WO1997005300B1 - Method for starting a chlor-alkali diaphragm cell - Google Patents

Method for starting a chlor-alkali diaphragm cell

Info

Publication number
WO1997005300B1
WO1997005300B1 PCT/US1996/012096 US9612096W WO9705300B1 WO 1997005300 B1 WO1997005300 B1 WO 1997005300B1 US 9612096 W US9612096 W US 9612096W WO 9705300 B1 WO9705300 B1 WO 9705300B1
Authority
WO
WIPO (PCT)
Prior art keywords
amphoteric
aluminum
anolyte
added
original
Prior art date
Application number
PCT/US1996/012096
Other languages
French (fr)
Other versions
WO1997005300A1 (en
Filing date
Publication date
Priority claimed from US08/507,173 external-priority patent/US5630930A/en
Application filed filed Critical
Priority to CA002223854A priority Critical patent/CA2223854C/en
Priority to DE69622188T priority patent/DE69622188T2/en
Priority to EP96926757A priority patent/EP0865517B1/en
Publication of WO1997005300A1 publication Critical patent/WO1997005300A1/en
Publication of WO1997005300B1 publication Critical patent/WO1997005300B1/en

Links

Abstract

Describes adding an anolyte soluble amphoteric material, e.g., an aluminum compound, to the anolyte of a chlor-alkali diaphragm cell having a synthetic diaphragm during the start-up period of the cell to reduce the permeability of the diaphragm. Complementary inorganic porosity modifying materials, e.g., magnesium materials such as magnesium chloride, and clays are also added to the anolyte during the start-up period of the cell.

Claims

AMENDED CLAIMS
[received by the International Bureau on 24 February 1997 (24.02.97); original claims 4-6 and 13-17 cancelled; original claims 1 and 9 amended; new claims 18-26 added; remaining claims unchanged (3 pages)]
1. In the process of operating a chlor-alkali electrolytic cell having a synthetic liquid permeable diaphragm separating the anolyte compartment from the catholyte compartment, the improvement which comprises introducing into the anolyte compartment during the cell start-up period a permeability moderating amount of inorganic amphoteric material that is soluble in the anolyte, that has an insoluble form under the conditions existing within the diaphragm, and that is dissolved by product catholyte liquor.
2. The process of claim 1 wherein the chlor- alkali cell electrolyzes sodium chloride brine and the product catholyte liquor is sodium hydroxide.
3. The process of claim 2 wherein the amphoteric material is selected from compounds of aluminum, zinc and mixtures of such compounds.
7. The process of claim 3 wherein the amphoteric compound is added at cell start-up.
8. The process of claim 3 wherein the product catholyte liquor has a concentration of from 9.5 to 11.5 weight percent sodium hydroxide.
9. The process of claim 3 wherein a permeability moderating amount of non-amphoteric inorganic material is added also to the anolyte during the cell start-up period. 33
10. The process of claim 9 wherein the non- amphoteric inorganic material is selected from magnesium compounds, zirconium compounds, amphibole clays, smectite clays and mixtures of such inorganic materials.
11. The process of claim 10 wherein the non- amphoteric inorganic material is magnesium chloride, magnesium chloride hydrates, clays selected from attapulgite, sepiolite, montmorillonite, saponite and hectorite clays, and mixtures of such inorganic materials.
12. The process of claim 9 wherein the non- amphoteric inorganic material is added to the anolyte contemporaneously with the amphoteric material.
18. In the process of operating a chlor-alkali electrolytic cell for the electrolysis of sodium chloride brine, said cell having a synthetic liquid permeable diaphragm separating the anolyte compartment from the catholyte compartment, the improvement which comprises introducing into the anolyte compartment during the cell start-up period a permeability moderating amount of an amphoteric aluminum compound selected from aluminum chloride, aluminum sulfate, aluminum nitrate, hydrates of said aluminum compounds and readily soluble forms of aluminum hydroxide.
19. The process of claim 18 wherein from 8 to 50 grams of the aluminum compound, calculated as elemental aluminum, per square meter of diaphragm surface area is used.
20 . The process of claim 19 wherein from 15 to 35 grams of the aluminum compound are used. 21. The process of claim 18 wherein a permeability moderating amount of non-amphoteric inorganic material selected from magnesium compounds and clays are added also to the anolyte during the start-up period.
22. The process of claim 21 wherein the non- amphoteric inorganic material is selected from magnesium chloride, magnesium chloride hydrates, clays selected from attapulgite, sepiolite, montmorillonite, saponite and hectorite clays, and mixtures of such inorganic materials.
23. The process of claim 22 wherein from 15 to 35 grams of the aluminum compound, calculated as aluminum, per square meter of diaphragm surface,* from 2 to 40 grams of the magnesium compound, calculated as magnesium, per square meter of diaphragm surface, and from 20 to 200 grams of clay per square meter of diaphragm surface, are added to the anolyte.
24. The process of claim 21 wherein the amphoteric material is aluminum chloride or hydrates of aluminum chloride; and the non-amphoteric material is magnesium chloride, hydrates of magnesium chloride, attapulgite clay and mixtures of said non-amphoteric materials.
25. The process of claim 24 wherein the amphoteric material is added at cell start-up.
26. The process of claim 22 wherein the non- amphoteric inorganic material is added to the anolyte contemporaneously with the amphoteric material. 35
Statement Under Article 19
Claim 1 has been amended to specify that the diaphragm is "liquid permeable". Basis for this amendment may be found on page 1, line 20 of the specification. This amendment makes more explicit what waε implicit in the claim,* namely, that diaphragms used in chlor-alkali electrolytic cells are permeable to liquid, e.g., the alkali metal halide aqueous solution, introduced into the anolyte compartment.
Claim 9 has been amended to state that the non-amphoteric inorganic material is "also" added to the anolyte during the cell start-up period, i.e., the non-amphoteric material is added in addition to the permeability moderating amount of inorganic amphoteric material.
Claim 18 is based on original claims 1, 2 and 4. Claims 19 and 20 are based respectively on original claims 5 and 6. Claim 21 is based on original claim 13; claim 22 is based on original claim 11; and claim 23 is based on original claim 14. Claim 24 is based on original claim 4, and claim 25 is based on original claim 7. Finally, claim 26 is based on original claim 12.
The foregoing amendments to the claims conform the pending claims to the corresponding priority U.S. application, which claims have been allowed.
PCT/US1996/012096 1995-07-26 1996-07-23 Method for starting a chlor-alkali diaphragm cell WO1997005300A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CA002223854A CA2223854C (en) 1995-07-26 1996-07-23 Method for starting a chlor-alkali diaphragm cell
DE69622188T DE69622188T2 (en) 1995-07-26 1996-07-23 METHOD FOR STARTING A CHLORINE ALKALI DIAPHRAGIC CELL
EP96926757A EP0865517B1 (en) 1995-07-26 1996-07-23 Method for starting a chlor-alkali diaphragm cell

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/507,173 US5630930A (en) 1995-07-26 1995-07-26 Method for starting a chlor-alkali diaphragm cell
US08/507,173 1995-07-26

Publications (2)

Publication Number Publication Date
WO1997005300A1 WO1997005300A1 (en) 1997-02-13
WO1997005300B1 true WO1997005300B1 (en) 1997-03-27

Family

ID=24017544

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1996/012096 WO1997005300A1 (en) 1995-07-26 1996-07-23 Method for starting a chlor-alkali diaphragm cell

Country Status (5)

Country Link
US (1) US5630930A (en)
EP (1) EP0865517B1 (en)
CA (1) CA2223854C (en)
DE (1) DE69622188T2 (en)
WO (1) WO1997005300A1 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19650316A1 (en) * 1996-12-04 1998-06-10 Basf Ag Process for modifying the flow resistance of diaphragms
US6296745B1 (en) 2000-04-28 2001-10-02 Ppg Industries Ohio, Inc. Method of operating chlor-alkali electrolytic cells
US7329332B2 (en) * 2004-08-25 2008-02-12 Ppg Industries Ohio, Inc. Diaphragm for electrolytic cell
US7618527B2 (en) * 2005-08-31 2009-11-17 Ppg Industries Ohio, Inc. Method of operating a diaphragm electrolytic cell
US8460536B2 (en) * 2006-01-19 2013-06-11 Eagle Controlled 2 Ohio Spinco, Inc. Diaphragm for electrolytic cell
US8784620B2 (en) 2010-05-13 2014-07-22 Axiall Ohio, Inc. Method of operating a diaphragm electrolytic cell
WO2019055815A1 (en) * 2017-09-15 2019-03-21 Dow Global Technologies Llc Electrolyte permeable diaphragm
WO2019055801A1 (en) * 2017-09-15 2019-03-21 Dow Global Technologies Llc Temporarily modifying the permeability of an electrolyte permeable diaphragm
EP3670706B1 (en) * 2018-12-18 2024-02-21 Covestro Deutschland AG Method for the membrane electrolysis of alkali chloride solutions with gas diffusion electrode

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BE795460A (en) * 1972-02-16 1973-08-16 Diamond Shamrock Corp PERFECTIONS RELATING TO ELECTROLYTIC TANKS
US3991251A (en) * 1973-10-03 1976-11-09 Ppg Industries, Inc. Treatment of asbestos diaphragms and resulting diaphragm
US4210515A (en) * 1975-02-10 1980-07-01 Basf Wyandotte Corporation Thermoplastic fibers as separator or diaphragm in electrochemical cells
US4184939A (en) * 1977-09-26 1980-01-22 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4207163A (en) * 1977-09-26 1980-06-10 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4278524A (en) * 1977-09-26 1981-07-14 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4216072A (en) * 1977-11-10 1980-08-05 Olin Corporation Diaphragms for use in the electrolysis of alkali metal chlorides
US4170537A (en) * 1978-10-20 1979-10-09 Ppg Industries, Inc. Method of preparing a diaphragm having a gel of a hydrous oxide of zirconium in a porous matrix
US4170539A (en) * 1978-10-20 1979-10-09 Ppg Industries, Inc. Diaphragm having zirconium oxide and a hydrophilic fluorocarbon resin in a hydrophobic matrix
US4170538A (en) * 1978-10-20 1979-10-09 Ppg Industries, Inc. Diaphragm having zirconium and magnesium compounds in a porous matrix
US4173526A (en) * 1978-11-21 1979-11-06 E. I. Du Pont De Nemours And Company Chlor-alkali cell diaphragm and its treatment
US4416757A (en) * 1978-12-22 1983-11-22 Olin Corporation Coated thermoplastic polymer diaphragms and a method for their preparation
US4253935A (en) * 1979-09-19 1981-03-03 Ppg Industries, Inc. Method of preparing a diaphragm having a gel of a hydrous oxide or zirconium in a porous matrix
US4606805A (en) * 1982-09-03 1986-08-19 The Dow Chemical Company Electrolyte permeable diaphragm and method of making same
US4665120A (en) * 1983-01-27 1987-05-12 Eltech Systems Corporation Modified liquid permeable asbestos diaphragms with improved dimensional stability
US4853101A (en) * 1984-09-17 1989-08-01 Eltech Systems Corporation Porous separator comprising inorganic/polymer composite fiber and method of making same
US4666573A (en) * 1985-09-05 1987-05-19 Ppg Industries, Inc. Synthetic diaphragm and process of use thereof
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US5188712A (en) * 1991-01-03 1993-02-23 Ppg Industries, Inc. Diaphragm for use in chlor-alkali cells

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