Patent US4018869A successfully refreshed from Google Patents.
US4018869A
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US
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Process for the extractive purification of phosphoric acid containing cationic impurities
Assignee: Chemische Fabrik Budenhiem KG
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Filing: 1975-05-08
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Granted: 1977-04-19
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Expires: 1995-05-08
Abstract
Abstract A process for the purification of phosphoric acid containing cationic impurities is disclosed wherein there is added to a crude phosphoric acid an organic solvent miscible in all proportions with water and phosphoric acid and thereafter contacting the resulting solution with an inorganic material in aqueous or solid form to effect the preferential passage of the impurities of the crude phosphoric acid/organic solvent solution into an aqueous inorganic phase with phosphoric acid remaining in the organic solvent phase from which purified phosphoric acid is recovered by distillation of the organic solvent.
Inventors
- 👤 Klaus Beltz
- 👤 Klaus Frankenfeld
- 👤 Karl Gotzmann
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 15:45
CPC Classifications
C; C23; C23G; C23G1/00; C23G1/36; C01; C01B; C01B25/00; C01B25/16; C01B25/18; C01B25/234
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
202 words
A process for purifying an aqueous phosphoric acid containing cationic impurities using extraction techniques which comprises: a. adding to said aqueous phosphoric acid an organic solvent miscible in all proportions with phosphoric acid and water selected from the group consisting of an aliphatic alcohol and ketone, the weight ratio of said organic solvent to the weight ratio of P 2 O 5 in said aqueous phosphoric acid being in the range of from 1:1 to 20:1 b. removing any solids residue; c. countercurrently contacting the resulting mixture of step (a) with a concentrated solution of an inorganic multivalent cationic salt selected from the group consisting of aluminum, calcium, magnesium and zinc cationic salts, said inorganic multivalent cationic salt being soluble in water and not tending to form insoluble precipitates during such introduction, the volumetric ratio of said concentrated solution to the volume of said mixture being in the range of from 10:1 to 1:250 thereby forming a liquid aqueous inorganic salt phase including said cationic impurities and a liquid phosphoric acid-organic solvent phase; d. separating said organic solvent phase from said inorganic salt phase; e. repeating steps (c) and (d); and f. recovering phosphoric acid from the organic solvent phase by distillation.
Claim 2
Dependent Claim
202 words
A process for purifying an aqueous phosphoric acid containing cationic impurities using extraction techniques which comprises: a. adding to said aqueous phosphoric acid an organic solvent miscible in all proportions with phosphoric acid and water selected from the group consisting of an aliphatic alcohol and ketone, the weight ratio of said organic solvent to the weight ratio of P 2 O 5 in said aqueous phosphoric acid being in the range of from 1:1 to 20:1 b. removing any solids residue; c. countercurrently contacting the resulting mixture of step (a) with a concentrated solution of an inorganic multivalent cationic salt selected from the group consisting of aluminum, calcium, magnesium and zinc cationic salts, said inorganic multivalent cationic salt being soluble in water and not tending to form insoluble precipitates during such introduction, the volumetric ratio of said concentrated solution to the volume of said mixture being in the range of from 10:1 to 1:250 thereby forming a liquid aqueous inorganic salt phase including said cationic impurities and a liquid phosphoric acid-organic solvent phase; d. separating said organic solvent phase from said inorganic salt phase; e. repeating steps (c) and (d); and f. recovering phosphoric acid from the organic solvent phase by distillation.
Claim 3
Dependent Claim
39 words
The process as defined in claim 1 wherein said concentrated solution of inorganic salt is a solution of a salt of phosphoric acid which is soluble in water and which does not tend to form precipitates in step (c).
Claim 4
Dependent Claim
13 words
The process as defined in claim 1 wherein the aliphatic alcohol is isopropanol.
Claim 5
Dependent Claim
23 words
The process as defined in claim 1 wherein the contact and separation steps are performed in an extraction column operated in countercurrent flow.
Claim 6
Dependent Claim
20 words
The process as defined in claim 1 wherein the process is carried out batch wise in a plurality of mix-settlers.
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) | 1980-04-18 | 1980-10-18 | 1981-04-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-04-18 | 1984-10-18 | 1985-04-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-04-18 | 1988-10-18 | 1989-04-19 | $7700.00 | Window Closed / Lapsed |