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US4018869A Expired / Lapsed US ⏱️ 0.0 years remaining

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
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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)

GB464370A Cited
US3872215A Cited
US3764657A Cited
US3684438A Cited
US3862298A Cited

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

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