EP0097991B1 - Cellule d'électrolyse à membrane avec électrodes disposées verticalement - Google Patents
Cellule d'électrolyse à membrane avec électrodes disposées verticalement Download PDFInfo
- Publication number
- EP0097991B1 EP0097991B1 EP83200883A EP83200883A EP0097991B1 EP 0097991 B1 EP0097991 B1 EP 0097991B1 EP 83200883 A EP83200883 A EP 83200883A EP 83200883 A EP83200883 A EP 83200883A EP 0097991 B1 EP0097991 B1 EP 0097991B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- electrode
- membrane
- units
- electrodes
- spring elements
- 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.)
- Expired
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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
- 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
-
- 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
Definitions
- the invention relates to a membrane electrolysis cell with vertically arranged electrodes for electrochemical processes.
- the surfaces of both electrodes face each other in parallel.
- Flat parallelism of the surfaces is the prerequisite for an efficiently working cell, since this is the only way to ensure an even current distribution and to avoid local overheating.
- the distance between the anode and cathode should also be kept as small as possible. All of these requirements are relatively easy to implement in small laboratory cells, but the construction of large industrial units is difficult if the ideal ideas that are theoretically required are to be realized.
- the larger cells are, the more sensitive they are to deviations from plane parallelism and to current distortion.
- 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 the reduced active surface, the lack of mechanical stability and the loss of high-quality coating material on the back of the electrodes.
- membrane cells with ion exchange membranes are provided with a frame construction that is as rigid as possible, in which the electrodes are rigid, in the majority of cases by welded connections.
- the contact surfaces of the frames must also be machined accordingly.
- the membrane electrolysis cell known from FR-OS 2 486 105 has electrodes divided vertically into several units, and the anode arrangement has flexible spring elements which make the anodes displaceable.
- 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 or surface, there are inevitably different distances between the active surface and the counterelectrode, warps being easily caused, in particular, by local temperature increases in the sensitive partition walls of poor thermal conductivity. Furthermore, the entire active surface of the electrode cannot be brought into the energetically desirable close distance from the counter electrode.
- the object of the invention is therefore to avoid the mentioned and other disadvantages and to provide an electrode arrangement for a membrane electrolysis cell which, under technical operating conditions, ensures a secure plane parallelism of the electrode surfaces and an energetically favorable minimum electrode spacing and ensures safe and rapid gas removal.
- the two geometric reference systems in the cell namely frame / frame and anode / cathode
- the one electrode such as the cathode
- the electrode of the opposite polarity such as the anode vertically divided into several plates or strip units
- This flexible design is brought about by spring elements.
- the spring elements are useful on the Power leads attached to the electrodes and cause electrical contact with the individual strip units of the electrode (anode) via contact pressure or welding.
- the cathode in the above-mentioned arrangement, can also be set up flexibly when the anode is rigidly fixed.
- both electrodes which are divided into individual units, can also be made displaceable by spring elements. In this way, the unevenness of the contact surfaces of the cell frame which is inevitably present and can only be removed with a great deal of work is not transferred to the positioning of the electrode. Rather, the tolerances occurring in the area of the cell frame are bridged by means of the movable connection of the current distributor to the active surface of the electrode.
- the spring force of the spring elements is dimensioned so that it allows the relative spatial position of the anode and cathode to be adjusted.
- the frames can advantageously be made from commercially available, drawn material without substantial post-processing, and the required tight tolerances can be achieved using spacers.
- the movable or displaceable arrangement of the electrode active surfaces for discharging developed and accumulated gas such as chlorine gas
- the spring elements designed as flexible power supply lines form a concave curvature directed towards the cell bottom or an angle opened towards them.
- the spring element can be a leaf spring welded to the power supply.
- the chlorine gas collected under the individual flexible spring elements or current feeders is discharged upwards at one point by gas discharge elements arranged laterally in the electrolysis room. In this way, partial degassing of the electrode space or anode space takes place. This partial degassing in turn causes convection flows in the electrolyte and an improved electrolyte exchange in the active area of the electrodes, which leads to considerable improvements in the energy yield.
- horizontal separation points are created between the individual units of the electrode, on which the membrane does not rest, in which spacers are arranged. Due to the different densities of catholyte and anolyte, the membrane rests on an electrode at the same hydrostatic heights, i. that is, a lateral force acts on the electrode.
- the spacer in the case of gas-developing processes, is designed as a guide element for discharging the developed gas from the electrode space.
- the spacer acts as a gas separation unit when arranged horizontally. It then consists, for example, of strip-shaped plates with serrated edges or strips with slot-shaped or circular openings, or of grid-shaped or network-shaped strips. Such spacers bring about a complete gas withdrawal from the electrode gap after each division of the multiple horizontally divided electrode (cathode).
- FIGS. 1 to 4 of the drawing The invention is illustrated in more detail and by way of example in FIGS. 1 to 4 of the drawing.
- FIG. 1 shows a front view of an electrode frame F with a horizontally divided cathode plate 2.
- FIG. 1b is a similar view of an electrode frame with a vertically and horizontally divided anode 3.
- FIG. 4 shows a displaceable anode 3 in a top view.
- This figure is an enlarged view of section "B" in FIG. 1c and shows spring elements 7 which are connected to the power supply 8 and the anode 3. In the working position, the anode is pressed against the membrane 4.
- the electrolytic cell according to the invention has i.a. following advantages. Due to the movable electrode combination with spring elements caused by multiple divisions, the smallest critical electrode spacing can be maintained at any time during the operation of the electrolytic cell. This combination saves a considerable amount of technical production effort for both the electrodes and for the electrode frames with regard to maintaining tight manufacturing tolerances. Furthermore, a limitation of the height design of the electrolysis cell is practically removed, since developed gas is removed from the electrode gap in each division, i. H. gas accumulation is avoided.
- 1 cm 2 of one of the electrodes is raised by 1 mm. Then there is a current density at the raised point, which can be determined in a first approximation via the power consumption.
- the power consumption would be 1 cm 2 on the area raised by 1 mm
- 1 cm 2 of one of the electrodes is raised by 1 mm.
- the temperature difference between the membrane and the electrolyte increases by about 20%.
- Example 2 shows the limitations in the construction of large-scale electrolytic cells due to power warps. ⁇ 0.75 mm are tolerances that can just be maintained with reasonable effort. For a 1 m wide or tall cell, this tolerance means an accuracy of 0.075% based on the gauge block. Furthermore, 30 to 50% free area for the gas discharge is the maximum of the tolerable, because otherwise the effective current density increases too much.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Engineering & Computer Science (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
- Secondary Cells (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electroluminescent Light Sources (AREA)
- Radiation-Therapy Devices (AREA)
- Luminescent Compositions (AREA)
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT83200883T ATE30252T1 (de) | 1982-06-25 | 1983-06-16 | Membran-elektrolysezelle mit vertikal angeordneten elektroden. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19823223701 DE3223701A1 (de) | 1982-06-25 | 1982-06-25 | Membran-elektrolysezelle mit vertikal angeordneten elektroden |
DE3223701 | 1982-06-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0097991A1 EP0097991A1 (fr) | 1984-01-11 |
EP0097991B1 true EP0097991B1 (fr) | 1987-10-14 |
Family
ID=6166805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP83200883A Expired EP0097991B1 (fr) | 1982-06-25 | 1983-06-16 | Cellule d'électrolyse à membrane avec électrodes disposées verticalement |
Country Status (11)
Country | Link |
---|---|
US (1) | US4502935A (fr) |
EP (1) | EP0097991B1 (fr) |
JP (1) | JPS5913085A (fr) |
AT (1) | ATE30252T1 (fr) |
AU (1) | AU553793B2 (fr) |
BR (1) | BR8303395A (fr) |
CA (1) | CA1214750A (fr) |
DE (2) | DE3223701A1 (fr) |
FI (1) | FI73471C (fr) |
IN (1) | IN156644B (fr) |
ZA (1) | ZA834630B (fr) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE8400459L (sv) * | 1984-01-30 | 1985-07-31 | Kema Nord Ab | Elektrod for elektrolysorer |
DE3726674A1 (de) * | 1987-08-11 | 1989-02-23 | Heraeus Elektroden | Elektrodenstruktur fuer elektrochemische zellen |
DE3808495A1 (de) * | 1988-03-15 | 1989-09-28 | Metallgesellschaft Ag | Membranelektrolysevorrichtung |
US5221452A (en) * | 1990-02-15 | 1993-06-22 | Asahi Glass Company Ltd. | Monopolar ion exchange membrane electrolytic cell assembly |
US5254233A (en) * | 1990-02-15 | 1993-10-19 | Asahi Glass Company Ltd. | Monopolar ion exchange membrane electrolytic cell assembly |
US5100525A (en) * | 1990-07-25 | 1992-03-31 | Eltech Systems Corporation | Spring supported anode |
DE19859882A1 (de) * | 1998-12-23 | 1999-12-09 | W Strewe | Ionenaustauschermembranzelle für hohe Produktleistungen |
EP1397531A1 (fr) * | 2001-06-15 | 2004-03-17 | Akzo Nobel N.V. | Cellule d'electrolyse |
US7141147B2 (en) * | 2001-06-15 | 2006-11-28 | Akzo Nobel N.V. | Electrolytic cell |
US6797136B2 (en) * | 2001-09-07 | 2004-09-28 | Akzo Nobel N.V. | Electrolytic cell |
WO2003023090A1 (fr) * | 2001-09-07 | 2003-03-20 | Akzo Nobel N.V. | Cellule d'electrolyse |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE563393C (de) * | 1929-02-05 | 1932-11-04 | I G Farbenindustrie Akt Ges | Elektrolytische Zelle |
US3674676A (en) * | 1970-02-26 | 1972-07-04 | Diamond Shamrock Corp | Expandable electrodes |
BE793122A (fr) * | 1971-12-22 | 1973-06-21 | Rhone Progil | Electrodes bipolaires demontables |
US3960699A (en) * | 1974-12-23 | 1976-06-01 | Basf Wyandotte Corporation | Self supporting electrodes for chlor-alkali cell |
US4056458A (en) * | 1976-08-26 | 1977-11-01 | Diamond Shamrock Corporation | Monopolar membrane electrolytic cell |
DE2642559B1 (de) * | 1976-09-22 | 1978-02-23 | Heraeus Elektroden | Verfahren zur erneuerung wirksamer elektrodenflaechen von metallelektroden fuer elektrolysezellen |
US4075077A (en) * | 1977-05-16 | 1978-02-21 | Pennwalt Corporation | Electrolytic cell |
IT1114623B (it) * | 1977-07-01 | 1986-01-27 | Oronzio De Nora Impianti | Cella elettrolitica monopolare a diaframma |
US4154667A (en) * | 1978-01-03 | 1979-05-15 | Diamond Shamrock Corporation | Method of converting box anodes to expandable anodes |
JPS5629683A (en) * | 1979-08-17 | 1981-03-25 | Toagosei Chem Ind Co Ltd | Anode structure for diaphragmatic electrolysis cell |
IT1163737B (it) * | 1979-11-29 | 1987-04-08 | Oronzio De Nora Impianti | Elettrolizzatore bipolare comprendente mezzi per generare la ricircolazione interna dell'elettrolita e procedimento di elettrolisi |
US4443315A (en) * | 1980-07-03 | 1984-04-17 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Finger type electrolytic cell for the electrolysis of an aqueous alkali metal chloride solution |
-
1982
- 1982-06-25 DE DE19823223701 patent/DE3223701A1/de not_active Withdrawn
- 1982-09-22 IN IN1097/CAL/82A patent/IN156644B/en unknown
-
1983
- 1983-06-16 EP EP83200883A patent/EP0097991B1/fr not_active Expired
- 1983-06-16 DE DE8383200883T patent/DE3374072D1/de not_active Expired
- 1983-06-16 AT AT83200883T patent/ATE30252T1/de not_active IP Right Cessation
- 1983-06-23 FI FI832313A patent/FI73471C/fi not_active IP Right Cessation
- 1983-06-23 CA CA000431098A patent/CA1214750A/fr not_active Expired
- 1983-06-24 ZA ZA834630A patent/ZA834630B/xx unknown
- 1983-06-24 AU AU16260/83A patent/AU553793B2/en not_active Ceased
- 1983-06-24 US US06/507,840 patent/US4502935A/en not_active Expired - Fee Related
- 1983-06-24 BR BR8303395A patent/BR8303395A/pt not_active IP Right Cessation
- 1983-06-25 JP JP58114997A patent/JPS5913085A/ja active Pending
Also Published As
Publication number | Publication date |
---|---|
FI73471B (fi) | 1987-06-30 |
FI832313A0 (fi) | 1983-06-23 |
ATE30252T1 (de) | 1987-10-15 |
DE3374072D1 (en) | 1987-11-19 |
AU1626083A (en) | 1984-01-05 |
BR8303395A (pt) | 1984-02-07 |
IN156644B (fr) | 1985-09-28 |
JPS5913085A (ja) | 1984-01-23 |
EP0097991A1 (fr) | 1984-01-11 |
US4502935A (en) | 1985-03-05 |
CA1214750A (fr) | 1986-12-02 |
DE3223701A1 (de) | 1983-12-29 |
FI73471C (fi) | 1987-10-09 |
ZA834630B (en) | 1985-02-27 |
AU553793B2 (en) | 1986-07-24 |
FI832313L (fi) | 1983-12-26 |
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