US4238305A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Electrodialytic process for the conversion of impure soda values to sodium hydroxide and carbon dioxide
Assignee: Hmc Patents Holding Co Inc
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Filing: 1979-10-29
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Granted: 1980-12-09
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Expires: 1999-10-29
Abstract
Abstract An electrodialytic process for the conversion of soda sources containing anionic and optionally nonionic impurities to high purity, high strength sodium hydroxide and carbon dioxide gas is disclosed.
Inventors
- 👤 Alan B. Gancy
- 👤 Theodore J. Jenczewski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 03:02
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/42; B01D61/44; B01D61/445; C; C01; C01D; C01D1/00; C01D1/04
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
182 words
A process for the production of high strength, high purity NaOH and CO 2 from soda values in an electrodialysis cell having an anode and a cathode compartment separated by base and acid zones, which comprises the steps of: (a) introducing an aqueous soda solution having NaHCO 3 , Na 2 CO 3 , trona or mixtures thereof to an acid zone of the electrodialysis cell located between a cation permselective face of a bipolar membrane and one face of a cation permselective membrane; (b) introducing an aqueous NaOH solution to a base zone of the cell located between an anion permselective face of a bipolar membrane and the other face of said cation permselective membrane; (c) passing direct electric current through the electrodialysis cell thereby producing H 2 CO 3 and CO 2 gas from the soda solution in the acid zone and producing a NaOH-enriched stream in the base zone; (d) withdrawing the NaOH-enriched product stream from the base zone; and (e) withdrawing H 2 CO 3 and CO 2 gas and partially depleted soda solution from the acid zone.
Claim 2
Dependent Claim
182 words
A process for the production of high strength, high purity NaOH and CO 2 from soda values in an electrodialysis cell having an anode and a cathode compartment separated by base and acid zones, which comprises the steps of: (a) introducing an aqueous soda solution having NaHCO 3 , Na 2 CO 3 , trona or mixtures thereof to an acid zone of the electrodialysis cell located between a cation permselective face of a bipolar membrane and one face of a cation permselective membrane; (b) introducing an aqueous NaOH solution to a base zone of the cell located between an anion permselective face of a bipolar membrane and the other face of said cation permselective membrane; (c) passing direct electric current through the electrodialysis cell thereby producing H 2 CO 3 and CO 2 gas from the soda solution in the acid zone and producing a NaOH-enriched stream in the base zone; (d) withdrawing the NaOH-enriched product stream from the base zone; and (e) withdrawing H 2 CO 3 and CO 2 gas and partially depleted soda solution from the acid zone.
Claim 3
Dependent Claim
29 words
A process as described in claim 1 wherein the Na 2 CO 3 content in the soda solution introduced in step (a) is less than about 12 weight percent.
Claim 4
Dependent Claim
28 words
A process as described in claim 1 wherein in step (a) the soda values have been at least in part derived from sodium carbonate crystallizer mother liquid purge.
Claim 5
Dependent Claim
24 words
A process as described in claim 1 wherein the soda values in step (a) are at least in part derived from trona pond water.
Claim 6
Dependent Claim
23 words
A process as described in claim 1 wherein the soda values in step (a) are at least in part derived from uncalcined trona.
Claim 7
Dependent Claim
35 words
A process as described in claim 5 wherein the initial concentration of NaHCO 3 is less than about 5 weight percent and that of Na 2 CO 3 is less than about 6.2 weight percent.
Claim 8
Dependent Claim
28 words
A process as described in claim 1 wherein the NaOH product stream from step (d) is contacted with CO 2 gas to form Na 2 CO 3 .
Claim 9
Dependent Claim
20 words
A process as described in claim 1 wherein the aqueous soda solution contains sodium bicarbonate from the Solvay ammonia-soda process.
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) | 1983-12-09 | 1984-06-09 | 1984-12-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-12-09 | 1988-06-09 | 1988-12-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-12-09 | 1992-06-09 | 1992-12-09 | $7700.00 | Window Closed / Lapsed |