EP0252172B1 - Elektrolyseverfahren - Google Patents
Elektrolyseverfahren Download PDFInfo
- Publication number
- EP0252172B1 EP0252172B1 EP86109265A EP86109265A EP0252172B1 EP 0252172 B1 EP0252172 B1 EP 0252172B1 EP 86109265 A EP86109265 A EP 86109265A EP 86109265 A EP86109265 A EP 86109265A EP 0252172 B1 EP0252172 B1 EP 0252172B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cell
- process according
- electrolyte
- material transport
- transport coefficient
- 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
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
Definitions
- the invention relates to an electrolysis process, wherein an electrolyte is passed through an electrolysis cell and the mass transfer coefficient is increased by introducing mechanical energy.
- electrochemical cells For electrochemical reactions, e.g. To achieve in aqueous solutions, the most varied versions of electrochemical cells are used, e.g. Cells with a fixed bed made of graphite granules, metal wool or metal foam, or stacks of expanded metals. Plate cells are generally used at higher concentrations. It is also known that the mode of action of a cell, especially a plate cell, can be improved by increasing the stream transport coefficient. This is e.g. in that the medium to be treated is circulated at high speed through the cell and the batched liquid is then carried on in batches or a small volume flow is metered into the system in front of the cell and a corresponding small volume flow is branched off after the cell.
- the mass transfer coefficient is increased by the introduction of mechanical energy, but in the prior art the entire electrolytic cell has been exposed to mechanical vibrations or other means for increasing the mass transfer coefficient, without making a differentiation according to the electrolyte flow in the electrolysis cell .
- the change in the electrode overvoltages can be very disruptive because this leads to an area at the cell outlet in which undesired side reactions take place at the electrode. In most cases this is on the cathode e.g. the production of hydrogen.
- the invention is therefore based on the object of proposing an electrolysis process of the type mentioned at the outset, in which the current density at the cell outlet is appreciably increased, without the occurrence of undesirable side reactions.
- the invention is characterized in that the increase in the mass transfer coefficient increases along the direction of the electrolyte flow.
- the idea on which the invention is based is therefore to increase the current density at the cell outlet by increasing the mass transfer coefficient there compared to the cell outlet, for example by exposing the electrolyte to pressure waves whose intensity at the cell outlet is stronger than at the cell inlet. It is obvious that in one liquid-filled, open-topped container, the housing of which is caused to vibrate, for example by blows, the amplitude of the vibration is greater in the upper region than in the lower region, in which the side plates are held together by a base. For example, if an electrochemical cell consists of a rectangular box in which the electrodes are suspended as plates, and if this box is vibrated from the outside by vibrators, the amplitude of the vibration in the upper area of the box is greater than in the lower area. If one now places the cell inlet downwards in the box and the cell outlet upwards, the stream transport coefficient along the direction of the electrolyte flow can be influenced in this way, and this essentially increases. The gas bubbles at the cell outlet can then be reduced or avoided.
- FIG. 1 shows a vessel 1 of an electrolysis cell, in which an electrolyte 2 is located.
- An anode 3, which is surrounded by a diaphragm 4, and several cathodes 5 are immersed in the electrolyte.
- the electrolyte is continuously introduced into the vessel 1 via a side inlet 8 in the direction of arrow 9. It leaves the vessel via an overflow at the upper edge of the vessel or via holes or the like provided there.
- a distributor tube not shown and laid over the bottom of the vessel, ensures a uniform distribution of the electrolyte, the direction of flow of which is indicated in the cell by arrows 10 .
- Fig. 1 also shows that the vibrator 6 Schwin conditions in the direction of arrow 7, which are essentially perpendicular to the plane of the plates 3, 5.
- FIG. 2 shows a diagram as a further explanation, the direction of the electrolyte flow 10 being indicated as the abscissa x.
- the ordinates y are the amplitudes of the mechanical vibrations with which the electrolysis cell is subjected. It also follows from this that a smaller amplitude acts on the electrolyte at the inlet 16 of the electrolytic cell than at the outlet 17. This is shown by the curve 18.
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)
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT86109265T ATE40720T1 (de) | 1986-07-07 | 1986-07-07 | Elektrolyseverfahren. |
DE8686109265T DE3662060D1 (en) | 1986-07-07 | 1986-07-07 | Electrolysis process |
EP86109265A EP0252172B1 (de) | 1986-07-07 | 1986-07-07 | Elektrolyseverfahren |
DE8619501U DE8619501U1 (de) | 1986-07-07 | 1986-07-19 | Elektrolysezelle |
JP62021910A JPS6314884A (ja) | 1986-07-07 | 1987-02-03 | 電気分解法 |
US07/020,357 US4806224A (en) | 1986-07-07 | 1987-03-02 | Electrolytic process |
PT85218A PT85218B (pt) | 1986-07-07 | 1987-06-30 | Processo de electrolise |
ES8701977A ES2007633A6 (es) | 1986-07-07 | 1987-07-06 | Procedimiento de electrolisis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP86109265A EP0252172B1 (de) | 1986-07-07 | 1986-07-07 | Elektrolyseverfahren |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0252172A1 EP0252172A1 (de) | 1988-01-13 |
EP0252172B1 true EP0252172B1 (de) | 1989-02-08 |
Family
ID=8195250
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP86109265A Expired EP0252172B1 (de) | 1986-07-07 | 1986-07-07 | Elektrolyseverfahren |
Country Status (7)
Country | Link |
---|---|
US (1) | US4806224A (es) |
EP (1) | EP0252172B1 (es) |
JP (1) | JPS6314884A (es) |
AT (1) | ATE40720T1 (es) |
DE (2) | DE3662060D1 (es) |
ES (1) | ES2007633A6 (es) |
PT (1) | PT85218B (es) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2681079B1 (fr) * | 1991-09-06 | 1994-09-09 | Kodak Pathe | Dispositif et procede d'electrolyse a electrode poreuse et agitee. |
US5312532A (en) * | 1993-01-15 | 1994-05-17 | International Business Machines Corporation | Multi-compartment eletroplating system |
US5310486A (en) * | 1993-05-25 | 1994-05-10 | Harrison Western Environmental Services, Inc. | Multi-stage water treatment system and method for operating the same |
US5419823A (en) * | 1993-11-09 | 1995-05-30 | Hardwood Line Manufacturing Co. | Electroplating device and process |
US6454918B1 (en) * | 1999-03-23 | 2002-09-24 | Electroplating Engineers Of Japan Limited | Cup type plating apparatus |
AU2002332243A1 (en) * | 2001-12-03 | 2003-06-17 | Japan Techno Co., Ltd. | Hydrogen-oxygen gas generator and hydrogen-oxygen gas generating method using the generator |
WO2006116533A2 (en) * | 2005-04-27 | 2006-11-02 | Hw Process Technologies, Inc. | Treating produced waters |
JP4732833B2 (ja) * | 2005-08-22 | 2011-07-27 | 樫山工業株式会社 | スクリューロータおよび真空ポンプ |
US7365258B1 (en) | 2006-08-02 | 2008-04-29 | Drum Workshop, Inc. | Sound box with external and internal impact surfaces |
WO2008036816A2 (en) * | 2006-09-20 | 2008-03-27 | Hw Advanced Technologies, Inc. | Multivalent iron ion separation in metal recovery circuits |
US20080128354A1 (en) * | 2006-11-30 | 2008-06-05 | Hw Advanced Technologies, Inc. | Method for washing filtration membranes |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2744860A (en) * | 1951-11-13 | 1956-05-08 | Robert H Rines | Electroplating method |
US3351539A (en) * | 1965-04-06 | 1967-11-07 | Branson Instr | Sonic agitating method and apparatus |
DE1263768B (de) * | 1965-07-09 | 1968-03-21 | Basf Ag | Vorrichtung zur Durchfuehrung elektrochemischer Reaktionen organischer Verbindungen mit stroemendem Elektrolyten |
US3699014A (en) * | 1970-12-29 | 1972-10-17 | Norton Co | Vibratory process |
BG22251A1 (en) * | 1974-10-04 | 1979-12-12 | Petrov | Method and installation for non-ferros elektrolysis |
US4049512A (en) * | 1975-10-31 | 1977-09-20 | Tolle Jr Albert E | Cathode structure for electrolytic apparatus employing impellers |
US4125447A (en) * | 1978-03-24 | 1978-11-14 | Bachert Karl R | Means for plating the inner surface of tubes |
GB2078782A (en) * | 1980-06-20 | 1982-01-13 | Pullen Peter | Agitating Photographic Fix Solutions in Electrolytic Recovery of Silver Therefrom |
EP0171647A1 (de) * | 1984-07-25 | 1986-02-19 | Deutsche Carbone AG | Verfahren zum elektrolytischen Abscheiden von Metallen aus einem Elektrolysebad |
US4619749A (en) * | 1985-03-25 | 1986-10-28 | Nusbaum Ronald C | System for extracting silver from liquid solutions |
US4675254A (en) * | 1986-02-14 | 1987-06-23 | Gould Inc. | Electrochemical cell and method |
-
1986
- 1986-07-07 DE DE8686109265T patent/DE3662060D1/de not_active Expired
- 1986-07-07 EP EP86109265A patent/EP0252172B1/de not_active Expired
- 1986-07-07 AT AT86109265T patent/ATE40720T1/de not_active IP Right Cessation
- 1986-07-19 DE DE8619501U patent/DE8619501U1/de not_active Expired
-
1987
- 1987-02-03 JP JP62021910A patent/JPS6314884A/ja active Pending
- 1987-03-02 US US07/020,357 patent/US4806224A/en not_active Expired - Fee Related
- 1987-06-30 PT PT85218A patent/PT85218B/pt not_active IP Right Cessation
- 1987-07-06 ES ES8701977A patent/ES2007633A6/es not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE8619501U1 (de) | 1986-11-06 |
US4806224A (en) | 1989-02-21 |
PT85218B (pt) | 1993-07-30 |
ES2007633A6 (es) | 1989-07-01 |
DE3662060D1 (en) | 1989-03-16 |
JPS6314884A (ja) | 1988-01-22 |
PT85218A (pt) | 1988-07-29 |
EP0252172A1 (de) | 1988-01-13 |
ATE40720T1 (de) | 1989-02-15 |
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