US3984525A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Manufacture of phosphoric acid
Assignee: Solvay Solutions UK Ltd
•
Filing: 1974-03-25
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Granted: 1976-10-05
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Expires: 1994-03-25
Abstract
Abstract Production of phosphoric acid by the wet process and by-product calcium sulphate hemihydrate. Sulphuric acid reacts with phosphate rock in such conditions that gypsum is precipitated, the resulting slurry is transferred to a second vessel in which the conditions are such that the gypsum recrystallises to calcium sulphate hemihydrate. Calcium sulphate hemihydrate so produced may be converted to cement and sulphuric acid by a process analogous to the anhydrite process for production of sulphuric acid. The phosphoric acid produced may be desulphated in a process integrated with the phosphoric production.
Inventors
- 👤 Thomas Alan Williams
- 👤 Alexander Thomson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 19:53
CPC Classifications
C; C04; C04B; C04B7/00; C04B7/02; C04B7/04; C01; C01B; C01B25/00; C01B25/16; C01B25/18; C01B25/22
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
160 words
A process for the production of phosphoric acid and calcium sulphate hemihydrate which comprises reacting calcium-containing phosphate rock with sulphuric acid in a first reactor at a temperature between about 60°C and 70°C to precipitate the calcium in said phosphate rock as gypsum slurried with phosphoric acid, transferring the gypsum-phosphoric acid slurry to a second reactor, adding sulphuric acid in a concentration of at least 93% by weight and in an amount sufficient to bring about an SO 3 content of about 7% by weight based on the total contents of the said second reactor and so as to result in a temperature rise to about 75°C so as to cause the gypsum to recrystallize into solid calcium sulphate hemihydrate, the contents of said second reactor having a P 2 O 5 content of about 33% by weight based on the total contents of said second reactor, and separating said calcium sulphate hemihydrate from the phosphoric acid in said slurry.
Claim 2
Dependent Claim
160 words
A process for the production of phosphoric acid and calcium sulphate hemihydrate which comprises reacting calcium-containing phosphate rock with sulphuric acid in a first reactor at a temperature between about 60°C and 70°C to precipitate the calcium in said phosphate rock as gypsum slurried with phosphoric acid, transferring the gypsum-phosphoric acid slurry to a second reactor, adding sulphuric acid in a concentration of at least 93% by weight and in an amount sufficient to bring about an SO 3 content of about 7% by weight based on the total contents of the said second reactor and so as to result in a temperature rise to about 75°C so as to cause the gypsum to recrystallize into solid calcium sulphate hemihydrate, the contents of said second reactor having a P 2 O 5 content of about 33% by weight based on the total contents of said second reactor, and separating said calcium sulphate hemihydrate from the phosphoric acid in said slurry.
Claim 3
Dependent Claim
30 words
The process of claim 1, wherein the sulphuric acid added to said first reactor and reacted with said phosphate rock is in a concentration of at least 77% by weight.
Claim 4
Dependent Claim
42 words
The process of claim 2, wherein about one-quarter of the total weight of sulphuric acid utilized in said process is added to said second reactor and the remaining amount of sulphuric acid used in said process is added to said first reactor.
Claim 5
Dependent Claim
192 words
A cyclic process for the production of phosphoric acid and calcium sulphate hemihydrate which comprises reacting calcium-containing phosphate rock with sulphuric acid in a concentration of at least 77% by weight in a first reactor to precipitate the calcium in said phosphate rock as gypsum slurried with phosphoric acid, transferred the gypsum slurry to a second reactor and adding sufficient sulphuric acid in a concentration of at least about 93% by weight to raise the temperature of the contents of said second reactor to about 75°C and to bring about an SO 2 content of about 7% by weight based on the total content of the said second reactor so as to recrystallize the gypsum into solid calcium sulphate hemihydrate, the contents of said second reactor having a P 2 O 5 content of about 33% by weight based on the total contents of said second reactor, filtering said calcium sulphate hemihydrate from the phosphoric acid in said slurry to obtain a calcium sulphate hemihydrate product and phosphoric acid filtrate, and adding sufficient phosphate rock to said phosphoric acid filtrate to precipitate gypsum and recycling said precipitated gypsum to said first reactor.
Claim 6
Dependent Claim
192 words
A cyclic process for the production of phosphoric acid and calcium sulphate hemihydrate which comprises reacting calcium-containing phosphate rock with sulphuric acid in a concentration of at least 77% by weight in a first reactor to precipitate the calcium in said phosphate rock as gypsum slurried with phosphoric acid, transferred the gypsum slurry to a second reactor and adding sufficient sulphuric acid in a concentration of at least about 93% by weight to raise the temperature of the contents of said second reactor to about 75°C and to bring about an SO 2 content of about 7% by weight based on the total content of the said second reactor so as to recrystallize the gypsum into solid calcium sulphate hemihydrate, the contents of said second reactor having a P 2 O 5 content of about 33% by weight based on the total contents of said second reactor, filtering said calcium sulphate hemihydrate from the phosphoric acid in said slurry to obtain a calcium sulphate hemihydrate product and phosphoric acid filtrate, and adding sufficient phosphate rock to said phosphoric acid filtrate to precipitate gypsum and recycling said precipitated gypsum to said first reactor.
Claim 7
Dependent Claim
192 words
A cyclic process for the production of phosphoric acid and calcium sulphate hemihydrate which comprises reacting calcium-containing phosphate rock with sulphuric acid in a concentration of at least 77% by weight in a first reactor to precipitate the calcium in said phosphate rock as gypsum slurried with phosphoric acid, transferring the gypsum slurry to a second reactor and adding sufficient sulphuric acid in a concentration of at least about 93% by weight to raise the temperature of the contents of said second reactor to about 75°C and to bring about an SO 3 content of about 7% by weight based on the total content of the said second reactor so as to recrystallize the gypsum into solid calcium sulphate hemihydrate, the contents of said second reactor having a P 2 O 5 content of about 33% by weight based on the total contents of said second reactor, filtering said calcium sulphate hemihydrate from the phosphoric acid in said slurry to obtain a calcium sulphate hemihydrate product and phosphoric acid filtrate, and adding sufficient phosphate rock to said phosphoric acid filtrate to precipitate gypsum and recycling said precipitated gypsum to said second reactor.
Claim 8
Dependent Claim
192 words
A cyclic process for the production of phosphoric acid and calcium sulphate hemihydrate which comprises reacting calcium-containing phosphate rock with sulphuric acid in a concentration of at least 77% by weight in a first reactor to precipitate the calcium in said phosphate rock as gypsum slurried with phosphoric acid, transferring the gypsum slurry to a second reactor and adding sufficient sulphuric acid in a concentration of at least about 93% by weight to raise the temperature of the contents of said second reactor to about 75°C and to bring about an SO 3 content of about 7% by weight based on the total content of the said second reactor so as to recrystallize the gypsum into solid calcium sulphate hemihydrate, the contents of said second reactor having a P 2 O 5 content of about 33% by weight based on the total contents of said second reactor, filtering said calcium sulphate hemihydrate from the phosphoric acid in said slurry to obtain a calcium sulphate hemihydrate product and phosphoric acid filtrate, and adding sufficient phosphate rock to said phosphoric acid filtrate to precipitate gypsum and recycling said precipitated gypsum to said second reactor.
References Cited (Backward Citations)
US3124419A
Cited
NL6609093A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-10-05 | 1980-04-05 | 1980-10-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-05 | 1984-04-05 | 1984-10-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-05 | 1988-04-05 | 1988-10-05 | $7700.00 | Window Closed / Lapsed |