US4275042A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Removal of oxalate from Bayer process liquor
Assignee: Alcan Research and Development Ltd
•
Filing: 1980-01-22
•
Granted: 1981-06-23
•
Expires: 2000-01-22
Abstract
Abstract Sodium oxalate in supersaturated solution in Bayer spent liquor stabilized by the presence of humic material is precipitated by the treatment with cationic sequestrants which interact with the humic material to give an insoluble product, thus removing it from solution and destabilizing the solution with respect to precipitation of sodium oxalate. Preferred cationic sequestrants are quaternary nitrogen compounds including medium or long chain alkyl groups. Precipitation of sodium oxalate can be expidited by addition of seed crystals and/or addition of sodium oxalate solution which is supersaturated at a temperature higher than that of the spent liquor.
Inventors
- 👤 Gordon Lever
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 20:37
CPC Classifications
C; C01; C01F; C01F7/00; C01F7/02; C01F7/46; C01F7/47; C01F7/473
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
162 words
A method for controlling the level of sodium oxalate present in the process liquor in the Bayer process for the production of alumina trihydrate which method comprises the steps of treating spent liquor which contains in excess of 1 gram per liter (as organic carbon) of humic matter and is supersaturated with regard to sodium oxalate, with a cationic sequestrant in an amount to remove sufficient of the said humic matter but not more than 0.5 gram per liter from the said liquor and thereby destabilizing the said liquor with regard to precipitation of sodium oxalate, said sequestrant being an organic cationic sequestrant having a cationic center that interacts with a weakly acidic anionic center in the humic matter to form a product sufficiently insoluble in the Bayer liquor to be physically separable therefrom, holding the said liquor to allow precipitation of sodium oxalate, separating the precipitated sodium oxalate and spent cationic sequestrant and returning the said liquor to the Bayer process.
Claim 2
Independent Claim
162 words
A method for controlling the level of sodium oxalate present in the process liquor in the Bayer process for the production of alumina trihydrate which method comprises the steps of treating spent liquor which contains in excess of 1 gram per liter (as organic carbon) of humic matter and is supersaturated with regard to sodium oxalate, with a cationic sequestrant in an amount to remove sufficient of the said humic matter but not more than 0.5 gram per liter from the said liquor and thereby destabilizing the said liquor with regard to precipitation of sodium oxalate, said sequestrant being an organic cationic sequestrant having a cationic center that interacts with a weakly acidic anionic center in the humic matter to form a product sufficiently insoluble in the Bayer liquor to be physically separable therefrom, holding the said liquor to allow precipitation of sodium oxalate, separating the precipitated sodium oxalate and spent cationic sequestrant and returning the said liquor to the Bayer process.
Claim 3
Dependent Claim
24 words
A method as claimed in claim 1 wherein the cationic sequestrant is a quaternary ammonium compound including at least 1 long chain alkyl group.
Claim 4
Dependent Claim
37 words
A method as claimed in claim 2 wherein the quaternary ammonium compound is one or more chloride or sulphate salts of tallow-trimethyl ammonium, ditallow-dimethyl ammonium, tallow-benzyl-dimethyl ammonium, ditallow-benzyl-methyl ammonium, tallow-dibenzyl-methyl ammonium and the hydrogenated tallow derivatives thereof.
Claim 5
Dependent Claim
32 words
A method as claimed in claim 1 wherein the cationic sequestrant is a heterocyclic quaternary nitrogen compound in which the nitrogen atom carries at least one medium or long chain alkyl group.
Claim 6
Dependent Claim
19 words
A method as claimed in claim 4 wherein the cationic sequestrant is a salt of lauryl pyridinium or diethylheptadecyl-imidazolinium.
Claim 7
Dependent Claim
15 words
A method as claimed in claim 5 wherein the cationic sequestrant is diethyl-heptadecyl-imidazolinium ethyl sulphate.
Claim 8
Dependent Claim
26 words
A method as claimed in claim 1 wherein the amount of cationic sequestrant used is from 0.05 to 0.2 grams per liter of the spent liquor.
Claim 9
Dependent Claim
36 words
A method as claimed in claim 1 wherein from 0.2 to 1 gram per liter of solid sodium oxalate is added to the treated liquor as seed to speed up precipitation of the solid sodium oxalate.
Claim 10
Dependent Claim
28 words
A method as claimed in claim 8 wherein the solid sodium oxalate used as seed is sodium oxalate precipitated from spent liquor by the method of claim 1.
Claim 11
Dependent Claim
23 words
A method as claimed in claim 1 wherein the temperature at which the spent liquor is treated is from 55° to 65° C.
Claim 12
Dependent Claim
43 words
A method as claimed in claim 1 wherein, prior to precipitation of the sodium oxalate from the spent liquor, a solution of sodium oxalate, which is supersaturated at a temperature higher than that of the spent liquor, is added to the spent liquor.
Claim 13
Dependent Claim
23 words
A method as claimed in claim 11 wherein the temperature at which the said solution is saturated is from 75° to 95° C.
Claim 14
Dependent Claim
27 words
A method as claimed in claim 1 wherein the treated spent liquor is held for from 0.5 to 10 hours to allow precipitation of the sodium oxalate.
Claim 15
Dependent Claim
34 words
A method as claimed in claim 1 in which the insoluble interaction product of the cationic sequestrant and the humic material is removed from the spent liquor prior to precipitation of the sodium oxalate.
Claim 16
Dependent Claim
50 words
A method as claimed in claim 14 wherein the insoluble intereaction product is a liquid having a density less than that of the spent liquor and is separated from the spent liquor prior to precipitation of the sodium oxalate by flotation on the upper surface of the treated spent liquor.
References Cited (Backward Citations)
SU207884A1
Cited
US3337305A
Cited
US3457032A
Cited
US3899571A
Cited
US4046855A
Cited
US4038039A
Cited
US4101629A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-06-22 | 1984-12-22 | 1985-06-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-06-22 | 1988-12-22 | 1989-06-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-06-22 | 1992-12-22 | 1993-06-23 | $7700.00 | Window Closed / Lapsed |