EP0131724A2 - Diaphragme tissé pour électrolytes aqueux - Google Patents
Diaphragme tissé pour électrolytes aqueux Download PDFInfo
- Publication number
- EP0131724A2 EP0131724A2 EP84106154A EP84106154A EP0131724A2 EP 0131724 A2 EP0131724 A2 EP 0131724A2 EP 84106154 A EP84106154 A EP 84106154A EP 84106154 A EP84106154 A EP 84106154A EP 0131724 A2 EP0131724 A2 EP 0131724A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- diaphragm
- threads
- diaphragm according
- electrolysis
- warp
- 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
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
- C25B13/00—Diaphragms; Spacing elements
Definitions
- the present invention relates to a woven diaphragm for aqueous electrolytes such as alkali chloride solutions, hydrochloric acid solutions and for the water electrolysis of water mixed with acids and / or alkalis.
- non-woven fibers made of asbestos fibers have been used as diaphragms in alkali chloride electrolysis.
- the need to largely replace asbestos has already led to proposals to use fluorocarbon polymers for diaphragms in the form of fabrics or foils, possibly including inorganic fiber structures.
- PVC fabrics have been used in the diaphragm process for hydrochloric acid electrolysis.
- Polytetrafluoroethylene fiber fabrics which have been rendered hydrophilic by an acid and / or radiation treatment have already been proposed for water electrolysis.
- An ideal diaphragm must meet a variety of requirements, such as resistance to the electrolytes and the reaction products, sufficient porosity for the electrolyte passage, good separation properties for the reaction products and low ohmic resistance.
- the present invention now provides diaphragms which are characterized in particular by their weave.
- the present invention relates to a woven diaphragm for electrolytic processes, which is characterized in that both warp and weft threads consist of multifilament threads, at least the multifilament weft thread being untwisted or up to max. 200 tours, preferably up to max. 50 tours, twisted per meter.
- the warp multifilaments can have a twist of 0 to 400 turns per meter, preferably about 100 to 200 turns per meter.
- Warp and weft threads are preferably woven in plain weave, particularly preferably plain weave,.
- the essentially untwisted or low-speed twisted weft threads give the diaphragm a capillarity that is sufficient porosity for the electrolyte passage with a good separation effect for the electrolysis products.
- PVDF Polyvinylidene fluoride
- PPS polyphenylene sulfide
- Ryton trademark of Philipps Petroleum
- fluorocarbon polymers are polyethylene tetrafluoroethylene and copolymers, or polytetrafluoroethylene, especially for sodium chloride electrolysis.
- threads composed of continuous filaments are used in particular. If twisted threads are used as warp threads, these can also be constructed from staple fibers, weaving with spinning flake auxiliaries and, if appropriate, the auxiliary being subsequently removed. If untwisted continuous threads are used as warp threads, the multifilament must be treated with finishing or layering agents before weaving. A twisting with at least 100 tours / m eliminates the use of such means and the effort for their subsequent removal.
- Preferred diaphragms according to the invention have 4 to 28 wefts per cm, preferably 8 to 20 wefts per cm.
- the titer should be 280 to 1100 dtex, single or double, preferably 300 to 600 dtex, double.
- the individual thread is preferably composed of 20 to 70 individual filaments, preferably 35 to 55 individual filaments.
- the chain preferably consists of 25 to 100 warp threads per cm, particularly preferably 45 to 70 warp threads per cm.
- the titer is preferably also 280 to 1100 dtex, particularly preferably 350 to 700 dtex.
- the warp thread can also have a twist of 0 to 400 turns per meter, preferably 100 to 150 turns per meter.
- Warp and weft are preferably selected within the above limits so that the diaphragm has a density of 200 to 600 g / m 2 , particularly preferably 300 to 500 g / m l .
- the cloth After weaving, the cloth can be compacted by calendering.
- the voltage drop during electrolysis at the diaphragm is increased as a result, but a purer quality of the gaseous electrolysis products is achieved.
- the multifilament is woven in a grosgrain weave with 57 warp threads per cm and 11.5 weft threads twice per cm.
- the diaphragm is installed in a test electrolytic cell with graphite electrodes.
- the graphite electrodes have vertical slots in a known manner.
- the electrodes were 11 cm high and 7.3 cm wide. The distance between the electrodes was 4 mm.
- the diaphragm was clamped between the electrode frames with rubber seals. 23% hydrochloric acid is introduced into the electrode chambers separated by the diaphragm. Depleted 18% hydrochloric acid escapes on the cathode side together with hydrogen and on the anode side together with chlorine.
- the temperature of the hydrochloric acid was 85 ° C.
- the electrolysis was operated with a current density of 5 kA / m2. A voltage drop of 2.32 volts is measured between the electrodes. On the cathode side there was 2.7% chlorine in the hydrogen the purity of the chlorine on the anode side was 99.7%.
- Example 1 The diaphragm used in Example 1 was additionally calendered under heat and pressure. The electrolysis was carried out in the same manner as in Example 1. There was a voltage drop of 2.43 volts. The hydrogen produced on the cathode side had 0.7% chlorine, the purity of the chlorine produced on the anode was 99.5%.
- Example 1 A diaphragm as in Example 1 was used and the electrolysis was carried out in the same way as in Example 1. However, 1% orthodichlorobenzene was added to the hydrochloric acid as an organic impurity. The result was a voltage drop of 2.36 volts, a purity of the chlorine of 99.8% and contamination of the hydrogen gas with 1% chlorine.
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)
- Chemical Or Physical Treatment Of Fibers (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19833321159 DE3321159A1 (de) | 1983-06-11 | 1983-06-11 | Gewebtes diaphragma fuer waessrige elektrolyte |
| DE3321159 | 1983-06-11 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP0131724A2 true EP0131724A2 (fr) | 1985-01-23 |
| EP0131724A3 EP0131724A3 (en) | 1986-10-22 |
| EP0131724B1 EP0131724B1 (fr) | 1988-08-10 |
Family
ID=6201252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP84106154A Expired EP0131724B1 (fr) | 1983-06-11 | 1984-05-30 | Diaphragme tissé pour électrolytes aqueux |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4539082A (fr) |
| EP (1) | EP0131724B1 (fr) |
| DD (1) | DD222045A5 (fr) |
| DE (2) | DE3321159A1 (fr) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4804449A (en) * | 1986-02-25 | 1989-02-14 | Sweeney Charles T | Electrolytic cell |
| US4707228A (en) * | 1986-06-06 | 1987-11-17 | Treadwell Corporation | Diaphragm for electrolytic and electrochemical cells |
| IT1205166B (it) * | 1987-06-22 | 1989-03-15 | Testori Spa Flli | Elemento separatore poroso completamente costituito da polifenilensolfuro,per l'elettrolisi dell'acqua |
| FR2617872B1 (fr) * | 1987-07-09 | 1989-11-24 | Rhone Poulenc Chimie | Diaphragme tisse a base de polychlorure de vinyle; un procede pour son obtention et son utilisation dans l'electrolyse de l'acide chlorhydrique |
| DE102006023261A1 (de) | 2006-05-18 | 2007-11-22 | Bayer Materialscience Ag | Verfahren zur Herstellung von Chlor aus Chlorwasserstoff und Sauerstoff |
| CN101372752B (zh) * | 2007-08-21 | 2010-12-08 | 天津工业大学 | 耐高温碱性水电解槽隔膜及其制备方法 |
| WO2010028052A1 (fr) * | 2008-09-08 | 2010-03-11 | Saint-Gobain Performance Plastics Corporation | Ensemble de couplage sanitaire |
| CN103938337A (zh) * | 2013-01-18 | 2014-07-23 | 东丽纤维研究所(中国)有限公司 | 一种水电解槽用隔膜布及其生产方法 |
| US20190078221A1 (en) * | 2016-04-18 | 2019-03-14 | Toray Fibers&Textiles Research Laboratories (China) Co., Ltd. | Polyphenylene sulfide woven fabric for water electrolyser and manufacturing method thereof |
| US20240305075A1 (en) * | 2023-03-07 | 2024-09-12 | Federal-Mogul Powertrain Llc | Flexible, arc resistant, fluid repellant, high temperature and abrasion resistant, circumferentially continuous, seamless textile sleeve and method of construction thereof |
| CN116479449A (zh) * | 2023-04-28 | 2023-07-25 | 厦门厦迪亚斯环保过滤技术有限公司 | 一种电解槽隔膜支撑网的制备方法 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2942327A (en) * | 1957-08-15 | 1960-06-28 | Landers Corp | Coated fabric |
| BE632859A (fr) * | 1962-05-28 | |||
| FR1470721A (fr) * | 1965-03-04 | 1967-02-24 | Bayer Ag | Procédé pour la préparation d'oxydes d'oléfines |
| US4324606A (en) * | 1979-12-27 | 1982-04-13 | E. I. Du Pont De Nemours And Company | Process for forming a reinforced membrane |
| NO148267C (no) * | 1981-06-16 | 1983-09-07 | Norsk Hydro As | Diafragma for vannelektrolyse |
-
1983
- 1983-06-11 DE DE19833321159 patent/DE3321159A1/de not_active Withdrawn
-
1984
- 1984-05-30 DE DE8484106154T patent/DE3473302D1/de not_active Expired
- 1984-05-30 EP EP84106154A patent/EP0131724B1/fr not_active Expired
- 1984-06-06 US US06/617,691 patent/US4539082A/en not_active Expired - Fee Related
- 1984-06-08 DD DD84263968A patent/DD222045A5/de not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| DD222045A5 (de) | 1985-05-08 |
| EP0131724A3 (en) | 1986-10-22 |
| EP0131724B1 (fr) | 1988-08-10 |
| DE3321159A1 (de) | 1984-12-13 |
| US4539082A (en) | 1985-09-03 |
| DE3473302D1 (en) | 1988-09-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0131724B1 (fr) | Diaphragme tissé pour électrolytes aqueux | |
| DE2311556A1 (de) | Verfahren zur elektrolyse einer waessrigen natriumchloridloesung | |
| DE2713816A1 (de) | Verfahren zur elektrolyse von natriumchloridloesungen | |
| DE2455222A1 (de) | Elektrolysezelle | |
| DE2729589C2 (fr) | ||
| DE2451847A1 (de) | Verfahren zur elektrolytischen herstellung von metallhydroxidloesungen | |
| DE1140907B (de) | Verfahren zur Gewinnung von Chlor aus Soleloesungen | |
| EP0068226B1 (fr) | Diaphragme pour l'électrolyse de l'eau | |
| CH619741A5 (fr) | ||
| DE4438275B4 (de) | Elektrolysezelle und Verfahren zur Elektrolyse einer wässrigen Kochsalzlösung | |
| DE2912271A1 (de) | Verfahren und vorrichtung zur ueberfuehrung und reinigung von halogen und halogenwasserstoffsaeure in einem elektrochemischen system | |
| DE2510362A1 (de) | Gewebter oder gewirkter ionenaustausch-textilstoff und verfahren zur herstellung desselben | |
| DE2816152C2 (de) | Verfahren zur Herstellung von Chlor aus Salzsäure durch Elektrolyse und Salzsäure-Elektrolysezelle | |
| DE2756720A1 (de) | Diaphragmen fuer chloralkalielektrolysezellen | |
| DE3041897A1 (de) | Salzsaeure-elektrolysezelle zur herstellung von chlor und wasserstoff | |
| DE2748082A1 (de) | Elektrolyse von alkalihalogeniden | |
| DE2451846A1 (de) | Verfahren zur elektrolytischen herstellung von metallhydroxidloesungen | |
| DE2134126A1 (de) | Diaphragma für die Chloralkali-Elektrolyse | |
| DE2432416A1 (de) | Verfahren zur gewinnung von elektrolytisch hergestellten alkalichloraten | |
| DE2747381A1 (de) | Verfahren zum elektrolysieren von waessrigen alkalihalogenidloesungen | |
| DE68907351T2 (de) | Elektrolyseverfahren zur Herstellung konzentrierter Natriumhydroxyde, mittels einer Membran. | |
| DE4143172C2 (de) | Verfahren zum Herstellen von Chlor und Alkalihydroxid | |
| DE3029870C2 (de) | Mit einem Glasfasergewebe verstärkte Kationenaustauscher-Membran | |
| EP1061158A2 (fr) | Fonctionnement en parallèle de cellules d'électrolyse à cathode de mercure et à membrane | |
| US4302303A (en) | Permeable diaphragm for an electrochemical cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| 17P | Request for examination filed |
Effective date: 19840530 |
|
| AK | Designated contracting states |
Designated state(s): BE DE FR IT |
|
| PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
| AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): BE DE FR IT |
|
| 17Q | First examination report despatched |
Effective date: 19870806 |
|
| GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
| AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE DE FR IT |
|
| ITF | It: translation for a ep patent filed | ||
| REF | Corresponds to: |
Ref document number: 3473302 Country of ref document: DE Date of ref document: 19880915 |
|
| ET | Fr: translation filed | ||
| PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
| 26N | No opposition filed | ||
| ITTA | It: last paid annual fee | ||
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19960412 Year of fee payment: 13 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19960429 Year of fee payment: 13 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19960522 Year of fee payment: 13 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Effective date: 19970531 |
|
| BERE | Be: lapsed |
Owner name: CRAMER & CO. WEBEREI Effective date: 19970531 Owner name: BAYER A.G. Effective date: 19970531 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19980130 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19980203 |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |