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US4209369A
Expired / Lapsed
US
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Process for electrolysis of sodium chloride by use of cation exchange membrane
Assignee: Asahi Kasei Corp
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Filing: 1978-12-14
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Granted: 1980-06-24
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Expires: 1998-12-14
Abstract
Abstract In a process for electrolysis of sodium chloride in an electrolytic cell divided into the anode chamber and the cathode chamber by a cation exchange membrane, well brine is used as the starting material for the electrolysis and the dilute aqueous sodium chloride solution formed as the result of the electrolysis is subjected to concentration for re-use as the starting material.
Inventors
- 👤 Maomi Seko
- 👤 Shinsaku Ogawa
- 👤 Reiji Takemura
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 12:49
CPC Classifications
C; C25; C25B; C25B1/00; C25B1/01; C25B1/34; C25B1/46; B; B01; B01D; B01D1/00; B01D1/26; C25B15/00; C25B15/08; C25B15/085; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
155 words
In a process for electrolysis of an aqueous sodium chloride solution in an electrolytic cell divided into an anode chamber and a cathode chamber by a cation exchange membrane between the anode and the cathode by carrying out electrolysis at 50° C. or higher while feeding purified well brine or dilute aqueous solution thereof as the feed sodium chloride solution into the anode chamber, the improvement which comprises using a cation exchange membrane having 50 g. or more of water permeability per current passage of one Faraday and operating the electrolysis by withdrawing a part of the dilute aqueous sodium chloride solution in the anode chamber which is depleted in sodium chloride concentration to a value in the range of from 100 to 250 g/liter, concentrating the solution withdrawn to a concentration ratio in the range of from 1.05 to 3.00, and returning the recovered concentrated sodium chloride solution thus obtained to the anode chamber.
Claim 2
Dependent Claim
155 words
In a process for electrolysis of an aqueous sodium chloride solution in an electrolytic cell divided into an anode chamber and a cathode chamber by a cation exchange membrane between the anode and the cathode by carrying out electrolysis at 50° C. or higher while feeding purified well brine or dilute aqueous solution thereof as the feed sodium chloride solution into the anode chamber, the improvement which comprises using a cation exchange membrane having 50 g. or more of water permeability per current passage of one Faraday and operating the electrolysis by withdrawing a part of the dilute aqueous sodium chloride solution in the anode chamber which is depleted in sodium chloride concentration to a value in the range of from 100 to 250 g/liter, concentrating the solution withdrawn to a concentration ratio in the range of from 1.05 to 3.00, and returning the recovered concentrated sodium chloride solution thus obtained to the anode chamber.
Claim 3
Dependent Claim
29 words
A process according to claim 1, wherein the heat generated in the electolytic cell is used at the heat source for concentration of the dilute aqueous sodium chloride solution.
Claim 4
Dependent Claim
26 words
A process according to claim 1, wherein the means for concentration is selected from the group consisting of multi-stage flash evaporators, multiple-effect evaporators and combinations thereof.
Claim 5
Dependent Claim
40 words
A process according to claim 3, wherein the means for concentration is a multi-stage flash evaporator and wherein the well brine is subjected to electrolysis after being used as a cooling source for condensing part of the multi-stage flash evaporator.
Claim 6
Dependent Claim
108 words
A process according to claim 4, wherein the multi-stage flash evaporator has three divided zones comprising a high temperature zone, a medium temperature zone and a low temperature zone, said dilute sodium chloride solution, said recovered concentrated aqueous sodium chloride solution and said feed aqueous sodium chloride solution being supplied for heat recovery so as to be pre-heated in the condensing parts of said zones, repectively, and wherein the pre-heated dilute aqueous sodium chloride solution is fed into the evaporation chamber, and the pre-heated recovered concentrated aqueous sodium chloride solution and the pre-heated feed aqueous sodium chloride solution are fed to the anode chamber in the electrolytic cell.
Claim 7
Dependent Claim
21 words
A process according to claim 1, wherein the means for concentration is an electrodialysis cell in which ion-exchange membranes are used.
Claim 8
Dependent Claim
27 words
A process according to any of claims 2, 3, 6, 1, 4 or 5 wherein the aqueous sodium chloride solution recovered after concentration is an unsaturated solution.
Claim 9
Dependent Claim
44 words
A process according to any of claims 2, 3, 6, 1, 4, or 5, wherein the cation-exchange membrane has a two-layer structure having on the anode side a layer comprising sulfonic acid groups and on the cathode side a layer comprising weakly acidic groups.
Claim 10
Dependent Claim
15 words
A process according to claim 8, wherein the weakly acidic groups are carboxylic acid groups.
Claim 11
Dependent Claim
59 words
A process according to any of claims 2, 3, 6, 1, 4, or 5, wherein the aqueous sodium chloride solution recovered after concentration is an unsaturated solution, and wherein the cation-exchange membrane has a two layer structure having on the anode side a layer comprising sulfonic acid groups and on the cathode side a layer comprising weakly acidic groups.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-06-24 | 1983-12-24 | 1984-06-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-06-24 | 1987-12-24 | 1988-06-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-06-24 | 1991-12-24 | 1992-06-24 | $7700.00 | Window Closed / Lapsed |