US4255407A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for the regeneration of pickling acids
Assignee: Repola Oy
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Filing: 1979-12-07
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Granted: 1981-03-10
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Expires: 1999-12-07
Abstract
Abstract A method for the regeneration of spent pickling acids. Said acid is mixed with such a minor quantity of a stronger acid that the losses of said stronger acid are compensated. The mixture obtained is stripped, whereby the weaker acids are vaporized. The vapor phase containing the weaker acids is passed to a condenser. The condensate obtained forms the regenerated pickling acid. The spent pickling acid can also be passed directly to an evaporator in which a solution containing a stronger acid is circulated. The vapor from the evaporator is passed to an absorption column and thereafter to a condenser, the regenerated acid being formed of the condensate from said condenser.
Inventors
- 👤 Juhani E. Puurunen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 04:11
CPC Classifications
C; C23; C23G; C23G1/00; C23G1/36; Y; Y10; Y10S; Y10S423/00; Y10S423/01
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
176 words
A method for the regeneration of spent pickling acids selected from the group consisting of nitric acid, hydrofluoric acid and mixtures thereof, characterized in that the spent pickling acid is mixed with such a minor quantity of sulphuric acid that the acid removed with the precipitate and any other acid losses are compensated, the mixture obtained is passed to a stripping column (5) in which the mixture comes into contact with steam from an evaporator/crystallizer (7) and the filtrate from a filter or centrifuge (30); whereby the weaker acids are brought into the vapour phase which is passed to a condenser (19), the liquid phase from the stripping column is passed to said evaporator/crystallizer in which the metals are concentrated and from which the vapour obtained is passed through said stripping column to said condenser, the condensate (20) obtained from said condenser forms the regenerated pickling acid, the liquid phase from said evaporator/crystallizer is passed to said filter or centrifuge in which the precipitate is separated, and the filtrate obtained is passed to said stripping column.
Claim 2
Independent Claim
176 words
A method for the regeneration of spent pickling acids selected from the group consisting of nitric acid, hydrofluoric acid and mixtures thereof, characterized in that the spent pickling acid is mixed with such a minor quantity of sulphuric acid that the acid removed with the precipitate and any other acid losses are compensated, the mixture obtained is passed to a stripping column (5) in which the mixture comes into contact with steam from an evaporator/crystallizer (7) and the filtrate from a filter or centrifuge (30); whereby the weaker acids are brought into the vapour phase which is passed to a condenser (19), the liquid phase from the stripping column is passed to said evaporator/crystallizer in which the metals are concentrated and from which the vapour obtained is passed through said stripping column to said condenser, the condensate (20) obtained from said condenser forms the regenerated pickling acid, the liquid phase from said evaporator/crystallizer is passed to said filter or centrifuge in which the precipitate is separated, and the filtrate obtained is passed to said stripping column.
Claim 3
Dependent Claim
82 words
A method as claimed in claim 1, characterized in that the vapour phase obtained from the stripping column is passed to an absorption column (16) in which the vapour substantially uncooled contacts a portion of the condensate from the condenser, whereby of the acids in the vapour phase, a substantial portion of the acid with the lowest vapour pressure is absorbed, and the condensate from the absorption column is combined with the condensate from the condenser, whereby a regenerated acid is formed.
Claim 4
Dependent Claim
173 words
A method as claimed in claim 1, characterized in that the spent pickling acid containing nitric acid and hydrofluoric acid is mixed with sulphuric acid in a quantity according to the material balance, the mixture obtained is passed to the stripping column wherein the mixture contacts the vapour from the evaporator/crystallizer and the filtrate from the filter or centrifuge (30) whereby the nitric acid and the hydrofluoric acid are transferred to the vapour phase, the liquid phase from the stripping column is passed to the evaporator/crystallizer in which the metals entrained into the liquid phase are concentrated as sulphates, the vapour phase from the evaporator/crystallizer is passed through the stripping column to the absorption column for nitric acid in which the vapour substantially uncooled contacts a portion of the condensate from the condenser, whereby a substantial portion of the nitric acid is absorbed in the condensate, the vapour from the absorption column is condensed, whereby the hydrofluoric acid is nearly entirely condensed, that the regenerated acid is formed by combining the condensates obtained.
Claim 5
Independent Claim
104 words
A method for the regeneration of spent pickling acids selected from the group consisting of nitric acid, hydrofluoric acid and mixtures thereof, characterized in that the spent pickling acid is passed directly to the evaporator (7) in which a solution containing sulphuric acid is circulated, and the vapour from the evaporator is passed to the absorption column (16) in which the uncooled vapour contacts a portion of the condensate from the evaporator and from which the vapour is passed to the condenser (19), the regenerated acid being formed of the condensate from said condenser and the condensate that has passed through the absorption column.
Claim 6
Independent Claim
104 words
A method for the regeneration of spent pickling acids selected from the group consisting of nitric acid, hydrofluoric acid and mixtures thereof, characterized in that the spent pickling acid is passed directly to the evaporator (7) in which a solution containing sulphuric acid is circulated, and the vapour from the evaporator is passed to the absorption column (16) in which the uncooled vapour contacts a portion of the condensate from the evaporator and from which the vapour is passed to the condenser (19), the regenerated acid being formed of the condensate from said condenser and the condensate that has passed through the absorption column.
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) | 1984-03-09 | 1984-09-08 | 1985-03-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-03-09 | 1988-09-08 | 1989-03-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-03-09 | 1992-09-08 | 1993-03-10 | $7700.00 | Window Closed / Lapsed |