CA2466498A1 - Electrochemical cell with gas diffusion electrodes - Google Patents

Electrochemical cell with gas diffusion electrodes Download PDF

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Publication number
CA2466498A1
CA2466498A1 CA002466498A CA2466498A CA2466498A1 CA 2466498 A1 CA2466498 A1 CA 2466498A1 CA 002466498 A CA002466498 A CA 002466498A CA 2466498 A CA2466498 A CA 2466498A CA 2466498 A1 CA2466498 A1 CA 2466498A1
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CA
Canada
Prior art keywords
cell
fed
gas diffusion
gas
planar element
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Granted
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CA002466498A
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French (fr)
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CA2466498C (en
Inventor
Giuseppe Faita
Fulvio Federico
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Thyssenkrupp Nucera Italy SRL
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Individual
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Publication of CA2466498C publication Critical patent/CA2466498C/en
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00Operating or servicing cells
    • C25B15/08Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/28Per-compounds
    • C25B1/30Peroxides
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/34Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B13/00Diaphragms; Spacing elements
    • C25B13/04Diaphragms; Spacing elements characterised by the material
    • C25B13/08Diaphragms; Spacing elements characterised by the material based on organic materials
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023Porous and characterised by the material
    • H01M8/0232Metals or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023Porous and characterised by the material
    • H01M8/0239Organic resins; Organic polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023Porous and characterised by the material
    • H01M8/0241Composites
    • H01M8/0245Composites in the form of layered or coated products
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0247Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/8605Porous electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0204Non-porous and characterised by the material
    • H01M8/0223Composites
    • H01M8/0228Composites in the form of layered or coated products
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Inorganic Chemistry (AREA)
  • Composite Materials (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Inert Electrodes (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

A membrane electrolysis cell comprising an anodic compartment and a cathodic compartment is described, wherein at least one of the two compartments contains an electrode fed with gas and a porous planar element is interposed between the membrane and the gas-fed electrode. A flow of chemically aggressive electrolyte crosses the porous planar element downwards under the effect of the gravity force. The planar element consists in a plastic elemen t withstanding the aggressive operative conditions: The use of perfluorinated plastics such as ECTFE, PTEFE, FEP, PFA is preferred, even though they are strongly hydrophobic. When the gas-fed electrode is a cathode and the gas contains oxygen, the gas crosses the cathodic compartment upwardly so as to minimise the risk of hydrogen build up. The cell equipped with the oxygen cathode is particularly advantageous for the sodium chloride electrolysis.</ SDOAB>

Claims (29)

1. A cell suitable for an electrochemical process comprising an anodic compartment containing an anode and a cathodic compartment containing a cathode separated by an ion-exchange membrane, at least one of the two anodic and cathodic compartments containing an assembly consisting in a current distributor connected to the wall of the relative compartment by means of supports, a gas diffusion electrode in contact with the surface of the current distributor and a planar porous element inserted between the membrane and the gas diffusion electrode and fed with at least one liquid reactant percolating in its interior, characterised in that the porous planar element comprises a plastic material selected from the group of high density polyethylene and fluorinated plastics.
2. The cell of claim 1 characterised in that said plastic material has hydrophobic behaviour towards said percolating reactant, with mutual contact angle not lower than 90°.
3. The cell of claim 2 characterised in that said fluorinated plastics are PTFE, ECTFE, PFA, FEP.
4. The cell of the previous claims characterised in that said plastic material is a coating applied to a metallic material.
5. The cell of the previous claims characterised in that the porous planar element comprises at least one component selected from the group of foams, planar meshes consisting in crossing and overlapping of wires, planar meshes of interwoven wires, meshes with controlled profile, mattresses of wire coils, expanded meshes, sintered layers.
6. The cell of the previous claims characterised in that the current distributor consists in a first conductive foil provided with openings overlaid to a second conductive foil provided with openings of smaller dimensions than those of said first foil, and that said second foil is in contact with said gas diffusion electrode.
7. The cell of claim 6 characterised in that said first conductive foil is rigid.
8. The cell of claim 6 characterised in that said first foil and second foil are selected from the group of the expanded meshes, meshes of wires, perforated sheets.
9. The cell of the previous claims characterised in that the current distributor supports are elastic and said current distributor exerts a compression of the gas diffusion electrode and of the porous planar element against the ion-exchange membrane.
10. The cell of the previous claims characterised in that the current distributor is divided in at least two parts.
11. The cell of claim 9 characterised in that said elastic supports comprise a conductive mattress made of coils or undulated sheets.
12. The cell of the previous claims characterised in that only one of the two anodic and cathodic compartments comprises the assembly made of current distributor, gas diffusion electrode and porous planar element, that the current distributor supports are rigid, that the internal pressure of said compartment comprising the assembly made of current distributor, gas diffusion electrode and porous planar element is lower than the pressure of the other compartment and that the membrane compresses said assembly.
13. The cell of the previous claims characterised in that the gas of the gas diffusion electrode is fed to the lower part and that the exhausted gas is discharged from the upper part of said cell.
14. The cell of claim 13 characterised in that said gas fed to the lower part is forced to a zigzag motion by baffles.
15. The cell of claim 14 characterised in that catalytic porous masses are inserted in the flow section of said gas.
16. An electrolyser consisting in a modular arrangement of elementary cells, characterised in that at least one of the cells is a cell of the previous claims.
17. The electrolyser of claim 16 characterised in that the elementary cells are in monopolar electric connection.
18. The electrolyser of claim 16 characterised in that the elementary cells are in bipolar electric connection.
19. An electrochemical process comprising the electrolysis of alkaline halides in a cell of claims 1 to 15.
20. The process of claim 19 characterised in that the cathodic compartment comprises an oxygen-fed gas diffusion cathode and a porous planar element fed with an alkaline hydroxide solution percolating in its interior.
21. The process of claim 20 characterised in that said oxygen is fed at the bottom and discharged from the top.
22. An electrochemical process comprising the production of hydrogen peroxide in a cell of claims 1 to 15.
23. The process of claim 22 characterised in that the cathodic compartment of said cell comprises an oxygen-fed gas diffusion cathode and a porous planar element fed with an alkaline hydroxide solution percolating in its interior.
24. The process of claim 23 characterised in that said oxygen is fed at the bottom and discharged from the top.
25. An electrochemical process comprising the electrolysis of alkaline sulphates in a cell of claims 1 to 15.
26. The process of claim 25 characterised in that the anodic compartment comprises a hydrogen-fed gas diffusion anode and a porous planar element fed with a sulphuric acid solution percolating in its interior, said solution optionally comprising an alkali sulphate.
27. An electrochemical process comprising the generation of electric current in an electrochemical cell of claims 1 to 15.
28. The process of claim 27 characterised in that said cell is an alkaline fuel cell, and that both compartments, anodic and cathodic, contain the assembly made of a current distributor, a gas diffusion electrode and a porous planar element.
29. An electrochemical cell comprising the distinctive features of the description and the figures.
CA2466498A 2001-11-12 2002-11-12 Electrochemical cell with gas diffusion electrodes Expired - Fee Related CA2466498C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
ITMI2001A002379 2001-11-12
IT2001MI002379A ITMI20012379A1 (en) 2001-11-12 2001-11-12 ELECTROLYSIS CELL WITH GAS DIFFUSION ELECTRODES
PCT/EP2002/012661 WO2003042430A2 (en) 2001-11-12 2002-11-12 Electrochemical cell with gas diffusion electrodes

Publications (2)

Publication Number Publication Date
CA2466498A1 true CA2466498A1 (en) 2003-05-22
CA2466498C CA2466498C (en) 2011-07-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
CA2466498A Expired - Fee Related CA2466498C (en) 2001-11-12 2002-11-12 Electrochemical cell with gas diffusion electrodes

Country Status (18)

Country Link
US (1) US7670472B2 (en)
EP (1) EP1446515B1 (en)
JP (1) JP4209777B2 (en)
KR (1) KR100939448B1 (en)
CN (1) CN1303255C (en)
AT (1) ATE509143T1 (en)
AU (1) AU2002351989B2 (en)
BR (1) BR0214015B1 (en)
CA (1) CA2466498C (en)
ES (1) ES2365604T3 (en)
HU (1) HU227835B1 (en)
IT (1) ITMI20012379A1 (en)
MA (1) MA26231A1 (en)
MX (1) MXPA04004513A (en)
PL (1) PL209191B1 (en)
RU (1) RU2303085C2 (en)
WO (1) WO2003042430A2 (en)
ZA (1) ZA200403438B (en)

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WO2005028708A3 (en) * 2003-09-12 2005-08-25 Bayer Materialscience Ag Method for the electrolysis of an aqueous solution of hydrogen chloride or chloralkali
RU2391448C2 (en) * 2003-09-12 2010-06-10 Байер Матириальсайенс Аг Method of electrolysis of aqueous solution of hydrogen chloride or alkaline metal chloride

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ZA200403438B (en) 2005-07-27
KR100939448B1 (en) 2010-01-29
ATE509143T1 (en) 2011-05-15
CA2466498C (en) 2011-07-12
RU2004117772A (en) 2005-04-10
EP1446515A2 (en) 2004-08-18
BR0214015A (en) 2004-10-13
MA26231A1 (en) 2004-07-01
JP2005509744A (en) 2005-04-14
WO2003042430A3 (en) 2004-03-11
US7670472B2 (en) 2010-03-02
RU2303085C2 (en) 2007-07-20
CN1303255C (en) 2007-03-07
ES2365604T3 (en) 2011-10-07
ITMI20012379A1 (en) 2003-05-12
HU227835B1 (en) 2012-05-02
AU2002351989B2 (en) 2007-07-19
HUP0402380A2 (en) 2005-03-29
KR20050044403A (en) 2005-05-12
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BR0214015B1 (en) 2012-09-18
WO2003042430A2 (en) 2003-05-22
CN1585836A (en) 2005-02-23
JP4209777B2 (en) 2009-01-14
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PL368714A1 (en) 2005-04-04
EP1446515B1 (en) 2011-05-11

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