figure 15-3 is the schematic diagram of the embodiment of the present invention 17；
Figure 15-4 is the schematic diagram of the embodiment of the present invention 18；
Figure 15-5 is the schematic diagram of the embodiment of the present invention 19；
Figure 15-6 is the schematic diagram of the embodiment of the present invention 20；
Figure 15-7 is the schematic diagram of the embodiment of the present invention 21；
Figure 15-8 is the schematic diagram of the embodiment of the present invention 22；
Figure 15-9 is the schematic diagram of the embodiment of the present invention 23；
Figure 15-10 is the schematic diagram of the embodiment of the present invention 24；
Figure 16-1 is the schematic diagram of the embodiment of the present invention 25；
Figure 16-2 is the schematic diagram of the embodiment of the present invention 26；
Figure 17-1 is the basic logic chart for exchanging electric energy for chemical energy；
Figure 17-2 is reducing agent oxidant electrochemical reaction controlled process figure；
Figure 17-3 is the schematic diagram of the embodiment of the present invention 27；
Figure 17-4 is the schematic diagram of the embodiment of the present invention 28；
Figure 17-5 is the schematic diagram of the embodiment of the present invention 29；
Figure 17-6 is the schematic diagram of the embodiment of the present invention 30.
In figure:
1 electrochemistry region A, 2 electrochemistry region B, 3 reducing agent feed channels, 4 oxidant feed channels, 5 cavitys, 51 chambers
Body A, 52 cavity B, 6 reducing agent control switches, 61 reducing agent control switch A, 62 reducing agent control switch B, the control of 7 oxidants are opened
Pass, 71 oxidant control switch A, 72 oxidant control switch B, 711 control switch A, 722 control switch B, 8 mixture feeds
Channel, 9 mixture control switches, 91 mixture control switch A, 92 mixture control switch B, 200 reversible electric machines.
Specific embodiment
Technical solution of the present invention is further illustrated in the following with reference to the drawings and specific embodiments.
Embodiment 1
Electrochemical appliance as shown in Figure 1, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
Setting is connected to reducing agent feed channel 3, the electrochemistry region A1 is connected to setting, the electrification with oxidant feed channel 4
School district domain B2 is connected to setting with reducing agent feed channel 3, and the electrochemistry region B2 is connected to setting with oxidant feed channel 4,
The electrochemistry region A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes alternating current Jie electricity area B, described
It is work normality that the export of electronics between electrochemistry region A1 and the electrochemistry region B2, which imports,.
As can embodiment in conversion, optionally make reducing agent feed channel 3 to the electrochemical school district
The process of the process of domain A1 feed reducing agent and oxidant feed channel 4 to the electrochemistry region A1 feed oxidant
Alternately, reducing agent feed channel 3 supplies the process of the electrochemistry region B2 feed reducing agent and the oxidant
Send channel 4 to the process of the electrochemistry region B2 feed oxidant alternately, in some time interval, to the electricity
One of chemical regions A1 feed Oxidizing and Reducing Agents, in the electrochemistry region B2 feed Oxidizing and Reducing Agents
It is another.
As can embodiment in conversion, optionally make reducing agent feed channel 3 to the electrochemical school district
The process of the process of domain A1 feed reducing agent and oxidant feed channel 4 to the electrochemistry region A1 feed oxidant
There are overlapping, reducing agent feed channel 3 supplies the process of the electrochemistry region B2 feed reducing agent and the oxidant
Channel 4 is sent to there is overlapping to the process of the electrochemistry region B2 feed oxidant.
As can embodiment in conversion, optionally make reducing agent feed channel 3 to the electrochemical school district
The process of the interrupted feed reducing agent of domain A1 and oxidant feed channel 4 aoxidize the interrupted feed of the electrochemistry region A1
There is overlapping in the process of agent, reducing agent feed channel 3 to the process of the interrupted feed reducing agent of the electrochemistry region B2 and
There is overlapping to the process of the interrupted feed oxidant of the electrochemistry region B2 in oxidant feed channel 4.
Embodiment 2
Electrochemical appliance as shown in Figure 2, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is arranged in cavity A51, the cavity A51 is connected to setting, the cavity A51 and oxidant feed with reducing agent feed channel 3
The connection setting of channel 4, the electrochemistry region B2 are arranged in cavity B52, and the cavity B52 and reducing agent feed channel 3 connect
Logical setting, the cavity B52 are connected to setting with oxidant feed channel 4, and the electrochemistry region A1 includes that alternating current connects electricity
Area A, the electrochemistry region B2 include alternating current Jie electricity area B, the electrochemistry region A1 and the electrochemistry region B2 it
Between electronics export import be work normality.
As can embodiment in conversion, supply that reducing agent feed channel 3 to the cavity A51
Send reducing agent process and oxidant feed channel 4 to the process of the cavity A51 feed oxidant alternately, it is described
Reducing agent feed channel 3 is to the process of the cavity B52 feed reducing agent and oxidant feed channel 4 to the cavity
The process of B52 feed oxidant alternately, in some time interval, to the cavity A51 feed Oxidizing and Reducing Agents
One of, to the another kind in the cavity B52 feed Oxidizing and Reducing Agents.
As can embodiment in conversion, supply that reducing agent feed channel 3 to the cavity A51
There is overlapping to the process of the cavity A51 feed oxidant in the process and oxidant feed channel 4 for sending reducing agent, described
Reducing agent feed channel 3 is to the process of the cavity B52 feed reducing agent and oxidant feed channel 4 to the cavity
There is overlapping in the process of B52 feed oxidant.
As can embodiment in conversion, optionally make reducing agent feed channel 3 disconnected to the cavity A51
There is the process of the interrupted feed oxidant of the cavity A51 in the process of continuous feed reducing agent and oxidant feed channel 4
Overlapping, process and oxidant feed channel of the reducing agent feed channel 3 to the interrupted feed reducing agent of the cavity B52
There is overlapping in the process of 4 pairs of interrupted feed oxidants of cavity B52.
Embodiment 3
Electrochemical appliance as shown in Figure 3, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is arranged in cavity 5 with the electrochemistry region B2, the cavity 5 is connected to setting, the cavity 5 with reducing agent feed channel 3
Setting is connected to oxidant feed channel 4, the electrochemistry region A1 includes alternating current Jie electricity area A, the electrochemistry region
B2 includes alternating current Jie electricity area B, and the export of the electronics between the electrochemistry region A1 and the electrochemistry region B2 imports
For the normality that works.
As can embodiment in conversion, optionally make the mistake of 3 feed reducing agent of reducing agent feed channel
The process of 4 feed oxidant of journey and oxidant feed channel is alternately.
As can embodiment in conversion, optionally make the mistake of 3 feed reducing agent of reducing agent feed channel
There is overlapping in the process of 4 feed oxidant of journey and oxidant feed channel.
As can embodiment in conversion, optionally make the interrupted feed reducing agent in reducing agent feed channel 3
The interrupted feed oxidant of feed process and oxidant feed channel 4 feed process exist overlapping.
Embodiment 4
Electrochemical appliance as shown in Figure 4, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is connected to setting with reducing agent feed channel 3 through reducing agent control switch A61, the electrochemistry region A1 is through oxidant control switch
A71 is connected to setting with oxidant feed channel 4, and the electrochemistry region B2 is through reducing agent control switch B62 and reducing agent feed
The connection setting of channel 3, the electrochemistry region B2 are connected to setting, institute with oxidant feed channel 4 through oxidant control switch B72
Stating electrochemistry region A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes alternating current Jie electricity area B, the electricity
It is work normality that the export of electronics between chemical regions A1 and the electrochemistry region B2, which imports,.
As can embodiment in conversion, optionally make the reducing agent control switch A61 by control device control
System and the oxidant control switch A71 are controlled the mistake of realization 3 feed reducing agent of reducing agent feed channel by control device
Alternately, the reducing agent control switch B62 is filled the process of 4 feed oxidant of journey and oxidant feed channel by control
It sets control and the oxidant control switch B72 is controlled by control device and realized 3 feed reducing agent of reducing agent feed channel
4 feed oxidant of process and oxidant feed channel process alternately, in some time interval, to the electricity
One of chemical regions A1 feed Oxidizing and Reducing Agents, in the electrochemistry region B2 feed Oxidizing and Reducing Agents
It is another.
As can embodiment in conversion, optionally make the reducing agent control switch A61 by control device control
System and the oxidant control switch A71 are controlled the mistake of realization 3 feed reducing agent of reducing agent feed channel by control device
There is overlapping in the process of 4 feed oxidant of journey and oxidant feed channel, the reducing agent control switch B62 is filled by control
It sets control and the oxidant control switch B72 is controlled by control device and realized 3 feed reducing agent of reducing agent feed channel
4 feed oxidant of process and oxidant feed channel process exist overlapping.
As can embodiment in conversion, optionally make the reducing agent control switch A61 by control device control
System and the oxidant control switch A71 are controlled by control device realizes the interrupted feed reducing agent in reducing agent feed channel 3
The interrupted feed oxidant of feed process and oxidant feed channel 4 feed process exist overlapping, the reducing agent control
System switch B62 is controlled by control device and the oxidant control switch B72 is controlled by control device and realized that the reducing agent supplies
Send the feed process of the interrupted feed oxidant of feed process and oxidant feed channel 4 of the interrupted feed reducing agent in channel 3
There are overlappings.
As can embodiment in conversion, optionally make the reducing agent control switch A61 and the oxidant
Control switch A71 is controlled by control device realizes that the reducing agent control switch A61 is opened and made the oxidant control switch
A71 discontinuously opens and makes the reducing agent control switch B62 and the oxidant control switch B72 to be controlled by control device
Realize that the reducing agent control switch B62 is opened and opened the oxidant control switch B72 discontinuously, or optionally,
It controls the reducing agent control switch A61 and the oxidant control switch A71 by control device and realizes the oxidant control
System switch A71 is opened and is opened the reducing agent control switch A61 discontinuously and make the reducing agent control switch B62 and institute
Oxidant control switch B72 is stated to be controlled the realization oxidant control switch B72 unlatching by control device and make the reducing agent
Control switch B62 is discontinuously opened, or selectively, makes the reducing agent control switch A61 and the oxidant control switch
A71 is controlled by control device realizes that the reducing agent control switch A61 is opened and opened the oxidant control switch A71 discontinuously
It opens and makes the reducing agent control switch B62 and the oxidant control switch B72 to be controlled by control device and realize the oxygen
Agent control switch B72 is opened and is opened the reducing agent control switch B62 discontinuously.
As can embodiment in conversion, optionally select not set the reducing agent control switch A61 and described
Reducing agent control switch B62, and control the oxidant control switch A71 by control device and realize that the oxidant control is opened
A71 is closed discontinuously to open and the oxidant control switch B72 is made to be controlled the realization oxidant control switch by control device
B72 is discontinuously opened.
As can embodiment in conversion, optionally select not set the oxidant control switch A71 and described
Oxidant control switch B72, and control the reducing agent control switch A61 by control device and realize that the reducing agent control is opened
A61 is closed discontinuously to open and the reducing agent control switch B62 is made to be controlled the realization reducing agent control switch by control device
B62 is discontinuously opened.
As can embodiment in conversion, optionally select not set the reducing agent control switch A61 and described
Oxidant control switch B72, and control the oxidant control switch A71 by control device and realize that the oxidant control is opened
A71 is closed discontinuously to open and the reducing agent control switch B62 is made to be controlled the realization reducing agent control switch by control device
B62 is discontinuously opened.
Embodiment 5
Electrochemical appliance as shown in Figure 5, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is arranged in cavity A51, the cavity A51 is connected to setting with reducing agent feed channel 3 through reducing agent control switch A61, described
Cavity A51 is connected to setting with oxidant feed channel 4 through oxidant control switch A71, and the electrochemistry region B2 is arranged in chamber
In body B52, the cavity B52 is connected to setting, the cavity B52 warp with reducing agent feed channel 3 through reducing agent control switch B62
Oxidant control switch B72 is connected to setting with oxidant feed channel 4, and the electrochemistry region A1 includes the area alternating current Jie electricity
A, the electrochemistry region B2 include alternating current Jie electricity area B, between the electrochemistry region A1 and the electrochemistry region B2
Electronics export import be work normality.
As can embodiment in conversion, optionally selection fills the reducing agent control switch A61 by control
It sets control and the oxidant control switch A71 is controlled by control device and realized 3 feed reducing agent of reducing agent feed channel
4 feed oxidant of process and oxidant feed channel process alternately, the reducing agent control switch B62 is controlled
Device control processed and the oxidant control switch B72 are controlled by control device realizes reducing agent feed channel 3 for returning
The process of 4 feed oxidant of the process of former agent and oxidant feed channel alternately, in some time interval, to institute
One of electrochemistry region A1 feed Oxidizing and Reducing Agents is stated, to the electrochemistry region B2 feed Oxidizing and Reducing Agents
In another kind.
As can embodiment in conversion, optionally selection fills the reducing agent control switch A61 by control
It sets control and the oxidant control switch A71 is controlled by control device and realized 3 feed reducing agent of reducing agent feed channel
The process of 4 feed oxidant of process and oxidant feed channel there is overlapping, the reducing agent control switch B62 is controlled
Device control processed and the oxidant control switch B72 are controlled by control device realizes reducing agent feed channel 3 for returning
There is overlapping in the process of 4 feed oxidant of the process of former agent and oxidant feed channel.
As can embodiment in conversion, optionally selection fills the reducing agent control switch A61 by control
It sets control and the oxidant control switch A71 is controlled by control device and realized reducing agent feed channel 3 discontinuously for returning
There is overlapping, the reduction in the feed process of the interrupted feed oxidant of feed process and oxidant feed channel 4 of former agent
Agent control switch B62 is controlled by control device and the oxidant control switch B72 is controlled by control device and realized the reduction
The feed of the interrupted feed oxidant of feed process and oxidant feed channel 4 of the interrupted feed reducing agent in agent feed channel 3
There is overlapping in process.
As can embodiment in conversion, optionally selection makes the reducing agent control switch A61 and the oxygen
Agent control switch A71 is controlled by control device realizes that the reducing agent control switch A61 is opened and controlled the oxidant
Switch A71 discontinuously opens and makes the reducing agent control switch B62 and the oxidant control switch B72 by control device
Control realizes that the reducing agent control switch B62 is opened and opened the oxidant control switch B72 discontinuously, or selectively
Selection controls the reducing agent control switch A61 and the oxidant control switch A71 by control device and realizes the oxidation
Agent control switch A71 is opened and is opened the reducing agent control switch A61 discontinuously and make the reducing agent control switch B62
It is controlled with the oxidant control switch B72 by control device and realizes that the oxidant control switch B72 is opened and made described go back
Former agent control switch B62 is discontinuously opened, or is selectively selected, and the reducing agent control switch A61 and the oxidant control are made
System switch A71 is controlled by control device realizes that the reducing agent control switch A61 is opened and made the oxidant control switch A71
Discontinuously open and make the reducing agent control switch B62 and the oxidant control switch B72 to be controlled realization by control device
The oxidant control switch B72 is opened and is opened the reducing agent control switch B62 discontinuously.
As can embodiment in conversion, optionally select not set the reducing agent control switch A61 and described
Reducing agent control switch B62, the oxidant control switch A71 are controlled interrupted unlatching, the oxidant control by control device
Switch B72 is controlled interrupted unlatching by control device.
As can embodiment in conversion, optionally select not set the oxidant control switch A71 and described
Oxidant control switch B72, the reducing agent control switch A61 are controlled interrupted unlatching, the reducing agent control by control device
Switch B62 is controlled interrupted unlatching by control device.
As can embodiment in conversion, optionally select not set the reducing agent control switch A61 and described
Oxidant control switch B72, the oxidant control switch A71 are controlled interrupted unlatching, the reducing agent control by control device
Switch B62 is controlled interrupted unlatching by control device.
Embodiment 6
Electrochemical appliance as shown in FIG. 6, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is arranged in cavity 5 with the electrochemistry region B2, the cavity 5 is through reducing agent control switch 6 and reducing agent feed channel 3
Connection setting, the cavity 5 are connected to setting, the electrochemistry region A1 with oxidant feed channel 4 through oxidant control switch 7
Including alternating current Jie electricity area A, the electrochemistry region B2 includes alternating current Jie electricity area B, the electrochemistry region A1 and institute
It is work normality that the export for stating the electronics between the B2 of electrochemistry region, which imports,.
As can embodiment in conversion, optionally selection makes the reducing agent control switch 6 by control device
Control and the oxidant control switch 7 are controlled the mistake of realization 3 feed reducing agent of reducing agent feed channel by control device
The process of 4 feed oxidant of journey and oxidant feed channel is alternately.
As can embodiment in conversion, optionally selection makes the reducing agent control switch 6 by control device
Control and the oxidant control switch 7 are controlled the mistake of realization 3 feed reducing agent of reducing agent feed channel by control device
There is overlapping in the process of 4 feed oxidant of journey and oxidant feed channel.
As can embodiment in conversion, optionally select the reducing agent control switch 6 by control device control
System and the oxidant control switch 7 are controlled by control device realizes the interrupted feed reducing agent in reducing agent feed channel 3
There is overlapping in the feed process of the interrupted feed oxidant of feed process and oxidant feed channel 4.
As can embodiment in conversion, optionally selection makes the reducing agent control switch 6 by control device
Control is realized to open and the oxidant control switch 7 is made to be controlled realization by control device and discontinuously be opened, or makes the reducing agent
Control switch 6 is controlled realization by control device and discontinuously opens and the oxidant control switch 7 is made to be controlled realization by control device
It opens.
Embodiment 7
Electrochemical appliance as shown in Figure 7, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
Setting is connected to reducing agent feed channel A31, the electrochemistry region A1 is connected to setting with oxidant feed channel A41, described
Electrochemistry region B2 is connected to setting, the electrochemistry region B2 and oxidant feed channel B42 with reducing agent feed channel B32
Control switch A711 is being arranged, in oxidant feed channel B42 in connection setting on oxidant feed channel A41
Upper setting control switch B722, the electrochemistry region A1 include alternating current Jie electricity area A, and the electrochemistry region B2 includes
Alternating current Jie electricity area B, it is work that the export of the electronics between the electrochemistry region A1 and the electrochemistry region B2, which imports,
Normality.
As an alternative embodiment, it is selectively chosen to be changed to be arranged by the control switch A711 and restore
Agent feed channel A31, the control switch B722 are also readily modified as setting on reducing agent feed channel B32.
As an alternative embodiment, being selectively chosen makes the control switch A711 and the control switch
B722 is controlled by control device and is alternately opened.
As an alternative embodiment, being selectively chosen makes the control switch A711 and the control switch
B722 is controlled by control device and is opened in the presence of overlapping.
As an alternative embodiment, being selectively chosen controls the control switch A711 by control device
It realizes and reducing agent described in feed is continued to the electrochemistry region A1 and is aoxidized to described in the interrupted feed of electrochemistry region A1
Agent and make the control switch B722 by control device controlled realization reduction described in feed is continued to the electrochemistry region B2
Agent and to oxidant described in the interrupted feed of electrochemistry region B2, or selectively selection keeps the control switch A711 controlled
Device control processed, which is realized, to be continued oxidant described in feed to the electrochemistry region A1 and discontinuously supplies the electrochemistry region A1
It send the reducing agent and the control switch B722 is made to be controlled realization by control device and the electrochemistry region B2 is persistently supplied
It send the oxidant and selection opens the control to reducing agent described in the interrupted feed of electrochemistry region B2, or selectively
Pass A711 is controlled realization by control device and continues reducing agent described in feed to the electrochemistry region A1 and to the electrochemical school district
Oxidant described in the interrupted feed of domain A1 and the control switch B722 is made to be controlled realization to the electrochemical school district by control device
Domain B2 continues oxidant described in feed and to reducing agent described in the interrupted feed of electrochemistry region B2.
Embodiment 8
Electrochemical appliance as shown in Figure 8, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is arranged in cavity A51, the cavity A51 is connected to setting with reducing agent feed channel A31, and the cavity A51 and oxidant supply
Channel A41 connection setting is sent, the electrochemistry region B2 is arranged in cavity B52, the cavity B52 and reducing agent feed channel
B32 connection setting, the cavity B52 is connected to setting with oxidant feed channel B42, on oxidant feed channel A41
Control switch A711 is set, control switch B722, the electrochemistry region A1 packet are set on oxidant feed channel B42
Include alternating current Jie electricity area A, the electrochemistry region B2 includes alternating current Jie electricity area B, the electrochemistry region A1 and described
It is work normality that the export of electronics between the B2 of electrochemistry region, which imports,.
As an alternative embodiment, it is selectively chosen to be changed to be arranged by the control switch A711 and restore
Agent feed channel A31, the control switch B722 are also readily modified as setting on reducing agent feed channel B32.
As an alternative embodiment, being selectively chosen makes the control switch A711 and the control switch
B722 is controlled by control device and is alternately opened.
As an alternative embodiment, being selectively chosen makes the control switch A711 and the control switch
B722 is controlled by control device and is opened in the presence of overlapping.
As an alternative embodiment, being selectively chosen controls the control switch A711 by control device
Realization continues reducing agent described in feed to the cavity A51 and to oxidant described in the interrupted feed of cavity A51 and makes institute
State control switch B722 by control device controlled realization reducing agent described in feed is continued to the cavity B52 and to the cavity
Oxidant described in the interrupted feed of B52, or selectively to select, the control switch A711 is made to be controlled realization pair by control device
The cavity A51 continues oxidant described in feed and to reducing agent described in the interrupted feed of cavity A51 and makes the control
Switch B722 by control device controlled realization to the cavity B52 continue oxidant described in feed and to the cavity B52 it is interrupted
Reducing agent described in feed, or selectively to select, the control switch A711 is made to be controlled realization to the chamber by control device
Body A51 continues reducing agent described in feed and to oxidant agent described in the interrupted feed of cavity A51 and makes the control switch
B722 is controlled realization by control device and continues oxidant described in feed to the cavity B52 and to the interrupted feed of cavity B52
The reducing agent.
Embodiment 9
Electrochemical appliance as shown in Figure 9, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region A1
It is connected to setting with the mixture feed channel 8 of reducing agent and oxidant, the electrochemistry region B2 and reducing agent and oxidant
The connection setting of mixture feed channel 8, the electrochemistry region A1 includes alternating current Jie electricity area A, the electrochemistry region B2
Including alternating current Jie electricity area B, the export importing of the electronics between the electrochemistry region A1 and the electrochemistry region B2 is
Work normality.
As an alternative embodiment, being selectively chosen keeps 8 continuous feeding of mixture feed channel mixed
Close object.
As an alternative embodiment, being selectively chosen keeps the interrupted feed in mixture feed channel 8 mixed
Close object.
Embodiment 10
Electrochemical appliance as shown in Figure 10, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region
A1 is arranged in cavity A51, and the cavity A51 is connected to setting with the mixture feed channel 8 of reducing agent and oxidant, described
Electrochemistry region B2 is arranged in cavity B52, and the cavity B52 is connected to the mixture feed channel 8 of reducing agent and oxidant
Setting, the electrochemistry region A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes alternating current Jie electricity area B,
It is work normality that the export of electronics between the electrochemistry region A1 and the electrochemistry region B2, which imports,.
As an alternative embodiment, being selectively chosen keeps 8 continuous feeding of mixture feed channel mixed
Close object.
As an alternative embodiment, being selectively chosen keeps the interrupted feed in mixture feed channel 8 mixed
Close object.
Embodiment 11
Electrochemical appliance as shown in figure 11, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region
The A1 and electrochemistry region B2 is arranged in cavity 5, the mixture feed channel 8 of the cavity 5 and reducing agent and oxidant
Connection setting, the electrochemistry region A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes that alternating current connects electricity
Area B, it is work normality that the export of the electronics between the electrochemistry region A1 and the electrochemistry region B2, which imports,.
As an alternative embodiment, being selectively chosen keeps 8 continuous feeding of mixture feed channel mixed
Close object.
As an alternative embodiment, being selectively chosen keeps the interrupted feed in mixture feed channel 8 mixed
Close object.
Embodiment 12
Electrochemical appliance as shown in figure 12, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region
A1 is connected to setting, the electrification school district with the mixture feed channel 8 of reducing agent and oxidant through mixture control switch A91
Domain B2 is connected to setting, the electrification school district with the mixture feed channel 8 of reducing agent and oxidant through mixture control switch B92
Domain A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes alternating current Jie electricity area B, the electrochemistry region A1
It is work normality that the export of electronics between the electrochemistry region B2, which imports,.
As an alternative embodiment, being selectively chosen fills the mixture control switch A91 by control
It sets control and realizes 8 continuous feeding mixture of mixture feed channel, the mixture control switch B92 is by control device control
System realizes 8 continuous feeding mixture of mixture feed channel.
As an alternative embodiment, being selectively chosen fills the mixture control switch A91 by control
It sets control and realizes the interrupted feed mixture in mixture feed channel 8, the mixture control switch B92 is by control device control
System realizes the interrupted feed mixture in mixture feed channel 8.
Embodiment 13
Electrochemical appliance as shown in fig. 13 that, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region
A1 is arranged in cavity A51, and mixture feed of the cavity A51 through mixture control switch 9 and reducing agent and oxidant is logical
The connection setting of road 8, the electrochemistry region B2 are arranged in cavity B52, and the cavity B52 is through mixture control switch 9 and also
Former agent is connected to setting with the mixture feed channel 8 of oxidant, and the electrochemistry region A1 includes alternating current Jie electricity area A, institute
Stating electrochemistry region B2 includes alternating current Jie electricity area B, the electricity between the electrochemistry region A1 and the electrochemistry region B2
It is work normality that the export of son, which imports,.
As an alternative embodiment, being selectively chosen makes the mixture control switch 9 by control device
8 continuous feeding mixture of mixture feed channel is realized in control.
As an alternative embodiment, being selectively chosen makes the mixture control switch 9 by control device
The interrupted feed mixture in mixture feed channel 8 is realized in control.
As an alternative embodiment, setting the present embodiment and its above-mentioned disposable implementation are selectively chosen
The mixture control switch 9 being connected to the cavity A51 in mode and the mixture being connected to the cavity B52
Control switch 9 is the same mixture control switch.
As an alternative embodiment, be selectively chosen make setting be connected to the cavity A51 it is described mix
Conjunction object control switch 9 is mixture control switch A91, and the mixture control switch 9 being connected to the cavity B52 is mixing
Object control switch B92, and control the mixture control switch A91 by control device and realize mixture feed channel 8
Continuous feeding mixture, the mixture control switch B92 is controlled by control device realizes that mixture feed channel 8 is continuous
Feed mixture.
As an alternative embodiment, be selectively chosen make setting be connected to the cavity A51 it is described mix
Conjunction object control switch 9 is mixture control switch A91, and the mixture control switch 9 being connected to the cavity B52 is mixing
Object control switch B92, and control the mixture control switch A91 by control device and realize mixture feed channel 8
Interrupted feed mixture, the mixture control switch B92 is controlled by control device realizes that mixture feed channel 8 is interrupted
Feed mixture.
Embodiment 14
Electrochemical appliance as shown in figure 14, including electrochemistry region A1 and electrochemistry region B2, the electrochemistry region
The A1 and electrochemistry region B2 is arranged in cavity 5, and the cavity 5 is through mixture control switch 9 and reducing agent and oxidant
Mixture feed channel 8 be connected to setting, the electrochemistry region A1 includes alternating current Jie electricity area A, the electrochemistry region
B2 includes alternating current Jie electricity area B, and the export of the electronics between the electrochemistry region A1 and the electrochemistry region B2 imports
For the normality that works.
As an alternative embodiment, being selectively chosen makes the mixture control switch 9 by control device
8 continuous feeding mixture of mixture feed channel is realized in control.
As an alternative embodiment, being selectively chosen makes the mixture control switch 9 by control device
The interrupted feed mixture in mixture feed channel 8 is realized in control.
As an alternative embodiment, the above-mentioned all embodiments of the present invention and its convertible ground embodiment are optional
It selects to selecting property to be inserted into inert substance and/or dead band duration between the reducing agent and the oxidant.
As an alternative embodiment, the above-mentioned all embodiments of the present invention and its convertible ground embodiment are optional
It selects to selecting property to be arranged by the electrochemistry region A1 and the setting of power supply electric communication or by the electrochemistry region A1 in electric field
In, and/or, the electrochemistry region B2 and power supply electric communication are arranged or the electrochemistry region B2 is arranged in electric field
In；Or, capacitor, DC power supply, AC power source, alternation are arranged between the electrochemistry region A1 and the electrochemistry region B2
Power supply, inductor conductor, inductance coil, charged particle pump, phase converter, reversing switch circuit, rectifier, electric field, oscillation electricity
Road, motor, reversible electric machine, the motor with additional rotation inertia or its two conjunction, its three conjunction, its four conjunction, its
Five conjunctions, its six conjunction, its seven conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11 conjunction,
The conjunction of its ten binomial, its 13 conjunction, its 14 conjunction, its 15 conjunction.
As an alternative embodiment, the above-mentioned all embodiments of the present invention and its convertible ground embodiment are optional
Select to selecting property to make that there is non-electronic conducting electrical relation between the electrochemistry region A1 and the electrochemistry region B2, or,
Make the electrochemistry region A1 through insulation, isolation space, electrolyte, dielectric, capacitor, plasma, ionic liquid, ion
At least one of gas, solion and electronic conduction area are closed with the electrochemistry region B2 with non-electronic conducting electricity
System.
As an alternative embodiment, the above-mentioned all embodiments of the present invention and its convertible ground embodiment are optional
It selects to selecting property to make the electrochemistry region A1 rotation setting, the electrochemistry region B2 rotation setting.
As an alternative embodiment, the spy in the various embodiments described above of the present invention and its disposable way of example
Sign can be combined with each other on the basis of reconcilable.
Embodiment 15
Figure 15-1 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), substance A and the work that substance B is alternately contacted with electrode A and substance B and substance A are alternately contacted with electrode B
Procedure chart, electrochemical appliance of the invention optionally work according to following courses of work.
In Figure 15-1,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer, and A representative species A (reducing agent), B are represented
Substance B (oxidant).When substance A is contacted with electrode A and substance B and electrode B contact (1. shown process in figure), substance A exists
Electrode A forming material A cation A+(i.e. reducing agent cation A+) and electronics, substance B is in electrode B serious hope electronics (because electronegativity is inhaled
Draw affine electronics), the electronics of electrode A is loaded 5a and exports to electrode B (substance B can receive and electronically form object in some cases
Matter B anion B—Or oxidant anion B—, do not show in figure), as the A of electrode A+(or the electronics or electrode B of electrode B
B—) when running up to setting degree, substance A and substance B switch (in such as figure 4. shown in) and electronics through load 5a from electrode B
It is imported into electrode A, the reaction of generation substance A and substance B redox reaction product C occurs in electrode A and electrode B at this time
(5. shown in such as figure).Because substance B has strong electronegativity, therefore electric when exporting from the coexistence state of substance B, substance A and electronics
The period of the day from 11 p.m. to 1 a.m will form substance B, substance A cation A+With electronics coexistence state, and then three react generate C.Next it can divide two-way
Continue, is as 5. passed through in figure all the wayShown in 1., and in process1. locate to switch substance A and substance B again, into
And realize cycle operation in cycles；Another way is as 5. passed through in figureShown in 7., that is, carry out that substance B is maintained to connect with electrode A
Touching, substance A contacts with electrode B, when the electronics (electronics and substance B coexists in electrode A or electronics is in electrode A and substance B of electrode A
Forming material B anion or oxidant anion B—, do not show in figure) or when electrode B A+When running up to setting degree (such as
In figure 8. shown in), switching substance A and substance B and electronics is made to export to electrode B (in such as figure 9. shown in) from electrode A through load 5a,
At this moment the reaction (in such as figure 10. shown in) for occurring to generate C in electrode A and electrode B, continue to substance A contacted with electrode A and
The state that substance B is contacted with electrode B reach in figure 1. shown in process, and then realize cycle operation in cycles.
Embodiment 16
Figure 15-2 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), H2And O2It is alternately contacted and O with electrode A2And H2The process chart alternately contacted with electrode B, this hair
Bright electrochemical appliance optionally works according to following courses of work.
In Figure 15-2,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.The principle and process and figure that this figure illustrates
Identical shown in 15-1, only the reducing agent substance A in Figure 15-1 is with H2To represent, oxidant species B is with O2To represent, reduction
Agent cation A+It is then H+。
Embodiment 17
Figure 15-3 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), CH3OH and O2Contact and O are alternateed with electrode A2And CH3OH and electrode B alternate the work of contact
Make procedure chart, electrochemical appliance of the invention optionally works according to following courses of work.
In Figure 15-3,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.The principle and process and figure that this figure illustrates
Identical shown in 15-1, only the reducing agent substance A in Figure 15-1 is with CH3OH is representative, and oxidant species B is with O2To represent.This
The principle shown in Figure 15-1 is compared with process outside, the principle shown in Figure 15-3 and in the process H2O is participated in as recycled material
Electrochemical reaction process.
Embodiment 18
Figure 15-4 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), the mixture of substance A and substance B is contacted with electrode A and the mixture and electrode B of substance B and substance A
The process chart that contact and electro ultrafiltration participate in, electrochemical appliance of the invention is optionally according to following course of work works
Make.
In Figure 15-4,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer, and A representative species A (reducing agent), B are represented
Substance B (oxidant).When the mixture of substance A and substance B contacts and the mixture and electrode B of substance A and substance B with electrode A
When contact (1. shown process in figure), the substance A in mixture is in electrode A forming material A cation A+(i.e. reducing agent just from
Sub- A+) and electronics, the substance A in mixture is in electrode B also forming material A cation A+(i.e. reducing agent cation A+) and electronics,
Substance B in mixture is thirsted for electronics (because electronegativity attracts affine electronics) in electrode A, and the substance B in mixture is in electrode B
Thirst for electronics (because electronegativity attracts affine electronics), therefore, electrode A and electrode B are in symmetry status, without electric current flowing.So
And when applying electro ultrafiltration, the electronics of electrode A is exported to electrode B, and (substance B can receive and electronically form object in some cases
Matter B anion B—Or oxidant anion B—, do not show in figure) and (in such as figure 1. and 2. shown in), as the A of electrode A+(or
The electronics of electrode B or the B of electrode B—) when running up to setting degree (in such as figure 3. shown in), lead electronics from electrode B through load 5a
Enter to electrode A (in such as figure 4. shown in), generation substance A and substance B redox reaction occurs in electrode A and electrode B at this time
The reaction (4. shown in such as figure) of product C.Because substance B has strong electronegativity, therefore when being total to from substance B, substance A and electronics
Depositing will form substance B, substance A cation A when exporting electronics in state+With electronics coexistence state, and then three react generate C.It connects down
Two-way can be divided to continue, be all the way as in figure 5. to shown in 1., and then realization cycle operation in cycles；Another way is
5. apply the electro ultrafiltration of opposite direction to shown in 6. in such as figure, when electrode A electronics (electronics and substance B coexist in electrode A, or
Electronics is in electrode A and substance B forming material B anion or oxidant anion B—, do not show in figure, in B—In the presence of, when
B—When running up to setting degree) when running up to setting degree or when electrode B A+(such as 8. institute in figure when running up to setting degree
Show), so that electronics is exported to electrode B (in such as figure 9. shown in) from electrode A through load 5a, is at this moment given birth in electrode A and electrode B
At the reaction (in such as figure 9. shown in) of C, apply opposite direction electro ultrafiltration reach in figure 1. shown in process, and then realize week
And renew cycle operation.The purpose of electro ultrafiltration is control and strengthen electrochemical reaction, and electro ultrafiltration can come from external power supply, can be with
Chemical potential in electrochemical reaction can be from the electric energy by storing process (for example, through capacitor or oscillating circuit
Electric energy) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, and is stored in electricity
At pole, released together when electric current is reversed.
Embodiment 19
Figure 15-5 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), the mixture of substance A and substance B and electrode A makes discontinuous contact and substance B and the mixture of substance A with
The process chart that electrode B makes discontinuous contact and electro ultrafiltration participate in, electrochemical appliance of the invention is optionally according to following
Course of work work.
In Figure 15-5,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer, and A representative species A (reducing agent), B are represented
Substance B (oxidant).Other than the influence of electrode and mixture makes discontinuous contact, principle shown in Figure 15-5 and process and Figure 15-4
Shown in it is identical, the purpose for making electrode and mixture makes discontinuous contact is to reduce duration existing for mixture, increases the safety of process
Property, reliability and controllability.The purpose of electro ultrafiltration is control and reinforcing electrochemical reaction, and electro ultrafiltration can come from external power supply,
It can come from the chemical potential in electrochemical reaction, can be from the electric energy by storing process (for example, through capacitor or oscillation electricity
The electric energy on road) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, but is stored
At electrode, released together when electric current is reversed.
Embodiment 20
Figure 15-6 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), H2And O2Mixture contacted with electrode A and H2And O2Mixture contacted with electrode B and also electricity make
With the process chart of participation, electrochemical appliance of the invention optionally works according to following courses of work.
In Figure 15-6,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.In addition to reducing agent is with H2To represent, oxidation
Agent is with O2Outer to represent, principle shown in Figure 15-6 is identical as shown in Figure 15-4 as process.The purpose of electro ultrafiltration be control with
Strengthen electrochemical reaction, electro ultrafiltration can come from external power supply, can come from the chemical potential in electrochemical reaction, can be from
By the electric energy (for example, electric energy through capacitor or oscillating circuit) etc. of storing process.Electro ultrafiltration consumes electric energy, but in electro ultrafiltration mistake
The electric energy consumed in journey is not lost, and is stored at electrode, is released together when electric current is reversed.
Embodiment 21
Figure 15-7 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), CH3OH and O2Mixture contacted with electrode A and CH3OH and O2Mixture contacted with electrode B and
And the process chart that electro ultrafiltration participates in, electrochemical appliance of the invention optionally work according to following courses of work.
In Figure 15-7,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.In addition to reducing agent is with CH3OH is representative,
Oxidant is with O2Outer to represent, principle shown in Figure 15-7 is identical as shown in Figure 15-4 as process.Furthermore and shown in Figure 15-4
Principle compared with process, the principle shown in Figure 15-7 and in the process H2O takes part in electrochemical reaction mistake as recycled material
Journey.The purpose of electro ultrafiltration is that control can come from external power supply, it is anti-to can come from electrochemistry with electrochemical reaction, electro ultrafiltration is strengthened
Chemical potential in answering can be from the electric energy (for example, electric energy through capacitor or oscillating circuit) etc. by storing process.Electricity
Effect consumption electric energy, but the electric energy consumed during electro ultrafiltration is not lost, and be stored at electrode, to electric current
It is released together when reversed.
Embodiment 22
Figure 15-8 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), substance A and substance B alternately contacts with electrode A and substance B and substance A replace with electrode B contact and
The process chart that electro ultrafiltration participates in, electrochemical appliance of the invention optionally work according to following courses of work.
In Figure 15-8,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer, and A representative species A (reducing agent), B are represented
Substance B (oxidant).When substance A is contacted with electrode A and substance B and electrode B contact (1. shown process in figure), substance A exists
Electrode A forming material A cation A+(i.e. reducing agent cation A+) and electronics, substance B is in electrode B serious hope electronics (because electronegativity is inhaled
Draw affine electronics), the electronics of electrode A is exported to electrode B (substance B in some cases under the action of the electro ultrafiltration of application
It can receive and electronically form substance B anion B—Or oxidant anion B—, do not show in figure), as the A of electrode A+(or electrode
The electronics of B or the B of electrode B—) when running up to setting degree, substance A and substance B switch (in such as figure 3. and 4. shown in) and
Electronics imported into electrode A from electrode B through load 5a, occurs to generate substance A and substance B oxidation at this time in electrode A and electrode B
The reaction (5. shown in such as figure) of reduction reaction product C.Because substance B has strong electronegativity, therefore works as from substance B, substance A
It will form substance B, substance A cation A with when exporting electronics in the coexistence state of electronics+With electronics coexistence state, and then three react
Generate C.Next two-way can be divided to continue, is as 5. passed through in figure all the wayShown in 1., and in process1. locating again
Secondary switching substance A and substance B, and then realize cycle operation in cycles；Another way is as 5. passed through in figureShown in 7., i.e.,
It carries out that substance B is maintained to contact with electrode A, substance A is contacted with electrode B, and applies the electro ultrafiltration of opposite direction, when the electricity of electrode A
Son (electronics and substance B coexists in electrode A or electronics is in electrode A and substance B forming material B anion or oxidant anion
B—, do not show in figure, in B—In the presence of, work as B—When running up to setting degree) when running up to setting degree or when electrode B A+Product
When tiring out setting degree (9. shown in such as figure), switches substance A and substance B and electronics is made to export to electricity from electrode A through load 5a
Pole B (in such as figure 10. withIt is shown), the reaction of generation C at this moment occurs (in such as figure in electrode A and electrode BIt is shown), continue
Maintain substance A contact with electrode A and state that substance B is contacted with electrode B reach in figure 1. shown in process, and then realization it is all and
Renew cycle operation.The purpose of electro ultrafiltration is that control can come from external power supply, can come with electrochemical reaction, electro ultrafiltration is strengthened
From the chemical potential in electrochemical reaction, the electric energy by storing process can be from (for example, the electricity through capacitor or oscillating circuit
Can) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, and is stored in electrode
Place, is released together when electric current is reversed.
Embodiment 23
Figure 15-9 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), H2And O2It is alternately contacted and O with electrode A2And H2With electrode B alternately contact and also electro ultrafiltration participation
Process chart, electrochemical appliance of the invention optionally work according to following courses of work.
In Figure 15-9,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.The principle and process and figure that this figure illustrates
Identical shown in 15-8, only the reducing agent substance A in Figure 15-8 is with H2To represent, oxidant species B is with O2To represent, reduction
Agent cation A+It is then H+.The purpose of electro ultrafiltration is control and reinforcing electrochemical reaction, and electro ultrafiltration can come from external power supply, can
With the chemical potential in electrochemical reaction, the electric energy by storing process can be from (for example, through capacitor or oscillating circuit
Electric energy) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, and is stored in
At electrode, released together when electric current is reversed.
Embodiment 24
Figure 15-10 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), CH3OH and O2Contact and O are alternateed with electrode A2And CH3OH alternateed with electrode B contact and
And the process chart that electro ultrafiltration participates in, electrochemical appliance of the invention optionally work according to following courses of work.
In Figure 15-10,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.The principle and process and figure that this figure illustrates
Identical shown in 15-8, only the reducing agent substance A in Figure 15-8 is with CH3OH is representative, and oxidant species B is with O2To represent.
Furthermore the principle shown in Figure 15-8 is compared with engineering, the principle shown in Figure 15-10 and in the process H2O is participated in as recycled material
Electrochemical reaction process.The purpose of electro ultrafiltration is control and reinforcing electrochemical reaction, and electro ultrafiltration can come from external power supply, can
With the chemical potential in electrochemical reaction, the electric energy by storing process can be from (for example, through capacitor or oscillating circuit
Electric energy) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, and is stored in
At electrode, released together when electric current is reversed.
Embodiment 25
Figure 16-1 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), O2H is contacted with electrode A2With electrode A makes discontinuous contact and O2H is contacted with electrode B2It is discontinuously connect with electrode B
The process chart that touching and electro ultrafiltration participate in, electrochemical appliance of the invention is optionally according to following course of work works
Make.
In Figure 16-1,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.In addition to reducing agent is with H2To represent, oxidation
Agent is with O2It is outer to represent, then in addition to H2Outside the influence of makes discontinuous contact, shown in principle shown in Figure 16-1 and process and Figure 15-4
It is identical.The purpose of mixture and electrode makes discontinuous contact is to reduce duration existing for reducing agent and oxidant mixture, improves safety
Property, controllability and reliability.The purpose of electro ultrafiltration is control and reinforcing electrochemical reaction, and electro ultrafiltration can come from external power supply,
It can come from the chemical potential in electrochemical reaction, can be from the electric energy by storing process (for example, through capacitor or oscillation electricity
The electric energy on road) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, but is stored
At electrode, released together when electric current is reversed.
Embodiment 26
Figure 16-2 show including electrode A (such as the present invention in electrochemistry region A) and electrode B (such as it is of the invention in
Electrochemistry region B), O2H is contacted with electrode A2With electrode A makes discontinuous contact and O2With electrode B makes discontinuous contact H2It is connect with electrode B
The process chart that touching and electro ultrafiltration participate in, electrochemical appliance of the invention is optionally according to following course of work works
Make.
In Figure 16-2,3a is electrode A, and 4a is electrode B, and 6a is interpolar spacer.In addition to reducing agent is with H2To represent, oxidation
Agent is with O2It is outer to represent, then in addition to H2、O2Outside the influence of makes discontinuous contact, shown in principle shown in Figure 16-2 and process and Figure 15-4
It is identical.The purpose of mixture and electrode makes discontinuous contact is to reduce duration existing for reducing agent and oxidant mixture, improves peace
Quan Xing, controllability and reliability.The purpose of electro ultrafiltration is control and reinforcing electrochemical reaction, and electro ultrafiltration can come from external electrical
Source can come from the chemical potential in electrochemical reaction, can be from the electric energy by storing process (for example, through capacitor or vibration
Swing the electric energy of circuit) etc..Electro ultrafiltration consumes electric energy, but the electric energy consumed during electro ultrafiltration is not lost, but by
It is stored at electrode, is released together when electric current is reversed.
Embodiment 27
The electrochemical appliance as shown in Figure 17-3, including electrochemistry region A1 and electrochemistry region B2, the electrification school district
Domain A1 is connected to setting with reducing agent feed channel 3, and the electrochemistry region A1 is connected to setting with oxidant feed channel 4, described
Electrochemistry region B2 is connected to setting with reducing agent feed channel 3, and the electrochemistry region B2 is connected to oxidant feed channel 4 and sets
It sets, the electrochemistry region A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes alternating current Jie electricity area B, institute
It is work normality that the export for stating the electronics between electrochemistry region A1 and the electrochemistry region B2, which imports,.In the present embodiment,
It is selectively chosen and plasma is set between the two poles of the earth (the electrochemistry region A1 and the electrochemistry region B2).This implementation
In example, the reducing agent, which is selectively chosen, is set as hydrogen, and the oxidant, which is selectively chosen, is set as oxygen.
Embodiment 28
The electrochemical appliance as shown in Figure 17-4, including electrochemistry region A1 and electrochemistry region B2, the electrification school district
Domain A1 is connected to setting with reducing agent feed channel 3, and the electrochemistry region A1 is connected to setting with oxidant feed channel 4, described
Electrochemistry region B2 is connected to setting with reducing agent feed channel 3, and the electrochemistry region B2 is connected to oxidant feed channel 4 and sets
It sets, the electrochemistry region A1 includes alternating current Jie electricity area A, and the electrochemistry region B2 includes alternating current Jie electricity area B, institute
It is work normality that the export for stating the electronics between electrochemistry region A1 and the electrochemistry region B2, which imports,.In the present embodiment,
It is selectively chosen and plasma is set between the two poles of the earth (the electrochemistry region A1 and the electrochemistry region B2).This implementation
The difference of example and the technical solution of embodiment 27 is to be provided with reversible electric machine 200.In the present embodiment, the reducing agent be may be selected
It selects to be set as hydrogen to property, the oxidant, which is selectively chosen, is set as oxygen.
Embodiment 29
The electrochemical appliance as shown in Figure 17-5, including electrochemistry region A1 and electrochemistry region B2, the electrification school district
Domain A1 is connected to setting, the electrochemistry region B2 and reducing agent and oxidation with the mixture feed channel 8 of reducing agent and oxidant
The mixture feed channel 8 of agent is connected to setting, and the electrochemistry region A1 includes alternating current Jie electricity area A, the electrification school district
Domain B2 includes alternating current Jie electricity area B, and the export of the electronics between the electrochemistry region A1 and the electrochemistry region B2 is led
Enter for the normality that works.In the present embodiment, it is selectively chosen in the two poles of the earth (the electrochemistry region A1 and the electrochemical school district
Domain B2) between plasma is set.In the present embodiment, the reducing agent, which is selectively chosen, is set as hydrogen, and the oxidant is optional
It selects to selecting property to be set as oxygen.
Embodiment 30
The electrochemical appliance as shown in Figure 17-6, including electrochemistry region A1 and electrochemistry region B2, the electrification school district
Domain A1 is connected to setting, the electrochemistry region B2 and reducing agent and oxidation with the mixture feed channel 8 of reducing agent and oxidant
The mixture feed channel 8 of agent is connected to setting, and the electrochemistry region A1 includes alternating current Jie electricity area A, the electrification school district
Domain B2 includes alternating current Jie electricity area B, and the export of the electronics between the electrochemistry region A1 and the electrochemistry region B2 is led
Enter for the normality that works.In the present embodiment, it is selectively chosen in the two poles of the earth (the electrochemistry region A1 and the electrochemical school district
Domain B2) between plasma is set.The difference of the technical solution of the present embodiment and embodiment 29 is to be provided with reversible electric machine 200.
In the present embodiment, the reducing agent, which is selectively chosen, is set as hydrogen, and the oxidant, which is selectively chosen, is set as oxygen.
As disposable embodiment, the aforementioned all embodiments of the present invention further can selectively select to make institute
It states reducing agent and is selectively chosen and be set as hydrogen, the oxidant, which is selectively chosen, is set as oxygen.
The principle of the electrochemical appliance of the invention is described as follows:
Figure 17-1 is the basic logic chart for exchanging electric energy for chemical energy.All are that with the process that chemical energy exchanges electric energy for
Electronics is exported from reducing agent, so that reducing agent is formed reducing agent cation, electronics is then imported into reducing agent cation and oxygen again
In the coexisting body of agent, and then realize that reducing agent cation, oxidant and electronics three react generation reducing agent and oxidant is anti-
The product that should be generated, the summation that the electronics export during this imports is to export the process of electric energy.Figure 17-1 be using hydrogen as
The diagram that the representative of reducing agent, the representative using oxygen as oxidant carry out this basic logic.
Figure 17-2 is reducing agent oxidant electrochemical reaction controlled process figure.Reducing agent and oxidant at electrode (such as
Electrochemistry region A, electrochemistry region B in the present invention) reaction that could occur, the electrochemistry that can either export electric energy is anti-
It answers, still cannot export the reducing agent of electric energy and the direct oxidation reduction reaction of oxidant, essence is all reducing agent, oxidation
Agent and electrode act on the indispensable reaction of three, and electrode to the effect of chemical reaction is realized by electro ultrafiltration.This meaning
Taste, the electrical property (or electriferous state) by changing electrode can control this kind of reaction.For example, if having electrode
There is electronegativity (ability of i.e. affine electronics is reinforced, or the ability of the affine electronics electronically formed by export), so that it may make also
Former dosage form occurs at reducing agent cation process and can be with Accelerating reduction dosage form at the process of reducing agent cation, if making electrode
With electropositivity (i.e. the ability of release electronics is reinforced, or because what importing electronically formed provides the ability of electronics), so that it may make
Oxidant react with reducing agent cation and can accelerated oxidation agent (in other words, make to aoxidize with reacting for reducing agent cation
Dosage form at oxidant anion process occur and can accelerated oxidation dosage form at oxidant anion process).It is participated in electrode
The reducing agent and oxidant of (such as catalyst participation) directly carry out needing electrode i.e. without just during redox reaction
Electricity (does not have electropositivity and does not have electronegativity yet, do not existed by the electropositivity of itself or electronegativity of electro ultrafiltration without negative electricity
This column, in other words, the electronegativity of electrode and electropositivity is needed not to be changed), otherwise redox reaction can not directly into
Row.This means that as long as we change the electrical property (changing its electropositivity, electronegativity, change its charging property) of electrode, so that it may
The process that reducing agent and oxidant directly carry out redox reaction heat release and lose output electric energy is avoided or weakened, is made with realizing
The safety and controllability that chemical energy electric energy conversion process is carried out with the mixture of reducing agent and oxidant also may be implemented to also
Probabilistic control caused by the mixed process being difficult to avoid that in former agent and oxidant handoff procedure.Figure 17-2 using hydrogen as
The representative of reducing agent, using oxygen as the representative of oxidant, using D as electrode (such as the electrochemistry region A in the present invention, electrification
School district domain B) representative, for by electrode implement electro ultrafiltration change its electrically so that control chemically react process carry out
It illustrates, in figure, D+Indicate the electrode (electrode that the ability of i.e. affine electronics is reinforced, i.e., because electronics is exported with electronegativity
The electrode that its electron affinity energy power is reinforced), D—Indicate that there is electropositive electrode (i.e. electricity that the ability of release electronics is reinforced
Pole, i.e., because electronics is imported into the electrode that its ability for discharging electronics is reinforced).
Attached drawing of the invention is only a kind of signal, and any technical solution for meeting the application literature record belongs to the application
Protection scope.
It is clear that the invention is not restricted to above embodiments, according to techniques known and technology disclosed in this invention
Scheme, can derive or associate many variant schemes out, and all these variant schemes also are regarded as being protection model of the invention
It encloses.
Claims (24)
1. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) is connected to setting with reducing agent feed channel (3), and the electrochemistry region A (1) is connected to oxidant feed channel (4)
Setting, the electrochemistry region B (2) are connected to setting, the electrochemistry region B (2) and oxidant with reducing agent feed channel (3)
Feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B, the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2) is led
Enter for the normality that works；
Or, the electrochemistry region A (1) is connected to setting, the electrochemistry region A (1) and oxidation with reducing agent feed channel (3)
Agent feed channel (4) connection setting, the electrochemistry region B (2) are connected to setting, the electrification with reducing agent feed channel (3)
School district domain B (2) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B；Reducing agent feed channel (3) is to the electrochemistry region A
(1) mistake of the process of feed reducing agent and oxidant feed channel (4) to electrochemistry region A (1) the feed oxidant
Journey alternately, process and the oxygen of the reducing agent feed channel (3) to electrochemistry region B (2) the feed reducing agent
Agent feed channel (4) to the process of electrochemistry region B (2) the feed oxidant alternately, in some time interval,
To one of described electrochemistry region A (1) feed Oxidizing and Reducing Agents, to electrochemistry region B (2) the feed oxidant
With the another kind in reducing agent；The export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2) imports
For the normality that works；
Or, the electrochemistry region A (1) is connected to setting, the electrochemistry region A (1) and oxidation with reducing agent feed channel (3)
Agent feed channel (4) connection setting, the electrochemistry region B (2) are connected to setting, the electrification with reducing agent feed channel (3)
School district domain B (2) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B；Reducing agent feed channel (3) is to the electrochemistry region A
(1) mistake of the process of feed reducing agent and oxidant feed channel (4) to electrochemistry region A (1) the feed oxidant
There is overlapping, process and the oxygen of the reducing agent feed channel (3) to electrochemistry region B (2) the feed reducing agent in journey
There is overlapping to the process of electrochemistry region B (2) the feed oxidant in agent feed channel (4)；The electrochemistry region A
(1) it is work normality that the export of the electronics between the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) is connected to setting, the electrochemistry region A (1) and oxidation with reducing agent feed channel (3)
Agent feed channel (4) connection setting, the electrochemistry region B (2) are connected to setting, the electrification with reducing agent feed channel (3)
School district domain B (2) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B；Reducing agent feed channel (3) is to the electrochemistry region A
(1) process of interrupted feed reducing agent and oxidant feed channel (4) are to the interrupted feed oxygen of the electrochemistry region A (1)
There is overlapping in the process of agent, reducing agent feed channel (3) is to the interrupted feed reducing agent of the electrochemistry region B (2)
There is overlapping to the process of the interrupted feed oxidant of the electrochemistry region B (2) in process and oxidant feed channel (4)；
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,.
2. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
In cavity A (51), the cavity A (51) is connected to setting, the cavity A with reducing agent feed channel (3) for region A (1) setting
(51) setting is connected to oxidant feed channel (4), electrochemistry region B (2) setting is in cavity B (52), the cavity B
(52) setting is connected to reducing agent feed channel (3), the cavity B (52) is connected to setting with oxidant feed channel (4), described
Electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternating current Jie electricity area B, described
It is work normality that the export of electronics between electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent feed channel (3) are even
Logical setting, the cavity A (51) are connected to setting with oxidant feed channel (4), and the electrochemistry region B (2) is arranged in cavity B
(52) in, the cavity B (52) is connected to setting, the cavity B (52) and oxidant feed channel with reducing agent feed channel (3)
(4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternation
Electric current Jie electricity area B；Process and the oxidant of the reducing agent feed channel (3) to cavity A (51) the feed reducing agent
Alternately to the process of cavity A (51) the feed oxidant, reducing agent feed channel (3) is to institute in feed channel (4)
The process for stating cavity B (52) feed reducing agent and oxidant feed channel (4) are to cavity B (52) the feed oxidant
Process alternately, in some time interval, to one of described cavity A (51) feed Oxidizing and Reducing Agents, to institute
State the another kind in cavity B (52) feed Oxidizing and Reducing Agents；The electrochemistry region A (1) and the electrochemistry region B
(2) it is work normality that the export of the electronics between, which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent feed channel (3) are even
Logical setting, the cavity A (51) are connected to setting with oxidant feed channel (4), and the electrochemistry region B (2) is arranged in cavity B
(52) in, the cavity B (52) is connected to setting, the cavity B (52) and oxidant feed channel with reducing agent feed channel (3)
(4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternation
Electric current Jie electricity area B；Process and the oxidant of the reducing agent feed channel (3) to cavity A (51) the feed reducing agent
There is overlapping to the process of cavity A (51) the feed oxidant in feed channel (4), reducing agent feed channel (3) is to institute
The process for stating cavity B (52) feed reducing agent and oxidant feed channel (4) are to cavity B (52) the feed oxidant
There is overlapping in process；It is work that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,
Normality；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent feed channel (3) are even
Logical setting, the cavity A (51) are connected to setting with oxidant feed channel (4), and the electrochemistry region B (2) is arranged in cavity B
(52) in, the cavity B (52) is connected to setting, the cavity B (52) and oxidant feed channel with reducing agent feed channel (3)
(4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternation
Electric current Jie electricity area B；Process and the oxygen of the reducing agent feed channel (3) to the interrupted feed reducing agent of the cavity A (51)
There is overlapping, reducing agent feed channel to the process of the interrupted feed oxidant of the cavity A (51) in agent feed channel (4)
(3) to the process and oxidant feed channel (4) of the interrupted feed reducing agent of the cavity B (52) to the cavity B (52)
There is overlapping in the process of interrupted feed oxidant；Electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
Export import be work normality.
3. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) and the electrochemistry region B (2) setting is in cavity (5), and the cavity (5) and reducing agent feed channel (3) are even
Logical setting, the cavity (5) are connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes alternating current
The area Jie electricity A, the electrochemistry region B (2) include alternating current Jie electricity area B, the electrochemistry region A (1) and the electrochemistry
It is work normality that the export of electronics between region B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting be in the cavity (5), the cavity (5) with also
Former agent feed channel (3) connection setting, the cavity (5) are connected to setting, the electrochemistry region with oxidant feed channel (4)
A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternating current Jie electricity area B, the reducing agent feed
The process of channel (3) feed reducing agent and the process of oxidant feed channel (4) feed oxidant alternately, the electricity
It is work normality that the export of electronics between chemical regions A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting be in the cavity (5), the cavity (5) with also
Former agent feed channel (3) connection setting, the cavity (5) are connected to setting, the electrochemistry region with oxidant feed channel (4)
A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternating current Jie electricity area B, the reducing agent feed
There is overlapping, the electricity in the process of channel (3) feed reducing agent and the process of oxidant feed channel (4) feed oxidant
It is work normality that the export of electronics between chemical regions A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting be in the cavity (5), the cavity (5) with also
Former agent feed channel (3) connection setting, the cavity (5) are connected to setting, the electrochemistry region with oxidant feed channel (4)
A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternating current Jie electricity area B, the reducing agent feed
The confession of the interrupted feed oxidant of feed process and oxidant feed channel (4) of the interrupted feed reducing agent in channel (3) passes through
There is overlapping in journey, it is that work is normal that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,
State.
4. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) is connected to setting, electrochemistry region A (1) warp with reducing agent feed channel (3) through reducing agent control switch A (61)
Oxidant control switch A (71) is connected to setting with oxidant feed channel (4), and the electrochemistry region B (2) controls through reducing agent
Switch B (62) is connected to setting with reducing agent feed channel (3), and the electrochemistry region B (2) is through oxidant control switch B (72)
Setting is connected to oxidant feed channel (4), the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry
Region B (2) includes alternating current Jie electricity area B, the electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
Export import be work normality；
Or, the electrochemistry region A (1) is connected to setting, institute with reducing agent feed channel (3) through reducing agent control switch A (61)
It states electrochemistry region A (1) and is connected to setting, the electrification school district with oxidant feed channel (4) through oxidant control switch A (71)
Domain B (2) is connected to setting with reducing agent feed channel (3) through reducing agent control switch B (62), and the electrochemistry region B (2) is through oxygen
Agent control switch B (72) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes that alternating current connects
Electric area A, the electrochemistry region B (2) include alternating current Jie electricity area B；The reducing agent control switch A (61) is by control device
Control and the oxidant control switch A (71) are controlled by control device realizes that reducing agent feed channel (3) feed restores
The process of agent and the process of oxidant feed channel (4) feed oxidant alternately, the reducing agent control switch B
(62) it is controlled by control device and the oxidant control switch B (72) is controlled by control device and realizes that the reducing agent feed is logical
The process of road (3) feed reducing agent and the process of oxidant feed channel (4) feed oxidant alternately, certain for the moment
Between interval in, to one of described electrochemistry region A (1) feed Oxidizing and Reducing Agents, to the electrochemistry region B (2)
Another kind in feed Oxidizing and Reducing Agents；Electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
Export import be work normality；
Or, the electrochemistry region A (1) is connected to setting, institute with reducing agent feed channel (3) through reducing agent control switch A (61)
It states electrochemistry region A (1) and is connected to setting, the electrification school district with oxidant feed channel (4) through oxidant control switch A (71)
Domain B (2) is connected to setting with reducing agent feed channel (3) through reducing agent control switch B (62), and the electrochemistry region B (2) is through oxygen
Agent control switch B (72) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes that alternating current connects
Electric area A, the electrochemistry region B (2) include alternating current Jie electricity area B；The reducing agent control switch A (61) is by control device
Control and the oxidant control switch A (71) are controlled by control device realizes that reducing agent feed channel (3) feed restores
There is overlapping in the process of agent and the process of oxidant feed channel (4) feed oxidant, state reducing agent control switch B (62)
It is controlled by control device and the oxidant control switch B (72) is controlled by control device and realizes reducing agent feed channel
(3) there is overlapping in the process of feed reducing agent and the process of oxidant feed channel (4) feed oxidant；The electrochemistry
It is work normality that the export of electronics between region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) is connected to setting, institute with reducing agent feed channel (3) through reducing agent control switch A (61)
It states electrochemistry region A (1) and is connected to setting, the electrification school district with oxidant feed channel (4) through oxidant control switch A (71)
Domain B (2) is connected to setting with reducing agent feed channel (3) through reducing agent control switch B (62), and the electrochemistry region B (2) is through oxygen
Agent control switch B (72) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes that alternating current connects
Electric area A, the electrochemistry region B (2) include alternating current Jie electricity area B；The reducing agent control switch A (61) is by control device
Control and the oxidant control switch A (71) are controlled by control device realizes reducing agent feed channel (3) interrupted feed
There is overlapping in the feed process of the interrupted feed oxidant of the feed process of reducing agent and oxidant feed channel (4), described
Reducing agent control switch B (62) is controlled by control device and the oxidant control switch B (72) by control device is controlled realization
The feed process and oxidant feed channel (4) interrupted feed of the interrupted feed reducing agent in reducing agent feed channel (3)
There is overlapping in the feed process of oxidant；Electronics between the electrochemistry region A (1) and the electrochemistry region B (2) is led
Import out is work normality；
Or, the electrochemistry region A (1) is connected to setting, institute with reducing agent feed channel (3) through reducing agent control switch A (61)
It states electrochemistry region A (1) and is connected to setting, the electrification school district with oxidant feed channel (4) through oxidant control switch A (71)
Domain B (2) is connected to setting with reducing agent feed channel (3) through reducing agent control switch B (62), and the electrochemistry region B (2) is through oxygen
Agent control switch B (72) is connected to setting with oxidant feed channel (4), and the electrochemistry region A (1) includes that alternating current connects
Electric area A, the electrochemistry region B (2) include alternating current Jie electricity area B；Make the reducing agent control switch A (61) and the oxygen
Agent control switch A (71) is controlled by control device realizes that the reducing agent control switch A (61) opens and makes the oxidant
Control switch A (71) discontinuously open and make the reducing agent control switch B (62) and the oxidant control switch B (72) by
Control device control realizes that the reducing agent control switch B (62) opens and opens the oxidant control switch B (72) discontinuously
It opens, or, controlling the reducing agent control switch A (61) and the oxidant control switch A (71) by control device realizes institute
Oxidant control switch A (71) is stated to open and the reducing agent control switch A (61) is made discontinuously to open and make the reducing agent
Control switch B (62) and the oxidant control switch B (72) are controlled by control device realizes the oxidant control switch B
(72) it opens and opens the reducing agent control switch B (62) discontinuously, or make the reducing agent control switch A (61) and described
Oxidant control switch A (71) is controlled by control device realizes that the reducing agent control switch A (61) opens and makes the oxidation
Agent control switch A (71) is discontinuously opened and is made the reducing agent control switch B (62) and the oxidant control switch B (72)
It is controlled by control device and realizes that the oxidant control switch B (72) opens and keeps the reducing agent control switch B (62) interrupted
It opens；It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) is connected to setting with reducing agent feed channel (3), the electrochemistry region A (1) is through aoxidizing
Agent control switch A (71) is connected to setting, the electrochemistry region B (2) and reducing agent feed channel with oxidant feed channel (4)
(3) connection setting, the electrochemistry region B (2), which is connected to through oxidant control switch B (72) with oxidant feed channel (4), to be set
It sets, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes the area alternating current Jie electricity
B；It controls the oxidant control switch A (71) by control device and realizes that the oxidant control switch A (71) is discontinuously opened
And it controls the oxidant control switch B (72) by control device and realizes that the oxidant control switch B (72) is discontinuously opened
It opens；It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) is connected to setting with oxidant feed channel (4), the electrochemistry region A (1) is through restoring
Agent control switch A (61) is connected to setting, the electrochemistry region B (2) and oxidant feed channel with reducing agent feed channel (3)
(4) connection setting, the electrochemistry region B (2), which is connected to through reducing agent control switch B (62) with reducing agent feed channel (3), to be set
It sets, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes the area alternating current Jie electricity
B；It controls the reducing agent control switch A (61) by control device and realizes that the reducing agent control switch A (61) is discontinuously opened
And it controls the reducing agent control switch B (62) by control device and realizes that the reducing agent control switch B (62) is discontinuously opened
It opens；It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) is connected to setting with reducing agent feed channel (3), the electrochemistry region A (1) is through aoxidizing
Agent control switch A (71) is connected to setting, the electrochemistry region B (2) and oxidant feed channel with oxidant feed channel (4)
(4) connection setting, the electrochemistry region B (2), which is connected to through reducing agent control switch B (62) with reducing agent feed channel (3), to be set
It sets, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes the area alternating current Jie electricity
B；It controls the oxidant control switch A (71) by control device and realizes that the oxidant control switch A (71) is discontinuously opened
And it controls the reducing agent control switch B (62) by control device and realizes that the reducing agent control switch B (62) is discontinuously opened
It opens；It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,.
5. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) setting is in cavity A (51), and the cavity A (51) is through reducing agent control switch A (61) and reducing agent feed channel
(3) connection setting, the cavity A (51) are connected to setting, institute with oxidant feed channel (4) through oxidant control switch A (71)
Electrochemistry region B (2) setting is stated in cavity B (52), the cavity B (52) is through reducing agent control switch B (62) and reducing agent
Feed channel (3) connection setting, the cavity B (52) are connected to through oxidant control switch B (72) with oxidant feed channel (4)
Setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes that alternating current connects electricity
Area B, it is work normality that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) is through reducing agent control switch A (61)
Setting is connected to reducing agent feed channel (3), the cavity A (51) is logical through oxidant control switch A (71) and oxidant feed
Road (4) connection setting, in cavity B (52), the cavity B (52) is opened through reducing agent control for electrochemistry region B (2) setting
It closes B (62) and is connected to setting with reducing agent feed channel (3), the cavity B (52) is through oxidant control switch B (72) and oxidant
Feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B；The reducing agent control switch A (61) is controlled and the oxidant control switch by control device
A (71) is controlled the process and the oxidant feed for realizing reducing agent feed channel (3) feed reducing agent by control device
Alternately, the reducing agent control switch B (62) is controlled and the oxygen process of channel (4) feed oxidant by control device
Agent control switch B (72) is controlled process and the institute for realizing reducing agent feed channel (3) feed reducing agent by control device
The process of oxidant feed channel (4) feed oxidant is stated alternately, in some time interval, to the electrochemistry region
One of A (1) feed Oxidizing and Reducing Agents, to another in electrochemistry region B (2) the feed Oxidizing and Reducing Agents
Kind；It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) is through reducing agent control switch A (61)
Setting is connected to reducing agent feed channel (3), the cavity A (51) is logical through oxidant control switch A (71) and oxidant feed
Road (4) connection setting, in cavity B (52), the cavity B (52) is opened through reducing agent control for electrochemistry region B (2) setting
It closes B (62) and is connected to setting with reducing agent feed channel (3), the cavity B (52) is through oxidant control switch B (72) and oxidant
Feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B；The reducing agent control switch A (61) is controlled and the oxidant control switch by control device
A (71) is controlled the process and the oxidant feed for realizing reducing agent feed channel (3) feed reducing agent by control device
There is overlapping in the process of channel (4) feed oxidant, the reducing agent control switch B (62) is controlled and the oxygen by control device
Agent control switch B (72) is controlled process and the institute for realizing reducing agent feed channel (3) feed reducing agent by control device
There is overlapping in the process for stating oxidant feed channel (4) feed oxidant；The electrochemistry region A (1) and the electrochemical school district
It is work normality that the export of electronics between domain B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) is through reducing agent control switch A (61)
Setting is connected to reducing agent feed channel (3), the cavity A (51) is logical through oxidant control switch A (71) and oxidant feed
Road (4) connection setting, in cavity B (52), the cavity B (52) is opened through reducing agent control for electrochemistry region B (2) setting
It closes B (62) and is connected to setting with reducing agent feed channel (3), the cavity B (52) is through oxidant control switch B (72) and oxidant
Feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B；The reducing agent control switch A (61) is controlled and the oxidant control switch by control device
A (71) is controlled by control device realizes reducing agent feed channel (3) discontinuously the feed process of feed reducing agent and described oxygen
There is overlapping in the feed process of the interrupted feed oxidant in agent feed channel (4), the reducing agent control switch B (62) is controlled
Device control and the oxidant control switch B (72) are controlled by control device realizes that reducing agent feed channel (3) are interrupted
There is overlapping in the feed process of the interrupted feed oxidant of the feed process of feed reducing agent and oxidant feed channel (4)；
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) is through reducing agent control switch A (61)
Setting is connected to reducing agent feed channel (3), the cavity A (51) is logical through oxidant control switch A (71) and oxidant feed
Road (4) connection setting, in cavity B (52), the cavity B (52) is opened through reducing agent control for electrochemistry region B (2) setting
It closes B (62) and is connected to setting with reducing agent feed channel (3), the cavity B (52) is through oxidant control switch B (72) and oxidant
Feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B；Control the reducing agent control switch A (61) and the oxidant control switch A (71)
Device control realize the reducing agent control switch A (61) open and open the oxidant control switch A (71) discontinuously and
And control the reducing agent control switch B (62) and the oxidant control switch B (72) described in realization also by control device
Former agent control switch B (62) opens and opens the oxidant control switch B (72) discontinuously, or, controlling the reducing agent
Switch A (61) and the oxidant control switch A (71) are controlled by control device realizes that the oxidant control switch A (71) is opened
It opens and the reducing agent control switch A (61) is made discontinuously to open and make the reducing agent control switch B (62) and the oxidation
Agent control switch B (72) is controlled by control device realizes that the oxidant control switch B (72) opens and makes the reducing agent control
It makes switch B (62) discontinuously to open, or keeps the reducing agent control switch A (61) and the oxidant control switch A (71) controlled
Device control processed realizes that the reducing agent control switch A (61) opens and opens the oxidant control switch A (71) discontinuously
And control the reducing agent control switch B (62) and the oxidant control switch B (72) described in realization by control device
Oxidant control switch B (72) is opened and is opened the reducing agent control switch B (62) discontinuously；The electrochemistry region A (1)
It is work normality that the export of electronics between the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent feed channel (3) are even
Logical setting, the cavity A (51) are connected to setting, the electrification with oxidant feed channel (4) through oxidant control switch A (71)
In cavity B (52), the cavity B (52) is connected to setting, the cavity with reducing agent feed channel (3) for school district domain B (2) setting
B (52) is connected to setting with oxidant feed channel (4) through oxidant control switch B (72), and the electrochemistry region A (1) includes
Alternating current Jie electricity area A, the electrochemistry region B (2) include alternating current Jie electricity area B, the oxidant control switch A (71)
Interrupted unlatching is controlled by control device, the oxidant control switch B (72) is controlled interrupted unlatching by control device；The electrification
It is work normality that the export of electronics between school district domain A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and oxidant feed channel (4) are even
Logical setting, the cavity A (51) are connected to setting, the electrification with reducing agent feed channel (3) through reducing agent control switch A (61)
In cavity B (52), the cavity B (52) is connected to setting, the cavity with oxidant feed channel (4) for school district domain B (2) setting
B (52) is connected to setting with reducing agent feed channel (3) through reducing agent control switch B (62), and the electrochemistry region A (1) includes
Alternating current Jie electricity area A, the electrochemistry region B (2) include alternating current Jie electricity area B, the reducing agent control switch A (61)
Interrupted unlatching is controlled by control device, the reducing agent control switch B (62) is controlled interrupted unlatching by control device；The electrification
It is work normality that the export of electronics between school district domain A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent feed channel (3) are even
Logical setting, the cavity A (51) are connected to setting, the electrification with oxidant feed channel (4) through oxidant control switch A (71)
In cavity B (52), the cavity B (52) is connected to setting, the cavity with oxidant feed channel (4) for school district domain B (2) setting
B (52) is connected to setting with reducing agent feed channel (3) through reducing agent control switch B (62), and the electrochemistry region A (1) includes
Alternating current Jie electricity area A, the electrochemistry region B (2) include alternating current Jie electricity area B, the oxidant control switch A (71)
Interrupted unlatching is controlled by control device, the reducing agent control switch B (62) is controlled interrupted unlatching by control device；The electrification
It is work normality that the export of electronics between school district domain A (1) and the electrochemistry region B (2), which imports,.
6. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) and the electrochemistry region B (2) setting in the cavity (5), the cavity (5) through reducing agent control switch (6) with
Reducing agent feed channel (3) connection setting, the cavity (5) connect through oxidant control switch (7) and oxidant feed channel (4)
Logical setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes that alternating current connects
Electric area B, it is work normality that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting are in cavity (5), the cavity (5) is through also
Former agent control switch (6) is connected to setting with reducing agent feed channel (3), and the cavity (5) is through oxidant control switch (7) and oxygen
Agent feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B
It (2) include alternating current Jie electricity area B, the reducing agent control switch (6) is controlled by control device and oxidant control is opened
It closes (7) and is controlled the process and the oxidant feed for realizing reducing agent feed channel (3) feed reducing agent by control device
The process of channel (4) feed oxidant alternately, between the electrochemistry region A (1) and the electrochemistry region B (2)
It is work normality that the export of electronics, which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting are in cavity (5), the cavity (5) is through also
Former agent control switch (6) is connected to setting with reducing agent feed channel (3), and the cavity (5) is through oxidant control switch (7) and oxygen
Agent feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B
It (2) include alternating current Jie electricity area B, the reducing agent control switch (6) is controlled by control device and oxidant control is opened
It closes (7) and is controlled the process and the oxidant feed for realizing reducing agent feed channel (3) feed reducing agent by control device
There is overlapping in the process of channel (4) feed oxidant, between the electrochemistry region A (1) and the electrochemistry region B (2)
It is work normality that the export of electronics, which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting are in cavity (5), the cavity (5) is through also
Former agent control switch (6) is connected to setting with reducing agent feed channel (3), and the cavity (5) is through oxidant control switch (7) and oxygen
Agent feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B
It (2) include alternating current Jie electricity area B, the reducing agent control switch (6) is controlled by control device and oxidant control is opened
It closes (7) and is controlled the feed process for realizing reducing agent feed channel (3) interrupted feed reducing agent and described oxygen by control device
There is overlapping, the electrochemistry region A (1) and the electrification in the feed process of the interrupted feed oxidant in agent feed channel (4)
It is work normality that the export of electronics between school district domain B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting are in cavity (5), the cavity (5) is through also
Former agent control switch (6) is connected to setting with reducing agent feed channel (3), and the cavity (5) is through oxidant control switch (7) and oxygen
Agent feed channel (4) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B
It (2) include alternating current Jie electricity area B；So that the reducing agent control switch (6) is controlled realization unlatching by control device and makes described
Oxidant control switch (7) is controlled realization by control device and is discontinuously opened, or fills the reducing agent control switch (6) by control
Control realization is set discontinuously to open and the oxidant control switch (7) is made to be controlled realization unlatching by control device；The electrochemistry
It is work normality that the export of electronics between region A (1) and the electrochemistry region B (2), which imports,.
7. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) is connected to setting, the electrochemistry region A (1) and oxidant feed channel A (41) with reducing agent feed channel A (31)
Connection setting, the electrochemistry region B (2) are connected to setting with reducing agent feed channel B (32), the electrochemistry region B (2) and
Oxidant feed channel B (42) connection setting, in reducing agent feed channel A (31) or in oxidant feed channel A
(41) control switch A (711) are set on, in reducing agent feed channel B (32) or in oxidant feed channel B (42)
Upper setting control switch B (722), the electrochemistry region A (1) include alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B, the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2) is led
Enter for the normality that works；
Or, the electrochemistry region A (1) is connected to setting, the electrochemistry region A (1) and oxygen with reducing agent feed channel A (31)
Agent feed channel A (41) connection setting, the electrochemistry region B (2) are connected to setting, institute with reducing agent feed channel B (32)
It states electrochemistry region B (2) and is connected to setting with oxidant feed channel B (42), in reducing agent feed channel A (31) or in institute
Setting control switch A (711) on oxidant feed channel A (41) is stated, in reducing agent feed channel B (32) or in the oxygen
Control switch B (722) are set on agent feed channel B (42), the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B, the control switch A (711) and the control switch B (722)
It is controlled by control device and is alternately opened, the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
Importing is work normality；
Or, the electrochemistry region A (1) is connected to setting, the electrochemistry region A (1) and oxygen with reducing agent feed channel A (31)
Agent feed channel A (41) connection setting, the electrochemistry region B (2) are connected to setting, institute with reducing agent feed channel B (32)
It states electrochemistry region B (2) and is connected to setting with oxidant feed channel B (42), in reducing agent feed channel A (31) or in institute
Setting control switch A (711) on oxidant feed channel A (41) is stated, in reducing agent feed channel B (32) or in the oxygen
Control switch B (722) are set on agent feed channel B (42), the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B, the control switch A (711) and the control switch B (722)
It is controlled by control device and is opened in the presence of overlapping, the electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
It is work normality that export, which imports,；
Or, the electrochemistry region A (1) is connected to setting, the electrochemistry region A (1) and oxygen with reducing agent feed channel A (31)
Agent feed channel A (41) connection setting, the electrochemistry region B (2) are connected to setting, institute with reducing agent feed channel B (32)
It states electrochemistry region B (2) and is connected to setting with oxidant feed channel B (42), in reducing agent feed channel A (31) or in institute
Setting control switch A (711) on oxidant feed channel A (41) is stated, in reducing agent feed channel B (32) or in the oxygen
Control switch B (722) are set on agent feed channel B (42), the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B；The control switch A (711) is set to be controlled realization by control device
Reducing agent described in feed is continued to the electrochemistry region A (1) and is aoxidized to described in the electrochemistry region A (1) discontinuously feed
Agent and make the control switch B (722) by control device controlled realization the electrochemistry region B (2) is continued described in feed
Reducing agent and to the interrupted oxidant described in feed of the electrochemistry region B (2), or fill the control switch A (711) by control
It sets control and realizes and oxidant described in feed is continued to the electrochemistry region A (1) and the electrochemistry region A (1) is discontinuously supplied
It send the reducing agent and the control switch B (722) is made to be controlled realization by control device and the electrochemistry region B (2) is held
Oxidant described in continuous feed and to reducing agent described in the electrochemistry region B (2) discontinuously feed, or make the control switch A
(711) realization is controlled by control device reducing agent described in feed is continued to the electrochemistry region A (1) and to the electrochemical school district
Domain A (1) discontinuously oxidant described in feed and control the control switch B (722) by control device to realize to the electrification
School district domain B (2) continues oxidant described in feed and to reducing agent described in the electrochemistry region B (2) discontinuously feed, the electrification
It is work normality that the export of electronics between school district domain A (1) and the electrochemistry region B (2), which imports,.
8. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
In cavity A (51), the cavity A (51) is connected to setting, the cavity with reducing agent feed channel A (31) for region A (1) setting
A (51) is connected to setting with oxidant feed channel A (41), and electrochemistry region B (2) setting is in cavity B (52), the chamber
Body B (52) is connected to setting with reducing agent feed channel B (32), and the cavity B (52) is connected to oxidant feed channel B (42) to be set
It sets, control switch A (711) is set in reducing agent feed channel A (31) or on oxidant feed channel A (41),
In reducing agent feed channel B (32) or on oxidant feed channel B (42), control switch B (722) are set, it is described
Electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternating current Jie electricity area B, described
It is work normality that the export of electronics between electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is interior in cavity A (51), the cavity A (51) and reducing agent feed channel A (31)
Connection setting, the cavity A (51) are connected to setting with oxidant feed channel A (41), and electrochemistry region B (2) setting exists
In cavity B (52), the cavity B (52) is connected to setting, the cavity B (52) and oxidant with reducing agent feed channel B (32)
Feed channel B (42) connection setting, in reducing agent feed channel A (31) or on oxidant feed channel A (41)
It is arranged control switch A (711), is arranged in reducing agent feed channel B (32) or on oxidant feed channel B (42)
Control switch B (722), the electrochemistry region A (1) include alternating current Jie electricity area A, and the electrochemistry region B (2) includes handing over
Time-dependent current Jie electricity area B, the control switch A (711) and the control switch B (722) are controlled by control device and are alternately opened, institute
It is work normality that the export for stating the electronics between electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is interior in cavity A (51), the cavity A (51) and reducing agent feed channel A (31)
Connection setting, the cavity A (51) are connected to setting with oxidant feed channel A (41), and electrochemistry region B (2) setting exists
In cavity B (52), the cavity B (52) is connected to setting, the cavity B (52) and oxidant with reducing agent feed channel B (32)
Feed channel B (42) connection setting, in reducing agent feed channel A (31) or on oxidant feed channel A (41)
It is arranged control switch A (711), is arranged in reducing agent feed channel B (32) or on oxidant feed channel B (42)
Control switch B (722), the electrochemistry region A (1) include alternating current Jie electricity area A, and the electrochemistry region B (2) includes handing over
Time-dependent current Jie electricity area B, the control switch A (711) and the control switch B (722) are controlled by control device and are opened in the presence of overlapping
It opens, it is work normality that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is interior in cavity A (51), the cavity A (51) and reducing agent feed channel A (31)
Connection setting, the cavity A (51) are connected to setting with oxidant feed channel A (41), and electrochemistry region B (2) setting exists
In cavity B (52), the cavity B (52) is connected to setting, the cavity B (52) and oxidant with reducing agent feed channel B (32)
Feed channel B (42) connection setting, in reducing agent feed channel A (31) or on oxidant feed channel A (41)
It is arranged control switch A (711), is arranged in reducing agent feed channel B (32) or on oxidant feed channel B (42)
Control switch B (722), the electrochemistry region A (1) include alternating current Jie electricity area A, and the electrochemistry region B (2) includes handing over
Time-dependent current Jie electricity area B；So that the control switch A (711) is controlled realization by control device and feed institute is continued to the cavity A (51)
It states reducing agent and discontinuously oxidant described in feed and makes the control switch B (722) by control device the cavity A (51)
Control, which is realized, continues reducing agent described in feed to the cavity B (52) and to oxidant described in the interrupted feed of the cavity B (52),
Or so that the control switch A (711) is controlled realization by control device and oxidant described in feed and right is continued to the cavity A (51)
The cavity A (51) discontinuously reducing agent described in feed and control the control switch B (722) by control device to realize to institute
It states cavity B (52) and continues oxidant described in feed and to the interrupted reducing agent described in feed of the cavity B (52), or make the control
Switch A (711) is controlled realization by control device and continues reducing agent described in feed to the cavity A (51) and to the cavity A
(51) discontinuously oxidant agent described in feed and control the control switch B (722) by control device to realize to the cavity B
(52) continue oxidant described in feed and to reducing agent described in the cavity B (52) discontinuously feed；The electrochemistry region A (1)
It is work normality that the export of electronics between the electrochemistry region B (2), which imports,.
9. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrochemistry
Region A (1) is connected to setting, the electrochemistry region B (2) and reduction with the mixture feed channel (8) of reducing agent and oxidant
Agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region A (1) includes alternating current Jie electricity area A,
The electrochemistry region B (2) includes alternating current Jie electricity area B, the electrochemistry region A (1) and the electrochemistry region B (2)
Between electronics export import be work normality；
Or, the electrochemistry region A (1) is connected to setting, the electrification with the mixture feed channel (8) of reducing agent and oxidant
School district domain B (2) is connected to setting with the mixture feed channel (8) of reducing agent and oxidant, and the electrochemistry region A (1) includes
Alternating current Jie electricity area A, the electrochemistry region B (2) include alternating current Jie electricity area B, and mixture feed channel (8) is even
Continuous feed mixture, it is work that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,
Normality；
Or, the electrochemistry region A (1) is connected to setting, the electrification with the mixture feed channel (8) of reducing agent and oxidant
School district domain B (2) is connected to setting with the mixture feed channel (8) of reducing agent and oxidant, and the electrochemistry region A (1) includes
Alternating current Jie electricity area A, the electrochemistry region B (2) include alternating current Jie electricity area B, and mixture feed channel (8) is disconnected
Continuous feed mixture, it is work that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,
Normality.
10. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrification
School district domain A (1) setting is in cavity A (51), the mixture feed channel (8) of the cavity A (51) and reducing agent and oxidant
Connection setting, the electrochemistry region B (2) setting in cavity B (52), the cavity B (52) and reducing agent and oxidant
Mixture feed channel (8) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrification school district
Domain B (2) includes alternating current Jie electricity area B, the electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
It is work normality that export, which imports,；
Or, the electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent and oxidant it is mixed
Close object feed channel (8) connection setting, the electrochemistry region B (2) setting in cavity B (52), the cavity B (52) with also
Former agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region A (1) includes the area alternating current Jie electricity
A, the electrochemistry region B (2) include alternating current Jie electricity area B, mixture feed channel (8) continuous feeding mixture,
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) and reducing agent and oxidant it is mixed
Close object feed channel (8) connection setting, the electrochemistry region B (2) setting in cavity B (52), the cavity B (52) with also
Former agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region A (1) includes the area alternating current Jie electricity
A, the electrochemistry region B (2) include alternating current Jie electricity area B, the interrupted feed mixture in mixture feed channel (8),
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,.
11. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrification
School district domain A (1) and the electrochemistry region B (2) setting in the cavity (5), the cavity (5) and reducing agent and oxidant it is mixed
Object feed channel (8) connection setting is closed, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B
It (2) include alternating current Jie electricity area B, the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2)
Importing is work normality；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting be in the cavity (5), the cavity (5) with also
Former agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region A (1) includes the area alternating current Jie electricity
A, the electrochemistry region B (2) include alternating current Jie electricity area B, mixture feed channel (8) continuous feeding mixture,
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting be in the cavity (5), the cavity (5) with also
Former agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region A (1) includes the area alternating current Jie electricity
A, the electrochemistry region B (2) include alternating current Jie electricity area B, the interrupted feed mixture in mixture feed channel (8),
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,.
12. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrification
School district domain A (1) is connected to setting, institute with the mixture feed channel (8) of reducing agent and oxidant through mixture control switch A (91)
It states electrochemistry region B (2) and is connected to through mixture control switch B (92) with the mixture feed channel (8) of reducing agent and oxidant
Setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes that alternating current connects electricity
Area B, it is work normality that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, mixture feed of the electrochemistry region A (1) through mixture control switch A (91) and reducing agent and oxidant is logical
Road (8) connection setting, the mixture of the electrochemistry region B (2) through (92) and reducing agent and oxidant mixture control switch B
Feed channel (8) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B, the mixture control switch A (91) is controlled by control device realizes that the mixture feed is logical
Road (8) continuous feeding mixture, the mixture control switch B (92) is controlled by control device realizes that the mixture feed is logical
The export of road (8) continuous feeding mixture, the electronics between the electrochemistry region A (1) and the electrochemistry region B (2) is led
Enter for the normality that works；
Or, mixture feed of the electrochemistry region A (1) through mixture control switch A (91) and reducing agent and oxidant is logical
Road (8) connection setting, the mixture of the electrochemistry region B (2) through (92) and reducing agent and oxidant mixture control switch B
Feed channel (8) connection setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, the electrochemistry region B (2)
Including alternating current Jie electricity area B, the mixture control switch A (91) is controlled by control device realizes that the mixture feed is logical
Discontinuously feed mixture, the mixture control switch B (92) are controlled the realization mixture feed by control device and are led in road (8)
Discontinuously feed mixture, the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2) are led in road (8)
Enter for the normality that works.
13. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrification
School district domain A (1) setting is in cavity A (51), and the cavity A (51) is through mixture control switch (9) and reducing agent and oxidant
Mixture feed channel (8) be connected to setting, the electrochemistry region B (2) setting is in cavity B (52), the cavity B (52)
Setting, the electrochemistry region are connected to the mixture feed channel (8) of reducing agent and oxidant through mixture control switch (9)
A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes alternating current Jie electricity area B, the electrochemistry region A
(1) it is work normality that the export of the electronics between the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) through mixture control switch (9) with
Reducing agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region B (2) is arranged in cavity B (52)
Interior, the cavity B (52) is connected to the mixture feed channel (8) of reducing agent and oxidant through mixture control switch (9) and sets
It sets, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes the area alternating current Jie electricity
B, the mixture control switch (9) is controlled by control device realizes mixture feed channel (8) continuous feeding mixture,
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) is through mixture control switch A (91)
Setting is connected to the mixture feed channel (8) of reducing agent and oxidant, the electrochemistry region B (2) is arranged in cavity B (52)
Interior, the cavity B (52) is connected to through mixture control switch B (92) with the mixture feed channel (8) of reducing agent and oxidant
Setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes that alternating current connects electricity
Area B, the mixture control switch A (91) is controlled by control device realizes that mixture feed channel (8) continuous feeding is mixed
Object is closed, the mixture control switch B (92) is controlled by control device realizes that mixture feed channel (8) continuous feeding is mixed
Object is closed, it is work normality that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) through mixture control switch (9) with
Reducing agent is connected to setting with the mixture feed channel (8) of oxidant, and the electrochemistry region B (2) is arranged in cavity B (52)
Interior, the cavity B (52) is connected to the mixture feed channel (8) of reducing agent and oxidant through mixture control switch (9) and sets
It sets, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes the area alternating current Jie electricity
B, the mixture control switch (9) is controlled by control device realizes mixture feed channel (8) discontinuously feed mixture,
It is work normality that the export of electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,；
Or, electrochemistry region A (1) setting is in cavity A (51), the cavity A (51) is through mixture control switch A (91)
Setting is connected to the mixture feed channel (8) of reducing agent and oxidant, the electrochemistry region B (2) is arranged in cavity B (52)
Interior, the cavity B (52) is connected to through mixture control switch B (92) with the mixture feed channel (8) of reducing agent and oxidant
Setting, the electrochemistry region A (1) includes alternating current Jie electricity area A, and the electrochemistry region B (2) includes that alternating current connects electricity
Area B, the mixture control switch A (91) is controlled by control device realizes that mixture feed channel (8) discontinuously feed is mixed
Object is closed, the mixture control switch B (92) is controlled by control device realizes that mixture feed channel (8) discontinuously feed is mixed
Object is closed, it is work normality that the export of the electronics between the electrochemistry region A (1) and the electrochemistry region B (2), which imports,.
14. a kind of electrochemical appliance, including electrochemistry region A (1) and electrochemistry region B (2), it is characterised in that: the electrification
School district domain A (1) and the electrochemistry region B (2) setting is in cavity (5), and the cavity (5) is through mixture control switch (9)
Setting is connected to the mixture feed channel (8) of reducing agent and oxidant, the electrochemistry region A (1) includes that alternating current connects
Electric area A, the electrochemistry region B (2) include alternating current Jie electricity area B, the electrochemistry region A (1) and the electrochemical school district
It is work normality that the export of electronics between domain B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting are in cavity (5), the cavity (5) is through mixed
It closes object control switch (9) and is connected to setting, the electrochemistry region A (1) with the mixture feed channel (8) of reducing agent and oxidant
Including alternating current Jie electricity area A, the electrochemistry region B (2) includes alternating current Jie electricity area B, the mixture control switch
(9) by control device controlled realize mixture feed channel (8) continuous feeding mixture, the electrochemistry region A (1) and
It is work normality that the export of electronics between the electrochemistry region B (2), which imports,；
Or, the electrochemistry region A (1) and the electrochemistry region B (2) setting are in cavity (5), the cavity (5) is through mixed
It closes object control switch (9) and is connected to setting, the electrochemistry region A (1) with the mixture feed channel (8) of reducing agent and oxidant
Including alternating current Jie electricity area A, the electrochemistry region B (2) includes alternating current Jie electricity area B, the mixture control switch
(9) controlled by control device and realize mixture feed channel (8) discontinuously feed mixture, the electrochemistry region A (1) and
It is work normality that the export of electronics between the electrochemistry region B (2), which imports,.
15. the electrochemical appliance as described in any one of claims 1 to 8, it is characterised in that: in the reducing agent and the oxidation
Inert substance and/or dead band duration are inserted between agent.
16. the electrochemical appliance as described in any one of claims 1 to 14, it is characterised in that: the electrochemistry region A (1) with
The setting of power supply electric communication or the electrochemistry region A (1) are arranged in the electric field, and/or, the electrochemistry region B (2) and electricity
The setting of source electric communication or the electrochemistry region B (2) setting are in the electric field；Or, the electrochemistry region A (1) and the electricity
Capacitor, DC power supply, AC power source, alternating source, inductor conductor, inductance coil, band electrochondria are set between chemical regions B (2)
Sub- pump, reversing switch circuit, rectifier, electric field, oscillating circuit, motor, reversible electric machine, has additional rotation at phase converter
The motor of inertia or its two conjunction, its three conjunction, its four conjunction, its five conjunction, its six conjunction, its seven it
Conjunction, its eight conjunction, its nine conjunction, its ten conjunction, its 11 conjunction, the conjunction of its ten binomial, its 13 conjunction, its
14 conjunctions, its 15 conjunction.
17. electrochemical appliance as claimed in claim 15, it is characterised in that: the electrochemistry region A (1) and power supply electric communication
Setting or the electrochemistry region A (1) are arranged in the electric field, and/or, the electrochemistry region B (2) sets with power supply electric communication
It sets or the electrochemistry region B (2) is arranged in the electric field；Or, the electrochemistry region A (1) and the electrochemistry region B (2)
Between be arranged capacitor, DC power supply, AC power source, alternating source, inductor conductor, inductance coil, charged particle pump, phase transition
Device, reversing switch circuit, rectifier, electric field, oscillating circuit, motor, reversible electric machine, the motor with additional rotation inertia or its
Two conjunctions, its three conjunction, its four conjunction, its five conjunction, its six conjunction, its seven conjunction, its eight conjunction, its
Nine conjunctions, its ten conjunction, its 11 conjunction, the conjunction of its ten binomial, its 13 conjunction, its 14 conjunction, its ten
Five conjunctions.
18. the electrochemical appliance as described in any one of claim 1 to 14 and 17, it is characterised in that: the electrochemistry region A
(1) there is non-electronic conducting electrical relation between the electrochemistry region B (2), or, the electrochemistry region A (1) is through completely cutting off
Body, isolation space, electrolyte, dielectric, capacitor, plasma, ionic liquid, ionized gas, solion and electronic conduction
At least one of area has non-electronic conducting electrical relation with the electrochemistry region B (2).
19. electrochemical appliance as claimed in claim 15, it is characterised in that: the electrochemistry region A (1) and the electrochemical school district
There is non-electronic conducting electrical relation, or, the electrochemistry region A (1) is through insulation, isolation space, electrolysis between domain B (2)
At least one of matter, dielectric, capacitor, plasma, ionic liquid, ionized gas, solion and electronic conduction area with
The electrochemistry region B (2) has non-electronic conducting electrical relation.
20. electrochemical appliance as claimed in claim 16, it is characterised in that: the electrochemistry region A (1) and the electrochemical school district
There is non-electronic conducting electrical relation, or, the electrochemistry region A (1) is through insulation, isolation space, electrolysis between domain B (2)
At least one of matter, dielectric, capacitor, plasma, ionic liquid, ionized gas, solion and electronic conduction area with
The electrochemistry region B (2) has non-electronic conducting electrical relation.
21. the electrochemical appliance as described in any one of claim 1 to 14 and 17 and 19 and 20, it is characterised in that: the electrification
School district domain A (1) rotation setting, electrochemistry region B (2) the rotation setting.
22. electrochemical appliance as claimed in claim 15, it is characterised in that: electrochemistry region A (1) the rotation setting, it is described
Electrochemistry region B (2) rotation setting.
23. electrochemical appliance as claimed in claim 16, it is characterised in that: electrochemistry region A (1) the rotation setting, it is described
Electrochemistry region B (2) rotation setting.
24. electrochemical appliance as claimed in claim 18, it is characterised in that: electrochemistry region A (1) the rotation setting, it is described
Electrochemistry region B (2) rotation setting.
Applications Claiming Priority (40)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810977121 | 2018-08-26 | ||
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