WO2004076722A1 - Procede et appareil d'electrolyse destines a produire de l'hydrogene et de l'oxygene par l'electrolyse d'une solution acqueuse d'electrolyte - Google Patents

Procede et appareil d'electrolyse destines a produire de l'hydrogene et de l'oxygene par l'electrolyse d'une solution acqueuse d'electrolyte Download PDF

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Publication number
WO2004076722A1
WO2004076722A1 PCT/UA2003/000021 UA0300021W WO2004076722A1 WO 2004076722 A1 WO2004076722 A1 WO 2004076722A1 UA 0300021 W UA0300021 W UA 0300021W WO 2004076722 A1 WO2004076722 A1 WO 2004076722A1
Authority
WO
WIPO (PCT)
Prior art keywords
eleκτροliτa
κaτοdnοy
ρasτvορa
anοdnοy
eleκτροdy
Prior art date
Application number
PCT/UA2003/000021
Other languages
English (en)
Russian (ru)
Inventor
Sergey Alexandrovich PARPALEY
Original Assignee
Parpaley, Aleksandra Illinichna
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Parpaley, Aleksandra Illinichna filed Critical Parpaley, Aleksandra Illinichna
Priority to AU2003242196A priority Critical patent/AU2003242196A1/en
Publication of WO2004076722A1 publication Critical patent/WO2004076722A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • the 15 gasses includes the supply of water to elektroulizer, the introduction of water to direct anodes and the resulting gases.
  • the water supply to the electrolyzer is led to the channel for the outlet of gases and the supply of water to the clean anodes through the exhaust pipe.
  • the supply of water to the electrolyzer is carried out for all channels for the outlet of gases.
  • 15 is a chamber separated by a filter and equipped with an easy-to-clean angle for the liquid in the circulator.
  • a known electrolysis device for whitening hydrogen and oxygen from water includes anode and
  • the purpose of the invention is to provide equipment and facilities for the production of hydrogen and oxygen with minimal electric energy costs, and to eliminate the risk of electrical energy.
  • the tasks set are resolved due to the fact that the means of obtaining the hydrogen and the acid of the electric energy of the elec- tric waste are carried out
  • Cameras are forging an additional level of excitation of anions 5 and ⁇ a ⁇ i ⁇ n ⁇ v in ⁇ azdelny ⁇ ⁇ a ⁇ sve ⁇ vym ⁇ blucheniem, ⁇ as ⁇ l ⁇ zhenn ⁇ y ⁇ d ⁇ e ⁇ eg ⁇ d ⁇ y between an ⁇ dn ⁇ y and ⁇ a ⁇ dn ⁇ y ⁇ ame ⁇ ami lam ⁇ y, ⁇ aya izluchae ⁇ in ul ⁇ a ⁇ i ⁇ le ⁇ v ⁇ m s ⁇ e ⁇ e and d ⁇ lni ⁇ elnym ele ⁇ g ⁇ adien ⁇ nym ⁇ lem us ⁇ i ⁇ elya, m ⁇ n ⁇ lya ⁇ nye ele ⁇ dy ⁇ g ⁇ ⁇ as ⁇ l ⁇ zheny in an ⁇ dn ⁇ y and
  • Filters, cameras and the main part of them are located in the chamber of dissociation is not available in the electorate.
  • ⁇ a ⁇ ig. 1 shows a schematic operation of an elec- tronics
  • Fig. 2 is a sectional view of the electrical circuit of the unit.
  • Fig. 3 is a schematic diagram of the process. When an increased operation is carried out, it is recommended that the
  • electrolyser 30 of the electrolyser was manufactured electrolyser with total dimensions 9 combined anode bodies, a single camera and a dissociation chamber: length 800 mm., Width 400 mm. and a height of 200 mm. They filled the room with a front electric potassium pan, a chamber of dissociation 4, and a second chamber and a three-chamber electrically powered supply. 5 Experiments were carried out, in addition to all options in the first variant, all the processes in the declared investigation were completed:
  • the unit 10 of the elec- tric unit 10 is sold to the unit 11 for the anion and the unit is equipped with a non-removable battery, which is equipped with a non-removable battery, and is equipped with a portable appliance.
  • Electrode for the production of hydrogen and acid from the external electrical part of the unit includes the battery
  • the anode 33 and the source 34 are connected to the units, which are secured to the walls of the housing 1 and are connected to the source of the permanent source.
  • the external shut-off valve 35 and the filter 36 are connected to the catalytic converter of the fresh electrical outlet 23.
  • the ultraviolet lamp 37 is installed in the lower part of the switch 5
  • ⁇ ab ⁇ ae ⁇ ele ⁇ lize ⁇ ⁇ a ⁇ za ⁇ lnyae ⁇ sya v ⁇ d ⁇ y with ⁇ n ⁇ vym ele ⁇ li ⁇ m, na ⁇ ime ⁇ , ed ⁇ im ⁇ aliem, ⁇ ame ⁇ a diss ⁇ tsiatsii 4, 8 nas ⁇ s ⁇ m ⁇ dae ⁇ sya v ⁇ dny ⁇ as ⁇ v ⁇ ele ⁇ li ⁇ a in an ⁇ dnuyu 2 and 3 ⁇ a ⁇ dnuyu ⁇ ame ⁇ y d ⁇ ⁇ bes ⁇ echeniya ⁇ dina ⁇ v ⁇ g ⁇ u ⁇ vnya.
  • An electrical voltage is supplied to anode 33, and

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Electroluminescent Light Sources (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

L'invention concerne un procédé et un appareil d'électrolyse destinés à fabriquer de l'hydrogène et de l'oxygène par l'électrolyse d'une solution aqueuse d'électrolyte. Un groupe d'inventions liées entre elles se rapporte à la fabrication d'hydrogène et d'oxygène par l'électrolyse d'une solution aqueuse d'électrolyte, destinée à leur utilisation en tant que matière première énergétique pour le secteur de combustibles et d'énergie, dans le transport automobile et dans les systèmes publics. Le procédé consiste à dissocier l'électrolyte et à l'alimenter via le filtre et le catalyseur sur les électrodes de la cathode et de l'anode, via un canal de séparation d'ions, après quoi les flux séparés de cations dans la chambre de cathode, et d'anions dans la chambre d'anode, sont excités par illumination et par un champ à gradient supplémentaire, le flux d'anions excités est injecté dans la zone de disposition des plaques d'anode, et le flux de cations excités est injecté dans la zone de disposition des plaques de cathode. On évacue une partie de la solution aqueuse d'électrolyte usée à partir des couches supérieures de la solution aqueuse, sa désionisation dans le filtre et le catalyseur de la solution aqueuse et son alimentation dans la chambre de dissociation; de plus, on évacue en permanence une partie de l'hydrogène et de l'oxygène obtenus sur l'anode et la cathode. L'invention permet d'assurer la fabrication de dispositifs destinés à fabriquer de l'hydrogène et de l'oxygène avec des dépenses minimales d'énergie électrique.
PCT/UA2003/000021 2003-02-25 2003-06-26 Procede et appareil d'electrolyse destines a produire de l'hydrogene et de l'oxygene par l'electrolyse d'une solution acqueuse d'electrolyte WO2004076722A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2003242196A AU2003242196A1 (en) 2003-02-25 2003-06-26 Method and elecrtolyser for producing hydrogen and oxygen by electrolysing an aqueous electrolyte solution

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
UA2003021661A UA79076C2 (en) 2003-02-25 2003-02-25 Method and electrolyzer for the generation of hydrogen and oxygen by electrolysis of electrolyte aqueous solution
UA2003021661 2003-02-25

Publications (1)

Publication Number Publication Date
WO2004076722A1 true WO2004076722A1 (fr) 2004-09-10

Family

ID=34391816

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/UA2003/000021 WO2004076722A1 (fr) 2003-02-25 2003-06-26 Procede et appareil d'electrolyse destines a produire de l'hydrogene et de l'oxygene par l'electrolyse d'une solution acqueuse d'electrolyte

Country Status (2)

Country Link
UA (1) UA79076C2 (fr)
WO (1) WO2004076722A1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI668332B (zh) * 2018-12-04 2019-08-11 林信湧 堆疊式產氫裝置

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4388162A (en) * 1982-02-08 1983-06-14 Institute Of Gas Technology Continuous flow electrochemical cell and process
SU1435664A1 (ru) * 1986-12-30 1988-11-07 Предприятие П/Я Р-6878 Генератор водорода
US4790916A (en) * 1984-03-14 1988-12-13 The Texas A&M University System One-unit photo-activated electrolyzer
RU2010890C1 (ru) * 1991-05-28 1994-04-15 Общество с ограниченной ответственностью "Институт физико-технологических исследований" Способ получения кислорода и водорода
RU2092614C1 (ru) * 1994-04-05 1997-10-10 Мамедов Юрий Мусаевич Электролизер
RU2129169C1 (ru) * 1995-08-08 1999-04-20 Горбачев Евгений Александрович Устройство для электролиза воды с применением лазера
RU2174162C1 (ru) * 1998-06-22 2001-09-27 Кудымов Георгий Иванович Устройство для преобразования энергии

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4388162A (en) * 1982-02-08 1983-06-14 Institute Of Gas Technology Continuous flow electrochemical cell and process
US4790916A (en) * 1984-03-14 1988-12-13 The Texas A&M University System One-unit photo-activated electrolyzer
SU1435664A1 (ru) * 1986-12-30 1988-11-07 Предприятие П/Я Р-6878 Генератор водорода
RU2010890C1 (ru) * 1991-05-28 1994-04-15 Общество с ограниченной ответственностью "Институт физико-технологических исследований" Способ получения кислорода и водорода
RU2092614C1 (ru) * 1994-04-05 1997-10-10 Мамедов Юрий Мусаевич Электролизер
RU2129169C1 (ru) * 1995-08-08 1999-04-20 Горбачев Евгений Александрович Устройство для электролиза воды с применением лазера
RU2174162C1 (ru) * 1998-06-22 2001-09-27 Кудымов Георгий Иванович Устройство для преобразования энергии

Also Published As

Publication number Publication date
UA79076C2 (en) 2007-05-25

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