US4299804A
Expired / Lapsed
US
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Removal of magnesium and aluminum impurities from wet process phosphoric acid
Assignee: Freeport Mcmoran Resource Partners Ltd
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Filing: 1978-03-09
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Granted: 1981-11-10
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Expires: 1998-03-09
Abstract
Abstract Magnesium and aluminum impurities may be removed from wet process phosphoric acid by adding a fluoride ion donating compound, such as hydrofluoric acid, for example, to thereby provide about four fluoride ions for each aluminum ion. Also, preferably, an aluminum ion donating compound, such as alum is added to the wet process acid to bring the aluminum ion to magnesium ion ratio up to about two to one to facilitate formation of crystalline compounds having the general stoichiometry MgAl 2 F 8 . The treated filter grade acid is then further treated in a crystallizer to form large crystals which will readily precipitate so the purified liquid phase, low in magnesium and aluminum containing impurities, may be separated from the crystalline phase.
Inventors
- 👤 Kenneth L. Parks
- 👤 Kyle D. Clevenger
- 👤 Daniel P. McDonald
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-10 00:49
CPC Classifications
C; C01; C01B; C01B25/00; C01B25/16; C01B25/18; C01B25/22; C01B25/222; C01B25/234; C01B25/237; C01B25/238
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
81 words
A method for removing magnesium and aluminum impurities from wet process phosphoric acid without subjecting said acid to treatment for silicon removal, consisting essentially of: adding a fluoride ion donating compound to said unconcentrated wet process phosphoric acid, said fluoride ion donating compound being added in a quantity sufficient to effect an initial fluorine to aluminum ion ratio of from about 3.5/l to about 7/l; and precipitating the resulting insoluble crystalline compounds and separating same from said wet process phosphoric acid.
Claim 2
Independent Claim
81 words
A method for removing magnesium and aluminum impurities from wet process phosphoric acid without subjecting said acid to treatment for silicon removal, consisting essentially of: adding a fluoride ion donating compound to said unconcentrated wet process phosphoric acid, said fluoride ion donating compound being added in a quantity sufficient to effect an initial fluorine to aluminum ion ratio of from about 3.5/l to about 7/l; and precipitating the resulting insoluble crystalline compounds and separating same from said wet process phosphoric acid.
Claim 3
Dependent Claim
29 words
The method of claim 1 wherein said fluoride ion donating compound is selected from the group consisting of hydrofluoric acid, sodium fluoride, sodium bifluoride, ammonium fluoride and ammonium bifluoride.
Claim 4
Dependent Claim
14 words
The method of claim 2 wherein said fluoride ion donating compound is hydrofluoric acid.
Claim 5
Dependent Claim
36 words
The method of claim 1, wherein said fluoride ion is added after filtration of the acidulated phosphate rock to remove solids formed during acidulation and before evaporation of water from said acid to concentrate the acid.
Claim 6
Dependent Claim
62 words
The method of claim 4, including the steps of: adding the fluoride donating compound to the wet process acid in a manner which promotes the growth of crystals which will readily settle and can be easily removed; and separating the liquid and solid phases to produce a wet process phosphoric acid having lesser and controlled amounts of Mg and Al containing impurities.
Claim 7
Dependent Claim
14 words
The method of claim 5, wherein the fluoride ion donating compound is hydrofluoric acid.
Claim 8
Dependent Claim
31 words
The method of claim 1 wherein said fluoride ion donating compound is added to unconcentrated wet process phosphoric acid prior to the filtration thereof to remove the solids formed during acidulation.
Claim 9
Independent Claim
90 words
A method of removing magnesium and aluminum impurities from wet process phosphoric acid without subjecting said acid to treatment for silicon removal, which method comprises: adding to said unconcentrated wet process acid a sufficient quantity of an aluminum ion donating compound to bring the Al ion to Mg ion ratio to a range of from about 1.1/l to about 2.0/l; and adding a sufficient quantity of a fluoride ion donating compound to raise the fluoride ion to Al ion ratio to a range of from about 3.5/l to about 7/l.
Claim 10
Independent Claim
90 words
A method of removing magnesium and aluminum impurities from wet process phosphoric acid without subjecting said acid to treatment for silicon removal, which method comprises: adding to said unconcentrated wet process acid a sufficient quantity of an aluminum ion donating compound to bring the Al ion to Mg ion ratio to a range of from about 1.1/l to about 2.0/l; and adding a sufficient quantity of a fluoride ion donating compound to raise the fluoride ion to Al ion ratio to a range of from about 3.5/l to about 7/l.
Claim 11
Dependent Claim
59 words
The method of claim 8, including the steps of: promoting the growth of crystalline compounds containing Mg, Al and F in the unconcentrated wet process acid after addition of the aluminum ion donating compound and the fluoride ion donating compound; and separating the liquid and solid phases to produce a liquid having reduced levels of Mg and Al impurities.
Claim 12
Dependent Claim
29 words
The method of claim 8 wherein said fluoride ion donating compound is selected from the group consisting of hydrofluoric acid, sodium fluoride, sodium bifluoride, ammonium fluoride and ammonium bifluoride.
Claim 13
Independent Claim
63 words
A method of removing magnesium and aluminum impurities from wet process phosphoric acid without subjecting said acid to treatment for silicon removal, which method consists essentially of: adding a fluoride ion donating compound to filter grade wet process phosphoric acid to provide approximately 4 fluoride ions for each aluminum ion to permit the formation of insoluble crystalline compounds of Mg, Al and F.
Claim 14
Independent Claim
63 words
A method of removing magnesium and aluminum impurities from wet process phosphoric acid without subjecting said acid to treatment for silicon removal, which method consists essentially of: adding a fluoride ion donating compound to filter grade wet process phosphoric acid to provide approximately 4 fluoride ions for each aluminum ion to permit the formation of insoluble crystalline compounds of Mg, Al and F.
Claim 15
Dependent Claim
29 words
The method of claim 11 wherein said fluoride ion donating compound is selected from the group consisting of hydrofluoric acid, sodium fluoride, sodium bifluoride, ammonium fluoride and ammonium bifluoride.
Claim 16
Dependent Claim
14 words
The method of claim 12 wherein said fluoride ion donating compound is hydrofluoric acid.
Claim 17
Dependent Claim
48 words
The method of claim 11, including the steps of: treating the wet process acid to promote growth of relatively large crystals which will readily settle; and separating the liquid and solid phases to produce a wet process phosphoric acid having reduced levels of dissolved Mg and Al impurities.
Claim 18
Dependent Claim
27 words
The method of claim 11, including the step of: adding sufficient alum to bring the Al ion to Mg ion ratio to between about 1.1/l and 2.0/l.
Claim 19
Dependent Claim
35 words
The method of claim 15, wherein said alum is added during digestion of the phosphate rock by a mineral acid and before filtration of the solids formed during digestion from the wet process phosphoric acid.
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) | 1984-11-09 | 1985-05-11 | 1985-11-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-09 | 1989-05-11 | 1989-11-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-09 | 1993-05-11 | 1993-11-10 | $7700.00 | Window Closed / Lapsed |