US4061718A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for the recovery of ammonia from liquor from the filters of ammonia-soda plants
Assignee: Solvay SA
•
Filing: 1975-11-05
•
Granted: 1977-12-06
•
Expires: 1995-11-05
Abstract
Abstract A method for the recovery of ammonia from liquor from the filters of ammonia-soda plants, which contains free ammonia and ammonium chloride. In this method the liquor is heated to release the free ammonia, and the remaining liquor is then treated successively in a prelimer with lime in an amount insufficient to decompose the whole part of the ammonium chloride and in a still with steam and an alkali metal hydroxide in an amount sufficient to decompose the remaining part of ammonium chloride.
Inventors
- 👤 Jean Verlaeten
- 👤 Paul Demilie
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 00:45
CPC Classifications
C; C01; C01C; C01C1/00; C01C1/02; C01C1/10; C01D; C01D7/00; C01D7/18
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
161 words
In a method for the recovery of ammonia from liquor from filters of ammonia-soda plants which contains free ammonia and ammonium chloride, wherein the liquor is heated and traversed by a current of steam in a heating column to release more particularly the free ammonia, then is treated in a prelimer with a basic agent in an amount sufficient to decompose the major part but not the whole of the ammonium chloride with liberation of ammonia and is finally treated with steam so as to entrain liberated gaseous products in a still where there also is introduced the balance of basic agent needed to decompose the whole of the ammonium chloride, the improvement wherein: prelimer is lime, the balance used in the still is an alkali metal hydroxide, and the amount of alkali metal hydroxide added is controlled in response to the presence of ammonium ions in the still outlet so as to minimize said amount of alkali metal hydroxide added.
Claim 2
Dependent Claim
161 words
In a method for the recovery of ammonia from liquor from filters of ammonia-soda plants which contains free ammonia and ammonium chloride, wherein the liquor is heated and traversed by a current of steam in a heating column to release more particularly the free ammonia, then is treated in a prelimer with a basic agent in an amount sufficient to decompose the major part but not the whole of the ammonium chloride with liberation of ammonia and is finally treated with steam so as to entrain liberated gaseous products in a still where there also is introduced the balance of basic agent needed to decompose the whole of the ammonium chloride, the improvement wherein: prelimer is lime, the balance used in the still is an alkali metal hydroxide, and the amount of alkali metal hydroxide added is controlled in response to the presence of ammonium ions in the still outlet so as to minimize said amount of alkali metal hydroxide added.
Claim 3
Dependent Claim
50 words
Method according to claim 1, wherein the alkali metal hydroxide is added in such an amount that the total amount of lime and alkali metal hydroxide added to the liquor is substantially equal to the stoichiometric amount of basic agent necessary to dissociate all the ammonium chloride of the liquor.
Claim 4
Dependent Claim
39 words
Method according to claim 1 wherein the amount of alkali metal hydroxide to be introduced in the liquor in the still is controlled by measuring the pH of the liquor just before removing the liquor out of the still.
Claim 5
Dependent Claim
22 words
Method according to claim 1 wherein the balance of basic agent introduced into the still is an aqueous solution of caustic soda.
Claim 6
Dependent Claim
23 words
Method according to claim 4, wherein the balance of basic agent introduce into the still is an aqueous solution of electrolytic caustic soda.
Claim 7
Dependent Claim
60 words
Method according to claim 1 wherein the alkali metal hydroxide is introduced in the liquor on a tray of the still adjacent to but before the last tray of the still with respect to the direction of the liquor circulation in the still, in an amount adapted to maintain the pH of the liquor leaving the still at about 9.5.
Claim 8
Dependent Claim
39 words
Method according to claim 6 wherein pH measurements of the liquor are carried out respectively on the last tray of the still and on the tray before the tray whereon the alkali metal hydroxide is introduced in the liquor.
Claim 9
Dependent Claim
16 words
Method according to claim 5 wherein the aqueous solution of electrolytic caustic soda contains sodium chloride.
References Cited (Backward Citations)
DE82328C
Cited
CA542096A
Cited
US1118332A
Cited
GB164335A
Cited
US1838587A
Cited
DE1141267B
Cited
US3329479A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-12-05 | 1981-06-06 | 1981-12-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-12-05 | 1985-06-06 | 1985-12-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-12-05 | 1989-06-06 | 1989-12-06 | $7700.00 | Window Closed / Lapsed |