US4056448A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for brine membrane cell operation with external caustic and nacl concentration control
Assignee: Diamond Shamrock Chemicals Co
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Filing: 1976-12-17
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Granted: 1977-11-01
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Expires: 1996-12-17
Abstract
Abstract Optimum current efficiencies are attained and maintained in a membrane chlor-alkali electrolytic cell by the constant, precise control of both the brine and caustic concentrations at each membrane phase boundary. Such control requires recycling through external holding tanks wherein the concentrations are adjusted to 560 grams per liter caustic and 190 grams per liter brine. Turbulent flow of such concentrations in the cells helps maintain the optimum concentration and also decreases the diffusion layer.
Inventors
- 👤 Andrew D. Babinsky
- 👤 Ronald L. Dotson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 19:25
CPC Classifications
C; C25; C25B; C25B1/00; C25B1/01; C25B1/34; C25B1/46
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
113 words
In a process for the electrolysis of an aqueous sodium chloride solution in an electrolytic cell the anolyte and catholyte compartments of which are separated by an electrolytically-conductive, hydraulically impervious, cation permselective membrane, having an equivalent weight of approximately 1200, the improvement which consists essentially of establishing and maintaining the sodium hydroxide concentration in the catholyte within the range of about 540 -580 grams per liter by the addition of water from outside the cell and simultaneously establishing and maintaining the sodium chloride concentration in the anolyte within the range of about 170 to 210 grams per liter while maintaining the current density in the range 0.75 to 1.25 amperes per square inch.
Claim 2
Dependent Claim
113 words
In a process for the electrolysis of an aqueous sodium chloride solution in an electrolytic cell the anolyte and catholyte compartments of which are separated by an electrolytically-conductive, hydraulically impervious, cation permselective membrane, having an equivalent weight of approximately 1200, the improvement which consists essentially of establishing and maintaining the sodium hydroxide concentration in the catholyte within the range of about 540 -580 grams per liter by the addition of water from outside the cell and simultaneously establishing and maintaining the sodium chloride concentration in the anolyte within the range of about 170 to 210 grams per liter while maintaining the current density in the range 0.75 to 1.25 amperes per square inch.
Claim 3
Dependent Claim
62 words
A process as stated in claim 1 wherein the sodium chloride concentration is maintained by recycling the solution in the anolyte, adding sodium chloride thereto external of the cell and returning the replenished solution to the cell in such a manner that it impinges on the membrane and at a speed sufficient to reduce the diffusion layer associated with the solution-membrane interface.
Claim 4
Dependent Claim
36 words
A process as stated in claim 2 wherein the sodium hydroxide concentration in the catholyte is maintained by recycling the solution, adding water thereto externally of the cell and returning the adjusted solution to the cathode.
References Cited (Backward Citations)
DE2311556A1
Cited
DE2503652A1
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-10-31 | 1981-05-02 | 1981-11-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-10-31 | 1985-05-02 | 1985-11-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-10-31 | 1989-05-02 | 1989-11-01 | $7700.00 | Window Closed / Lapsed |