EP0102099A1 - Plaque d'électrode verticale pour électrolyseurs à dégagement gazeux - Google Patents
Plaque d'électrode verticale pour électrolyseurs à dégagement gazeux Download PDFInfo
- Publication number
- EP0102099A1 EP0102099A1 EP83201053A EP83201053A EP0102099A1 EP 0102099 A1 EP0102099 A1 EP 0102099A1 EP 83201053 A EP83201053 A EP 83201053A EP 83201053 A EP83201053 A EP 83201053A EP 0102099 A1 EP0102099 A1 EP 0102099A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- electrode
- membrane
- distance
- counter electrode
- degassing
- 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
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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
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
- C25B11/03—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
Definitions
- the invention relates to a vertically arranged plate electrode for gas-forming electrolyzers with horizontally divided electrode plates, the upper edges of which are designed as gas discharge elements and face away from the counterelectrode.
- electrodes with openings for the removal of the reaction gases are generally used, for example perforated electrodes, wire mesh, or expanded metal.
- the disadvantages include reduced active surface, lack of stability and loss of high quality coating material on the back of the electrode.
- an electrode plate consisting of individual plates has already been provided for vertically arranged electrodes in gas-forming diaphragm cells, the individual plates having guide surfaces for the discharge of the gas generated. Due to the intended inclination of the guide plate, there are inevitably different distances between the active surface and the counter electrode.
- the electrodes In the known from FR-PS 1028153 E lektrolyseur are arranged, the electrodes with the least possible distance in parallel.
- the previously known electrodes are formed from one or more plates. The plates have horizontal openings, which are caused by bending the plate strips and offer the least resistance to the gas outlet. The bends face away from the counter electrode, there is no noticeable reduction in the active surface.
- a similar type of arrangement of electrodes is also known from DE-PS 453750. In the previously known electrodes, cuts are made, by means of which sections of any shape are bent out, in such a way that they are directed towards the side facing away from the electrode.
- electrodes or cathodes of this type have been known for more than 30 years, they have still not found their way into technical practice. Rather, perforated sheets, expanded metal or similar materials are still used.
- the invention has for its object to provide an electrode which ensures safe and rapid gas removal from the electrolyte with the smallest distance ratio.
- the invention solves this problem with a vertically arranged plate electrode for gas-forming electrolysers, in particular membrane electrolysers, with horizontally divided electrode plates, the entire active electrode surface of which is arranged parallel and at the shortest distance from the counterelectrode and whose respective upper edges are designed as a 'gas discharge element and turned away from the counterelectrode are.
- the invention consists in the fact that the ratio of the distance G between the counter electrode / membrane and the degassing apex S the lower edge of the electrode plate, to the distance E, between the counter electrode / membrane and the tear-off edge K of the angled gas discharge element, corresponds to a value F (degassing capacity) of less than 0.6.
- the angled part of the individual plates of the electrode according to the invention is generally designed as a flat surface, but can also be curved.
- the angle from the electrode plane is generally between 15 and 70 °.
- the individual electrode plate has a height of 5 to 50 cm and a thickness of about 1 to 3 mm in the vertical part. The thickness of the individual electrode plate depends on the width of the electrode, since no additional current distribution bolts are provided, which, for. B. with cells of conventional dimensions and when using expanded metal as an active surface are necessary.
- the electrode plates are firmly installed in a manner known per se in a frame which has connection elements for the supply of the electric current.
- the electrode according to the invention can be used as an anode or cathode in membrane electrolysis processes.
- titanium, tantalum, tungsten or zirconium is selected as the electrode material.
- the electrode is only provided with an activating coating on its surface facing the counterelectrode, in known manner from z.
- the electrode according to the invention can be made of e.g. B. steel or nickel or their alloys.
- the electrode plate according to the invention is used in electrolysers with membranes.
- membrane cells are only to be understood as those cells which have ion-selective membranes, such as perfluorinated cation exchange membranes.
- ion-selective membranes such as perfluorinated cation exchange membranes.
- Such membranes allow the separation of cathodic and anodic products of an electrolysis from one another or from the reactants supplied to the counterelectrode.
- FIGS. 1 and 2 of the drawing The electrode arrangement according to the invention is illustrated and illustrated by way of example in FIGS. 1 and 2 of the drawing.
- FIG. 1 a side view of an electrode divided into individual plate strips with angled gas discharge elements is shown horizontally (electrode frame and current supply elements are not shown).
- FIG. 2 shows the detail indicated by "A” in FIG.
- M denotes the membrane
- S the degassing vertex on the lower edge of the plate strip
- K the tear-off edge on the angled upper part of the plate strip arranged underneath.
- G is the distance M - S and E is the distance M - K.
- the degassing vertex lies in the plane of the active surface. If the electrode surfaces are not beveled, the degassing vertex is assumed to lie on the center line of the electrode.
- the term degassing ability is based further on the finding that the gas rising from the electrode gap expands to the tear-off edge K, then rises vertically upwards and divides at the apex of the degassing into a part which re-enters the electrode gap and a predominant other part which, according to the invention, steps behind the electrodes.
- a sodium chloride solution with a concentration of 320 g / l was electrolyzed in a technical chlor-alkali electrolysis plant with an ion-selective membrane to produce sodium hydroxide solution, chlorine and hydrogen.
- the current density was 3.1 KA / m 2 and the temperature of the electrolyte was 80 ° C.
- Electrodes according to the invention with heights of the individual plate strips of 14 cm and active areas of approximately 90% of the projected areas were used as cathodes.
- Steel ST 37 was used as the material without activation.
- a comparison was made with conventional expanded metal cathodes of the same material and the same projected active area.
- Dimensionally stable anodes were used as counter electrodes and a perfluorinated ion exchange membrane (trade name Nafion) was used as the selective membrane.
- the plate thickness was 6.5 mm with a strip width of the individual plate of 100 cm.
- the guide element was bent at an angle of 30 °.
- the gap width between the individual plate strips of the cathode was 20 mm and the distance between the cathode and membrane surface was 3 mm.
- the total electrode area was 1 x 1 m 2 .
- the advantages of the electrode plate of the invention can be seen in the fact that the electrode plate can be arranged at the smallest possible distance with a completely active surface parallel to the counter electrode and punctual overheating of the temperature-sensitive membranes can be avoided, the gas formed between the anode and cathode quickly from the area of the active Surface behind the electrode surface is derived. Furthermore, the electrodes can be produced in a simple manner from flat sheet metal without great technical outlay, and the one-sided application of an active surface layer is also possible without difficulty.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Catalysts (AREA)
- Inert Electrodes (AREA)
- Treating Waste Gases (AREA)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT83201053T ATE30343T1 (de) | 1982-08-03 | 1983-07-16 | Vertikal angeordnete plattenelektrode fuer gasbildende elektrolyseure. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19823228884 DE3228884A1 (de) | 1982-08-03 | 1982-08-03 | Vertikal angeordnete plattenelektrode fuer gasbildende elektrolyseure |
| DE3228884 | 1982-08-03 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0102099A1 true EP0102099A1 (fr) | 1984-03-07 |
| EP0102099B1 EP0102099B1 (fr) | 1987-10-21 |
Family
ID=6169972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP83201053A Expired EP0102099B1 (fr) | 1982-08-03 | 1983-07-16 | Plaque d'électrode verticale pour électrolyseurs à dégagement gazeux |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US4474612A (fr) |
| EP (1) | EP0102099B1 (fr) |
| JP (1) | JPH062959B2 (fr) |
| AT (1) | ATE30343T1 (fr) |
| BR (1) | BR8304151A (fr) |
| CA (1) | CA1228571A (fr) |
| DE (2) | DE3228884A1 (fr) |
| ES (1) | ES284413Y (fr) |
| IN (1) | IN157978B (fr) |
| MX (1) | MX153006A (fr) |
| ZA (1) | ZA835568B (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0776996A1 (fr) | 1995-11-22 | 1997-06-04 | De Nora S.P.A. | Electrode pour électrolyseurs à membrane |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3640584A1 (de) * | 1986-11-27 | 1988-06-09 | Metallgesellschaft Ag | Elektrodenanordnung fuer gasbildende elektrolyseure mit vertikal angeordneten plattenelektroden |
| DE3808495A1 (de) * | 1988-03-15 | 1989-09-28 | Metallgesellschaft Ag | Membranelektrolysevorrichtung |
| DE4224492C1 (de) * | 1992-07-24 | 1993-12-09 | Uhde Gmbh | Vorrichtung zum elektrolytischen Behandeln von Flüssigkeiten mit einer Anoden- und einer Kathodenkammer sowie deren Verwendung |
| DE4306889C1 (de) * | 1993-03-05 | 1994-08-18 | Heraeus Elektrochemie | Elektrodenanordnung für gasbildende elektrolytische Prozesse in Membran-Zellen und deren Verwendung |
| DE4438124A1 (de) * | 1994-10-27 | 1996-05-02 | Eilenburger Elektrolyse & Umwelttechnik Gmbh | Gas-Lift-Elektrolyse- und Reaktionssysteme zur Herstellung von Produkten und zur Anwendung in der Umwelttechnik |
| DE19816334A1 (de) * | 1998-04-11 | 1999-10-14 | Krupp Uhde Gmbh | Elektrolyseapparat zur Herstellung von Halogengasen |
| CA2349508C (fr) | 2001-06-04 | 2004-06-29 | Global Tech Environmental Products Inc. | Cellule d'electrolyse et dispositif pour moteur a combustion interne comprenant ladite cellule |
| CA2597068A1 (fr) * | 2007-06-19 | 2008-12-19 | Peter Romaniuk | Hydrox produit par electrolyse comme source partielle hybride de carburant pour moteurs a combustion interne classiques |
| US8808512B2 (en) | 2013-01-22 | 2014-08-19 | GTA, Inc. | Electrolyzer apparatus and method of making it |
| US9222178B2 (en) | 2013-01-22 | 2015-12-29 | GTA, Inc. | Electrolyzer |
| CN107473336A (zh) * | 2017-09-20 | 2017-12-15 | 合肥齐兴电器有限责任公司 | 一种便携式电解水器 |
| DE102023122813A1 (de) * | 2023-08-24 | 2025-02-27 | Ks Gleitlager Gmbh | Substrat für den Einsatz als Elektrode in einer Elektrolysezelle |
| FR3152519B1 (fr) * | 2023-09-01 | 2025-09-19 | Univ Rennes | cellule élémentaire pour l’électrolyse d’une solution électrolytique produisant des gaz |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR811238A (fr) * | 1936-09-24 | 1937-04-09 | Perfectionnements apportés aux électrolyseurs | |
| FR1028153A (fr) * | 1949-11-03 | 1953-05-20 | Montedison Spa | électrode pour électrolyseurs bipolaires |
| FR2070757A1 (fr) * | 1969-12-06 | 1971-09-17 | Nippon Soda Co |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE453750C (de) * | 1927-12-14 | I G Farbenindustrie Akt Ges | Elektrolysierzelle | |
| US1771091A (en) * | 1924-09-01 | 1930-07-22 | Firm Lawaczeck Gmbh | Electrolytic cell |
| GB1595183A (en) * | 1977-03-04 | 1981-08-12 | Ici Ltd | Diaphragm cell |
| US4142950A (en) * | 1977-11-10 | 1979-03-06 | Basf Wyandotte Corporation | Apparatus and process for electrolysis using a cation-permselective membrane and turbulence inducing means |
| JPS57164990A (en) * | 1981-04-03 | 1982-10-09 | Toyo Soda Mfg Co Ltd | Electrolyzing method for aqueous alkali chloride solution |
-
1982
- 1982-08-03 DE DE19823228884 patent/DE3228884A1/de not_active Withdrawn
-
1983
- 1983-07-16 DE DE8383201053T patent/DE3374139D1/de not_active Expired
- 1983-07-16 AT AT83201053T patent/ATE30343T1/de not_active IP Right Cessation
- 1983-07-16 EP EP83201053A patent/EP0102099B1/fr not_active Expired
- 1983-07-22 IN IN921/CAL/83A patent/IN157978B/en unknown
- 1983-07-28 ES ES1983284413U patent/ES284413Y/es not_active Expired
- 1983-07-29 ZA ZA835568A patent/ZA835568B/xx unknown
- 1983-08-01 MX MX198252A patent/MX153006A/es unknown
- 1983-08-02 BR BR8304151A patent/BR8304151A/pt not_active IP Right Cessation
- 1983-08-02 CA CA000433683A patent/CA1228571A/fr not_active Expired
- 1983-08-03 US US06/520,068 patent/US4474612A/en not_active Expired - Fee Related
- 1983-08-03 JP JP58142386A patent/JPH062959B2/ja not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR811238A (fr) * | 1936-09-24 | 1937-04-09 | Perfectionnements apportés aux électrolyseurs | |
| FR1028153A (fr) * | 1949-11-03 | 1953-05-20 | Montedison Spa | électrode pour électrolyseurs bipolaires |
| FR2070757A1 (fr) * | 1969-12-06 | 1971-09-17 | Nippon Soda Co |
Non-Patent Citations (1)
| Title |
|---|
| PATENTS ABSTRACTS OF JAPAN, Band 7, Nr. 7 (C-144)[1152], 12. Januar 1983 & JP - A - 57 164 990 (TOYO SODA KOGYO K.K.) 09-10-1982 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0776996A1 (fr) | 1995-11-22 | 1997-06-04 | De Nora S.P.A. | Electrode pour électrolyseurs à membrane |
Also Published As
| Publication number | Publication date |
|---|---|
| CA1228571A (fr) | 1987-10-27 |
| BR8304151A (pt) | 1984-03-13 |
| JPH062959B2 (ja) | 1994-01-12 |
| JPS5943885A (ja) | 1984-03-12 |
| US4474612B1 (fr) | 1989-01-03 |
| MX153006A (es) | 1986-07-16 |
| ZA835568B (en) | 1985-03-27 |
| ES284413U (es) | 1985-06-01 |
| EP0102099B1 (fr) | 1987-10-21 |
| IN157978B (fr) | 1986-08-09 |
| ATE30343T1 (de) | 1987-11-15 |
| ES284413Y (es) | 1986-01-16 |
| US4474612A (en) | 1984-10-02 |
| DE3228884A1 (de) | 1984-02-09 |
| DE3374139D1 (en) | 1987-11-26 |
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