EP1977027A2 - Elastic current distributor for percolating cells - Google Patents
Elastic current distributor for percolating cellsInfo
- Publication number
- EP1977027A2 EP1977027A2 EP07703878A EP07703878A EP1977027A2 EP 1977027 A2 EP1977027 A2 EP 1977027A2 EP 07703878 A EP07703878 A EP 07703878A EP 07703878 A EP07703878 A EP 07703878A EP 1977027 A2 EP1977027 A2 EP 1977027A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- cell
- gas
- diffusion electrode
- conductive protrusions
- metal sheet
- 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.)
- Withdrawn
Links
- 238000009792 diffusion process Methods 0.000 claims abstract description 31
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 7
- 239000003792 electrolyte Substances 0.000 claims abstract description 7
- 239000012528 membrane Substances 0.000 claims abstract description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 28
- 229910052751 metal Inorganic materials 0.000 claims description 15
- 239000002184 metal Substances 0.000 claims description 14
- 229910052759 nickel Inorganic materials 0.000 claims description 14
- 239000003014 ion exchange membrane Substances 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 230000006835 compression Effects 0.000 claims description 4
- 238000007906 compression Methods 0.000 claims description 4
- 238000007493 shaping process Methods 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 abstract description 4
- 239000003513 alkali Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 230000008569 process Effects 0.000 description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 238000005325 percolation Methods 0.000 description 4
- 239000010936 titanium Substances 0.000 description 4
- 229910052719 titanium Inorganic materials 0.000 description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000012267 brine Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052709 silver Inorganic materials 0.000 description 3
- 239000004332 silver Substances 0.000 description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000010349 cathodic reaction Methods 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000003491 array Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011244 liquid electrolyte Substances 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000009420 retrofitting Methods 0.000 description 1
- 229910001925 ruthenium oxide Inorganic materials 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 230000003019 stabilising effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
-
- 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
- C25B9/60—Constructional parts of cells
- C25B9/65—Means for supplying current; Electrode connections; Electric inter-cell connections
-
- 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
-
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0232—Metals or alloys
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the invention relates to a cell for industrial electrolytic processes, and in particular to a cell comprising an anodic compartment and a cathodic compartment separated by an ion-exchange membrane, wherein one or both compartments are equipped with gas- diffusion electrodes and the process electrolyte flows across a percolator or equivalent porous element.
- depolarised chlor-alkali electrolysis that is to the process of alkali chloride brine electrolysis wherein the hydrogen evolution cathodic reaction is inhibited in favour of the reaction of oxygen consumption on a gas-diffusion cathode, for instance as disclosed in EP 1033419; the invention is nevertheless not limited to chlor-alkali cells, being applicable to any industrial electrochemical process making use of gas-diffusion electrodes.
- depolarised chlor-alkali cells of particularly advanced type wherein the process electrolyte flows across a suitable porous planar element or percolator under the action of gravity: a cell of such kind is for instance disclosed in WO/0157290.
- anodic compartment obtained from a titanium shell, fed with an alkali chloride concentrated brine and containing a titanium anode provided with a catalytic coating for chlorine evolution, and a cathodic compartment delimited by a nickel cathodic shell; the two compartments are separated by a cation-exchange membrane.
- the caustic soda produced in the process flows by gravity across a porous element inserted in the cathodic compartment contacting on one side the ion-exchange membrane, on the other side a gas-diffusion cathode.
- the cathode is a thin porous element obtained from a silver net, a carbon cloth or other type of non self- standing equivalent structure. For this reason, the current transmission from the back- wall of the cathodic shell to the gas-diffusion electrode must be effected by means of a structure providing a more delocalised contact and capable of mechanically supporting the electrode.
- the cathode In order to improve the electrochemical features, it is also necessary that the cathode be pushed against the percolator with a certain pressure, indicatively 0.1 to 0.5 kg/cm 2 , so as to allow the electrical continuity while contributing to the confinement of the circulating liquid electrolyte.
- a certain pressure indicatively 0.1 to 0.5 kg/cm 2
- the cells of the prior art are provided with an electric current feed system relying on two distinct elements: firstly, a rigid current collector integral to the cathodic shell which may for instance consist of a rib array, as in the anodic side; secondly, a metal mattress positioned between the rigid current collector and the gas-diffusion electrode, which is capable, in conditions of suitable compression, to transmit a sufficient pressure to the gas-diffusion electrode thereby ensuring the required electrical continuity.
- the two-component type current transmission system involves in fact excessive costs and thicknesses, difficulties of installation and of dimensional control of the mattress (especially in the peripheral zone), difficulty of controlling the deformations and the elastic forces, besides of course adding a contact interface not particularly favourable in terms of ohmic drop, such as the one between mattress and gas-diffusion electrode.
- the invention consists of an electrolysis cell with an anodic compartment and a cathodic compartment separated by an ion-exchange membrane, wherein at least one of the two compartments is equipped with a gas-diffusion electrode having two major surfaces, a first major surface facing the membrane being in contact with a percolator traversed by an electrolyte flow, and a second major surface, opposed to the first major surface, being in contact with a current distributor comprising a multiplicity of elastic conductive protrusions suitable for compressing the gas-diffusion electrode against the percolator.
- percolator it is intended any porous planar element suitable for being traversed by gravity by a liquid flow, as disclosed in WO/0157290.
- the current distributor which replaces the rigid current collector-elastic current collector assembly of the prior art, is obtained by cutting and shaping of a single metal sheet, for instance a nickel sheet in the case of a cathodic collector for chlor-alkali cells.
- the nickel sheet is a sheet of thickness typically comprised between 0.5 and 1.5 mm, preferably provided with a coating suitable for reducing the contact resistance.
- the nickel material of the sheet may be variously alloyed and for instance selected from the assortment of commonly available products; the choice of a nickel material of grade and mechanical characteristics suitable for the manufacturing of springs, for instance with superior elastic features, will prove particularly advantageous.
- the conductive protrusions capable of imparting a sufficient pressure to the electrode are spring tags arranged in couples so that two adjacent spring tags protrude in opposite direction from the major plane of the metal sheet from which they are obtained. In this way a more effective and homogeneous support of the whole electrode surface is obtained.
- the above indicated solution is suited to an optimum cell design in almost every process condition; nevertheless, the use of the mattress according to the prior art as a contact element at high current density has the advantage of allowing an effective gas circulation (for the case of depolarised chlor- alkali electrolysis for example, an effective supply of oxygen to the gas-diffusion electrode) which could fall short with a simple lamellar structure.
- a particularly preferred embodiment provides the conductive protrusions to be in form of individual tiles, in their turn comprising one or more spring tags for providing the electrical contact but also one or more openings to favour the gas passage.
- the conductive protrusions may for instance be disposed in parallel rows distributed along the whole electrode surface.
- the current distributor in accordance with the invention is suitable for achieving an efficient electrical contact directly on the gas-diffusion electrode surface, at a pressure preferably comprised between 0.1 and 0.5 kg/cm 2 , thereby getting rid of a contact interface with respect to the system of the prior art in which a rigid current collector is coupled to an elastic current collector; on the other hand, in one embodiment of the invention an additional element for distributing the mechanical compression force may be inserted between current distributor and gas-diffusion electrode, for example consisting of a thin mesh, or of an expanded or punched sheet. In such case the number of contact interfaces is equivalent to that of the prior art, nevertheless the corresponding resistance is substantially lower than what would be obtained with the scarcely elastic mattress of the prior art directly in contact with a gas-diffusion electrode. Moreover, as it will be easily appreciated by one skilled in the art, the overall thickness of the cell is substantially lower.
- Figure 1 represents a percolation type depolarised chlor-alkali cell according to the prior art.
- FIG. 2 represents a percolation type depolarised chlor-alkali cell according to the present invention.
- FIG. 3 represents a first embodiment of the current distributor according to the invention.
- Figure 4 represents a second embodiment of the current distributor according to the invention.
- Figure 5 represents a third embodiment of the current distributor according to the invention.
- FIG 1 it is shown a percolation type depolarised chlor-alkali cell according to the prior art, comprising one anodic and one cathodic compartment separated by an ion- exchange membrane (500).
- the cathodic compartment is delimited by a cathodic back- wall (101 ), in contact with an electric current feed system relying on two distinct elements, a rigid current collector (201 ) integral thereto, and an elastic current collector (210) consisting of a mattress, for instance made of nickel.
- the cathode (301 ) consists of a porous gas-diffusion electrode fed with oxygen, contacting on one side the mattress (210), on the other side a percolator (400) consisting of a planar porous element traversed by the electrolyte flow under the action of gravity.
- the ion-exchange membrane (500) acting as the separator has a cathodic surface in contact with the percolator (400) and an anodic surface facing an anode (302) which may be in contact therewith or kept at a small predetermined distance.
- the anode (302) is normally comprised of a titanium substrate consisting of a mesh or of an expanded or punched sheet, or optionally of a juxtaposition of two such elements; the anodic substrate is provided with a catalytic coating for chlorine evolution as known in the art.
- the electrical continuity between anode (302) and anodic compartment back-wall (102) is ensured by a rigid current collector (202).
- the cathodic (201 ) and anodic (202) rigid current collectors may consist of rib arrays, undulated sheets, sheets provided with suitably spaced gophers or other types of current collectors as known by those skilled in the art.
- figure 2 it is shown a percolation type depolarised chlor-alkali according to the present invention, wherein the elements in common with the cell of figure 1 are indicated by the same reference numerals.
- the electric current feed system consists of a multiplicity of conductive protrusions (220), for instance an assembly of springs or elastic spring tags suitable for compressing the gas-diffusion electrode (301) against the percolator (400); between the assembly of conductive protrusions (220) and the gas-diffusion electrode (301 ) an optional element for distributing the mechanical compression force (230) is inserted, for instance a thin mesh, or an expanded or punched sheet.
- Figure 3 shows one embodiment of the multiplicity of conductive protrusions obtained from a single metal sheet and consisting in this case of an assembly of elastic spring tags (221 ) disposed in parallel according to a comb-like geometry: the spring tags are arranged in couples, so that each two spring tags protrude in opposite directions from the major plane of the original metal sheet.
- a single row of spring tags (221 ) may cover the whole active surface, or more rows may be arranged side by side, as will be evident to one skilled in the art.
- Figure 4 shows a preferred embodiment of the multiplicity of conductive protrusions obtained from a single metal sheet: in this case the protrusions are preferably quadrangular individual tiles (222) obtained by cutting and shaping of a sheet, optionally welded directly to the rigid current collector (201 ), each of them comprising elements performing different functions: for example, by means of a suitable folding step, each tile is provided with edges with a curvature angle of about 90° (223) in order to impart the required stiffness.
- a multiplicity of suitably spaced apart spring tags (224) acts as the contact element with the gas-diffusion electrode (301 ), and a multiplicity of holes (225) favours the gas supply and circulation, in this case with particular reference to the oxygen required for the cathodic reaction.
- FIG. 5 shows a variation of the preferred embodiment shown in figure 4 of the multiplicity of conductive protrusions obtained from a single metal sheet: in this case the original metal sheet is a punched sheet, and the multiplicity of holes (225') extends on the whole body of the tile (222), including the spring tags (224).
- an enhanced gas supply is obtained, also effective when the spring tags (224) are compressed until the end of stroke, coming in contact with the sheet from whence they are projected.
- An albeit marginal saving in the manufacturing phase is also obtained, consisting of the independent execution of holes (225) indicated on tile (222) of figure 4.
- the tile configuration also presents a further mechanical advantage: in case of a sudden high cathode counterpressure (for instance due to errors in the control of process conditions, or to element handling and assembling mistakes), the spring tags do not undergo a permanent deformation in view of the abutment of the GDE on the whole tile surface. In this case, the fact that the tiles are obtained from a punched sheet is even more important to guarantee the correct gas supply in any case, as is it evident to one skilled in the art.
- a lab experimental electrolysis cell of 0.16 m 2 active area was equipped according to the scheme of figure 2 with a titanium DSA ® anode (302) provided with a ruthenium and titanium oxide-based catalytic coating, a National ® N982 ion-exchange membrane (500) commercialised by Dupont/USA, a nickel foam percolator, a gas-diffusion electrode consisting of a silver net activated with a silver-based catalyst.
- the electric current feed system was comprised of a multiplicity of elastic conductive protrusions each consisting of a tile (222) as illustrated in figure 5, obtained from a 1 mm thick nickel punched sheet.
- the cell anodic compartment was fed with a circulating sodium chloride brine having a concentration of 210 g/l, at a current density of 4 kA/m 2 and at a temperature of 90 0 C.
- the cathodic product consisted of 32% by weight caustic soda flowing downwards across the percolator. In these conditions, after stabilising the process conditions on the plant for ten days, a cell voltage comprised between 2.00 and 2.05 V was detected.
- test of example 1 was repeated in analogous conditions, making use of a cell of the prior art.
- the only substantial difference consisted therefore in the cathodic current feed system, comprising a rigid current collector structure consisting of a nickel rib array welded to the cathodic back-wall coupled to a commercial nickel mattress.
Landscapes
- 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)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Fuel Cell (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT000054A ITMI20060054A1 (it) | 2006-01-16 | 2006-01-16 | Distributore di corrente elastico per celle a percolatore |
PCT/EP2007/050362 WO2007080193A2 (en) | 2006-01-16 | 2007-01-15 | Elastic current distributor for percolating cells |
Publications (1)
Publication Number | Publication Date |
---|---|
EP1977027A2 true EP1977027A2 (en) | 2008-10-08 |
Family
ID=38141182
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP07703878A Withdrawn EP1977027A2 (en) | 2006-01-16 | 2007-01-15 | Elastic current distributor for percolating cells |
Country Status (10)
Country | Link |
---|---|
US (1) | US20090050472A1 (ru) |
EP (1) | EP1977027A2 (ru) |
JP (2) | JP2009523906A (ru) |
KR (1) | KR101362680B1 (ru) |
CN (1) | CN101370966B (ru) |
BR (1) | BRPI0706587A2 (ru) |
CA (1) | CA2635098C (ru) |
IT (1) | ITMI20060054A1 (ru) |
RU (1) | RU2423554C2 (ru) |
WO (1) | WO2007080193A2 (ru) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ITMI20071375A1 (it) * | 2007-07-10 | 2009-01-11 | Uhdenora Spa | Collettore di corrente elastico per celle elettrochimiche |
WO2010137284A1 (ja) * | 2009-05-26 | 2010-12-02 | クロリンエンジニアズ株式会社 | ガス拡散電極装着イオン交換膜電解槽 |
DE102010021833A1 (de) * | 2010-05-28 | 2011-12-01 | Uhde Gmbh | Elektrode für Elektrolysezelle |
ITMI20130563A1 (it) * | 2013-04-10 | 2014-10-11 | Uhdenora Spa | Metodo di adeguamento di celle elettrolitiche aventi distanze interelettrodiche finite |
ES2727129T3 (es) | 2014-06-16 | 2019-10-14 | Siemens Ag | Capa de difusión gaseosa, celda electrolítica tipo PEM con una tal capa de difusión gaseosa, así como electrolizador |
CA2951389A1 (en) * | 2014-06-24 | 2015-12-30 | Chemetics Inc. | Narrow gap, undivided electrolysis cell |
KR20180128962A (ko) | 2016-04-07 | 2018-12-04 | 코베스트로 도이칠란트 아게 | 클로르-알칼리 전기분해를 위한 이중기능성 전극 및 전기분해 장치 |
EP3464683B1 (en) * | 2016-05-26 | 2021-07-07 | Calera Corporation | Anode assembly, contact strips, electrochemical cell, and methods to use and manufacture thereof |
JP6656091B2 (ja) * | 2016-06-14 | 2020-03-04 | ティッセンクルップ・ウーデ・クロリンエンジニアズ ゲー エム ベー ハー | 電解槽 |
DE102018209520A1 (de) * | 2018-06-14 | 2019-12-19 | Thyssenkrupp Uhde Chlorine Engineers Gmbh | Elektrolysezelle |
WO2020022440A1 (ja) | 2018-07-27 | 2020-01-30 | 株式会社大阪ソーダ | 電解槽用の導電性弾性体および電解槽 |
CN109786781A (zh) * | 2019-03-15 | 2019-05-21 | 徐州华清京昆能源有限公司 | 一种带有气道的一体式电极 |
DK3770303T3 (da) * | 2019-07-26 | 2022-09-26 | Zentrum Fuer Sonnenenergie Und Wasserstoff Forschung Baden Wuerttemberg | Elektrodepakningsenhed til en stabelstruktur for en elektrokemisk reaktor |
DE102020206448A1 (de) * | 2020-05-25 | 2021-11-25 | Siemens Aktiengesellschaft | Vorrichtung zum Befestigen einer Elektrode |
EP4279637A1 (de) | 2022-05-18 | 2023-11-22 | Zentrum für Sonnenenergie- und Wasserstoff-Forschung Baden-Württemberg | Elektrodenplatte mit integrierter stromübertragerstruktur und elektrodenpackungseinheit |
EP4339334A1 (en) * | 2022-09-15 | 2024-03-20 | thyssenkrupp nucera AG & Co. KGaA | Electrolysis cell with arched support members |
Family Cites Families (15)
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US4444632A (en) * | 1979-08-03 | 1984-04-24 | Oronzio Denora Impianti Elettrochimici S.P.A. | Electrolysis cell |
IT8025483A0 (it) * | 1980-10-21 | 1980-10-21 | Oronzio De Nora Impianti | Elettrocdi per celle ad elettrolita solido applicati sulla superficie di membrane scambiatrici di ioni e procedimentodi prparazione ed uso degli stessi. |
IT1122699B (it) * | 1979-08-03 | 1986-04-23 | Oronzio De Nora Impianti | Collettore elettrico resiliente e cella elettrochimica ad elettrolita solido comprendente lo stesso |
JPH0670276B2 (ja) * | 1983-05-02 | 1994-09-07 | オロンジオ・ド・ノラ・イムピアンチ・エレットロキミシ・ソシエタ・ペル・アジオニ | 塩素発生方法及びその電解槽 |
DE3439265A1 (de) * | 1984-10-26 | 1986-05-07 | Hoechst Ag, 6230 Frankfurt | Elektrolyseapparat mit horizontal angeordneten elektroden |
JP3110551B2 (ja) * | 1992-04-30 | 2000-11-20 | クロリンエンジニアズ株式会社 | 電解槽 |
IT1317753B1 (it) * | 2000-02-02 | 2003-07-15 | Nora S P A Ora De Nora Impiant | Cella di elettrolisi con elettrodo a diffusione di gas. |
WO2002103082A1 (en) * | 2001-06-15 | 2002-12-27 | Akzo Nobel N.V. | Electrolytic cell |
US7141147B2 (en) * | 2001-06-15 | 2006-11-28 | Akzo Nobel N.V. | Electrolytic cell |
DE10138214A1 (de) * | 2001-08-03 | 2003-02-20 | Bayer Ag | Elektrolysezelle und Verfahren zur elektrochemischen Herstellung von Chlor |
ITMI20012379A1 (it) * | 2001-11-12 | 2003-05-12 | Uhdenora Technologies Srl | Cella di elettrolisi con elettrodi a diffusione di gas |
DE10203689A1 (de) * | 2002-01-31 | 2003-08-07 | Bayer Ag | Kathodischer Stromverteiler für Elektrolysezellen |
JP3501453B2 (ja) * | 2002-04-05 | 2004-03-02 | クロリンエンジニアズ株式会社 | イオン交換膜電解槽 |
DE60302610T2 (de) * | 2002-04-05 | 2006-07-06 | Chlorine Engineers Corp., Ltd. | Ionenaustauschmembran-Elektrolyseur |
JP4297694B2 (ja) * | 2003-02-13 | 2009-07-15 | クロリンエンジニアズ株式会社 | ガス拡散陰極を用いたイオン交換膜型電解槽及びその運転方法 |
-
2006
- 2006-01-16 IT IT000054A patent/ITMI20060054A1/it unknown
-
2007
- 2007-01-15 BR BRPI0706587-6A patent/BRPI0706587A2/pt not_active IP Right Cessation
- 2007-01-15 CA CA2635098A patent/CA2635098C/en not_active Expired - Fee Related
- 2007-01-15 CN CN2007800024095A patent/CN101370966B/zh not_active Expired - Fee Related
- 2007-01-15 US US12/087,196 patent/US20090050472A1/en not_active Abandoned
- 2007-01-15 RU RU2008133577/07A patent/RU2423554C2/ru not_active IP Right Cessation
- 2007-01-15 WO PCT/EP2007/050362 patent/WO2007080193A2/en active Application Filing
- 2007-01-15 KR KR1020087020039A patent/KR101362680B1/ko not_active IP Right Cessation
- 2007-01-15 JP JP2008549885A patent/JP2009523906A/ja not_active Withdrawn
- 2007-01-15 EP EP07703878A patent/EP1977027A2/en not_active Withdrawn
-
2014
- 2014-02-17 JP JP2014027391A patent/JP5860075B2/ja not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
WO2007080193A3 (en) | 2007-11-29 |
ITMI20060054A1 (it) | 2007-07-17 |
JP2014088629A (ja) | 2014-05-15 |
CA2635098C (en) | 2016-03-08 |
KR101362680B1 (ko) | 2014-02-13 |
CN101370966B (zh) | 2013-05-08 |
US20090050472A1 (en) | 2009-02-26 |
KR20080087037A (ko) | 2008-09-29 |
CA2635098A1 (en) | 2007-07-19 |
WO2007080193A2 (en) | 2007-07-19 |
JP5860075B2 (ja) | 2016-02-16 |
BRPI0706587A2 (pt) | 2011-03-29 |
JP2009523906A (ja) | 2009-06-25 |
CN101370966A (zh) | 2009-02-18 |
RU2008133577A (ru) | 2010-02-27 |
RU2423554C2 (ru) | 2011-07-10 |
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