EP0170092A1 - Cellule d'électrolyse à électrodes disposées horizontalement - Google Patents
Cellule d'électrolyse à électrodes disposées horizontalement Download PDFInfo
- Publication number
- EP0170092A1 EP0170092A1 EP85108265A EP85108265A EP0170092A1 EP 0170092 A1 EP0170092 A1 EP 0170092A1 EP 85108265 A EP85108265 A EP 85108265A EP 85108265 A EP85108265 A EP 85108265A EP 0170092 A1 EP0170092 A1 EP 0170092A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cell
- membrane
- gas
- diffusion cathode
- electrolysis cell
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 9
- 239000012528 membrane Substances 0.000 claims abstract description 22
- 238000009792 diffusion process Methods 0.000 claims abstract description 13
- 125000006850 spacer group Chemical group 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 17
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 9
- 239000000460 chlorine Substances 0.000 claims description 9
- 229910052801 chlorine Inorganic materials 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000012267 brine Substances 0.000 claims description 4
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 3
- 239000000243 solution Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 7
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 5
- 229910052753 mercury Inorganic materials 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 101150114468 TUB1 gene Proteins 0.000 description 3
- 229910000497 Amalgam Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000005341 cation exchange Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910001514 alkali metal chloride Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
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
- 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
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
Definitions
- the invention relates to a trough-like electrolysis cell with horizontally arranged electrodes for producing chlorine from alkali chloride solution according to the membrane method, in which the anodes are arranged on the cell cover in a height-adjustable manner.
- the membrane cell consists of two electrolysis chambers, each with a gas-generating electrode, which are separated by a cation-selective membrane. If such a membrane cell were arranged horizontally, a gas cushion, depending on the arrangement of chlorine or hydrogen, would form under the membrane, and the electrolyte resistance would nullify the cell voltage advantage.
- the present invention achieves the object in that a gas diffusion cathode rests on a grate with support feet for support on the cell bottom and a spacer is arranged between the membrane and the gas diffusion cathode.
- the membrane can be clamped between the cell cover and the cell tub.
- the cell cover can have devices for supplying and discharging brine and chlorine and the cell trough can have devices for supplying oxygen-containing gas.
- the advantage of the invention is essentially to be seen in the fact that it is possible to inexpensively convert mercury cells into membrane cells with the advantages mentioned above.
- the electrolytic cell consists of the cell tub 1, which is connected to the negative pole of the power supply.
- This tub is provided with support feet 2 which stand on the cell floor and which carry the gas diffusion cathode 3. They also serve to supply current to the gas diffusion cathode 3.
- the support feet 2 consist of a metallic material, preferably of the same material as the cell trough, in order to ensure the best possible connection, for example by welding the support feet to the cell trough.
- the support feet 2 can be provided with a grate 4 on which the gas diffusion cathode 3 rests.
- the gas diffusion cathode 3 itself is a wire mesh or expanded metal coated with an electrochemically active catalyst, and is hydrophobized by means of a plastic, preferably polytetrafluoroethylene, in order to allow the sodium to seep through to prevent lye.
- a gas space I is created, via which the gas diffusion cathode 3 is supplied with oxygen or a gas containing oxygen, for example air.
- the gas space is provided with devices for introducing oxygen or air (not shown in the figure) and optionally with devices for disposing of excess oxygen or air depleted in oxygen (not shown in the figure).
- the cation exchange membrane 6 is clamped between the cell cover 5 and the cell tub 1. It separates the cathode compartment II, in which the sodium hydroxide solution circulates, from the anode compartment III, in which the conversion of the chloride ions to elemental chlorine takes place at a titanium or graphite anode 7.
- a spacer 8 in the cathode compartment II This can be designed in the form of a mesh made of a lye-resistant plastic or metal.
- the inlet and outlet (not shown) present in the cell tub 1 can be used for the catholyte circuit.
- the cell cover 5 is provided with devices (not shown) via which the anode compartment III is supplied with brine and the depleted brine and the chlorine formed can be disposed of.
- Graphite anodes or activated titanium anodes are used as anodes to keep the chlorine overvoltage low.
- the anodes 7 are fastened to the cell cover in a known manner in an adjustable manner. It is particularly advantageous if the membrane rests on the titanium anodes, which can be achieved with the adjustment device for the electrode spacing.
- the invention makes it possible to convert existing amalgam systems to the membrane process using a large part of the system parts. Another advantage exists when using a gas diffusion cathode in an additional cell voltage saving compared to membrane cells with a hydrogen-producing cathode, since the potential for oxygen reduction is about 1.2 volts more positive than the potential for hydrogen generation.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Electroluminescent Light Sources (AREA)
- External Artificial Organs (AREA)
- Professional, Industrial, Or Sporting Protective Garments (AREA)
- Measuring Pulse, Heart Rate, Blood Pressure Or Blood Flow (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT85108265T ATE36875T1 (de) | 1984-07-13 | 1985-07-04 | Elektrolysezelle mit horizontal angeordneten elektroden. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843425862 DE3425862A1 (de) | 1984-07-13 | 1984-07-13 | Elektrolysezelle mit horizontal angeordneten elektroden |
DE3425862 | 1984-07-13 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0170092A1 true EP0170092A1 (fr) | 1986-02-05 |
EP0170092B1 EP0170092B1 (fr) | 1988-08-31 |
Family
ID=6240568
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP85108265A Expired EP0170092B1 (fr) | 1984-07-13 | 1985-07-04 | Cellule d'électrolyse à électrodes disposées horizontalement |
Country Status (11)
Country | Link |
---|---|
US (1) | US4615783A (fr) |
EP (1) | EP0170092B1 (fr) |
AT (1) | ATE36875T1 (fr) |
AU (1) | AU573356B2 (fr) |
CA (1) | CA1254532A (fr) |
DE (2) | DE3425862A1 (fr) |
ES (1) | ES288013Y (fr) |
FI (1) | FI76837C (fr) |
IN (1) | IN164954B (fr) |
NO (1) | NO163786C (fr) |
ZA (1) | ZA855260B (fr) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4732660A (en) * | 1985-09-09 | 1988-03-22 | The Dow Chemical Company | Membrane electrolyzer |
US5209836A (en) * | 1991-12-19 | 1993-05-11 | Olin Corporation | Baseplate for electrolytic cell with a liquid metal cathode |
DE19844059A1 (de) * | 1998-09-25 | 2000-03-30 | Degussa | Elektrolysezelle und deren Verwendung |
US9222178B2 (en) | 2013-01-22 | 2015-12-29 | GTA, Inc. | Electrolyzer |
US8808512B2 (en) | 2013-01-22 | 2014-08-19 | GTA, Inc. | Electrolyzer apparatus and method of making it |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1380418A (en) * | 1971-01-27 | 1975-01-15 | Electric Power Storage Ltd | Electrolysis of chloride solutions |
EP0077982A1 (fr) * | 1981-10-22 | 1983-05-04 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Procédé électrolytique et cellule électrolytique |
EP0104137A2 (fr) * | 1982-08-26 | 1984-03-28 | Eltech Systems Corporation | Cellule d'électrolyse à électrode gazeuse et faible distance interélectrode |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1109311A (en) * | 1912-01-06 | 1914-09-01 | Edward A Allen | Method and means for electrolyzing saline solutions. |
US1187903A (en) * | 1913-06-30 | 1916-06-20 | William E Greenawalt | Electrolytic apparatus. |
US3976550A (en) * | 1971-09-22 | 1976-08-24 | Oronzio De Nora Implanti Elettrochimici S.P.A. | Horizontal, planar, bipolar diaphragm cells |
US3770611A (en) * | 1971-11-24 | 1973-11-06 | Olin Corp | Multiple tier horizontal diaphragm cells |
US4036714A (en) * | 1972-10-19 | 1977-07-19 | E. I. Du Pont De Nemours And Company, Inc. | Electrolytic cells and processes |
US3901774A (en) * | 1973-04-10 | 1975-08-26 | Tokuyama Soda Kk | Method of electrolyzing alkali metal halide solution and apparatus therefor |
US3893897A (en) * | 1974-04-12 | 1975-07-08 | Ppg Industries Inc | Method of operating electrolytic diaphragm cells having horizontal electrodes |
US3976556A (en) * | 1974-12-05 | 1976-08-24 | Oronzio De Nora Impianti Elettrochimici S.P.A. | Electrolysis cell |
FR2339684A1 (fr) * | 1976-01-30 | 1977-08-26 | Commissariat Energie Atomique | Electrolyseur horizontal a diaphragme |
-
1984
- 1984-07-13 DE DE19843425862 patent/DE3425862A1/de not_active Withdrawn
-
1985
- 1985-06-27 CA CA000485474A patent/CA1254532A/fr not_active Expired
- 1985-07-04 DE DE8585108265T patent/DE3564703D1/de not_active Expired
- 1985-07-04 EP EP85108265A patent/EP0170092B1/fr not_active Expired
- 1985-07-04 AT AT85108265T patent/ATE36875T1/de active
- 1985-07-08 IN IN516/MAS/85A patent/IN164954B/en unknown
- 1985-07-11 US US06/753,915 patent/US4615783A/en not_active Expired - Fee Related
- 1985-07-11 ES ES1985288013U patent/ES288013Y/es not_active Expired
- 1985-07-11 FI FI852746A patent/FI76837C/fi not_active IP Right Cessation
- 1985-07-12 ZA ZA855260A patent/ZA855260B/xx unknown
- 1985-07-12 NO NO852813A patent/NO163786C/no unknown
- 1985-07-12 AU AU44875/85A patent/AU573356B2/en not_active Ceased
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1380418A (en) * | 1971-01-27 | 1975-01-15 | Electric Power Storage Ltd | Electrolysis of chloride solutions |
EP0077982A1 (fr) * | 1981-10-22 | 1983-05-04 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Procédé électrolytique et cellule électrolytique |
EP0104137A2 (fr) * | 1982-08-26 | 1984-03-28 | Eltech Systems Corporation | Cellule d'électrolyse à électrode gazeuse et faible distance interélectrode |
Also Published As
Publication number | Publication date |
---|---|
FI852746A0 (fi) | 1985-07-11 |
ZA855260B (en) | 1986-03-26 |
DE3425862A1 (de) | 1986-01-23 |
IN164954B (fr) | 1989-07-15 |
US4615783A (en) | 1986-10-07 |
ES288013U (es) | 1985-11-16 |
FI76837B (fi) | 1988-08-31 |
FI852746L (fi) | 1986-01-14 |
AU4487585A (en) | 1986-01-16 |
NO163786B (no) | 1990-04-09 |
NO163786C (no) | 1990-07-18 |
EP0170092B1 (fr) | 1988-08-31 |
ES288013Y (es) | 1986-06-16 |
ATE36875T1 (de) | 1988-09-15 |
AU573356B2 (en) | 1988-06-02 |
NO852813L (no) | 1986-01-14 |
DE3564703D1 (en) | 1988-10-06 |
FI76837C (fi) | 1988-12-12 |
CA1254532A (fr) | 1989-05-23 |
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