US3974263A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing ammonium phosphate in two stages
Assignee: Fisons Ltd
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Filing: 1975-01-10
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Granted: 1976-08-10
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Expires: 1995-01-10
Abstract
Abstract The present invention relates to a two stage process for preparing ammonium phosphates in which ammonia at a comparatively low pressure and recovered from within the process of the invention is reacted with phosphoric acid in the liquid phase to yield an immediate product which is then ammoniated further in the second stage under elevated pressure.
Inventors
- 👤 John David Crerar
- 👤 John David Crowther Hemsley
- 👤 Ian Clive Hepworth
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 16:45
CPC Classifications
C; C05; C05B; C05B7/00; C01; C01B; C01B25/00; C01B25/16; C01B25/26; C01B25/28; C01B25/38; C01B25/40; C01B25/405
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
236 words
A process for producing solid ammonium phosphates in two stages which process comprises reacting in the liquid phase in a first stage phosphoric acid containing from 35 to 60% by weight of P 2 O 5 and up to 20% by weight of H 2 SO 4 at a pressure of from -0.1 to +1.5 kg/cm 2 gauge with ammonia gas obtained from the ammonia-containing off-gases of the second stage of the process so as to produce a fluid ammonium phosphate product having an NH 3 :H 3 PO 4 molar ratio which varies from 0.1:1 to 1.45:1 and containing from 10 to 45% by weight of water; passing the said reaction product from the first stage to a second stage operating at higher pressure wherein the reaction product is reacted at a pressure of from 0.5 to 3.5 kg/cm 2 gauge with ammonia gas to form a fluid ammonium phosphate having an NH 3 :H 3 PO 4 molar ratio of from 0.95:1 to 1.85:1 and a water content of from 4 to 20% by weight; discharging this fluid ammonium phosphate into a zone at lower pressure so as to produce a solid ammonium phosphate containing from 2 to 11% by weight of water: and recovering ammonia values from the off-gases of the said second stage of the process for use as the major source of ammonia gas in the first state of the process.
Claim 2
Dependent Claim
236 words
A process for producing solid ammonium phosphates in two stages which process comprises reacting in the liquid phase in a first stage phosphoric acid containing from 35 to 60% by weight of P 2 O 5 and up to 20% by weight of H 2 SO 4 at a pressure of from -0.1 to +1.5 kg/cm 2 gauge with ammonia gas obtained from the ammonia-containing off-gases of the second stage of the process so as to produce a fluid ammonium phosphate product having an NH 3 :H 3 PO 4 molar ratio which varies from 0.1:1 to 1.45:1 and containing from 10 to 45% by weight of water; passing the said reaction product from the first stage to a second stage operating at higher pressure wherein the reaction product is reacted at a pressure of from 0.5 to 3.5 kg/cm 2 gauge with ammonia gas to form a fluid ammonium phosphate having an NH 3 :H 3 PO 4 molar ratio of from 0.95:1 to 1.85:1 and a water content of from 4 to 20% by weight; discharging this fluid ammonium phosphate into a zone at lower pressure so as to produce a solid ammonium phosphate containing from 2 to 11% by weight of water: and recovering ammonia values from the off-gases of the said second stage of the process for use as the major source of ammonia gas in the first state of the process.
Claim 3
Dependent Claim
41 words
A process as claimed in claim 1 wherein the first stage is carried out to give a fluid ammonium phosphate substantially at its boiling point and having a NH 3 H 3 PO 4 molar ratio of from 0.1:1 to 0.8:1.
Claim 4
Dependent Claim
26 words
A process as claimed in claim 1 wherein the product from the second stage is sprayed onto a tumbling bed of particles in a granulation device.
Claim 5
Dependent Claim
189 words
A two stage process for producing particulate ammonium phosphate which comprises reacting in a first ammoniation stage the off-gases from the second stage of the process with phosphoric acid containing at least 35% P 2 O 5 in a stirred reactor at a pressure of from -0.1 to +1.5 kg/cm 2 gauge to give a fluid ammonium phosphate having an NH 3 :H 3 PO 4 molar ratio of from 0.1:1 to 0.8:1 and substantially at its boiling point; passing the fluid ammonium phosphate to a pressure reactor operated at from 0.5 to 3.5 kg/cm 2 gauge and at 130° to 180°C where it is reacted in a second ammoniation stage with gaseous ammonia to give a boiling fluid ammonium phosphate having an NH 3 :H 3 PO 4 molar ratio of from 0.95:1 to 1.85:1 and containing from 4 to 20% of water; expelling the fluid ammonium phosphate into a solidification zone at ambient pressure in which solid particles are formed; the off-gases from the second ammoniation stage being returned to the first ammoniation stage to provide the major part of the ammonia fed to the first stage.
Claim 6
Dependent Claim
189 words
A two stage process for producing particulate ammonium phosphate which comprises reacting in a first ammoniation stage the off-gases from the second stage of the process with phosphoric acid containing at least 35% P 2 O 5 in a stirred reactor at a pressure of from -0.1 to +1.5 kg/cm 2 gauge to give a fluid ammonium phosphate having an NH 3 :H 3 PO 4 molar ratio of from 0.1:1 to 0.8:1 and substantially at its boiling point; passing the fluid ammonium phosphate to a pressure reactor operated at from 0.5 to 3.5 kg/cm 2 gauge and at 130° to 180°C where it is reacted in a second ammoniation stage with gaseous ammonia to give a boiling fluid ammonium phosphate having an NH 3 :H 3 PO 4 molar ratio of from 0.95:1 to 1.85:1 and containing from 4 to 20% of water; expelling the fluid ammonium phosphate into a solidification zone at ambient pressure in which solid particles are formed; the off-gases from the second ammoniation stage being returned to the first ammoniation stage to provide the major part of the ammonia fed to the first stage.
Claim 7
Dependent Claim
15 words
A process as claimed in claim 4 wherein the solidification zone is a granulation device.
Claim 8
Dependent Claim
47 words
A process as claimed in claim 5 wherein the second ammoniation stage is carried out at an NH 3 :H 3 PO 4 molar ratio of from 0.95:1 to 1.6:1 and the fluid ammonium phosphate is expelled into a granulation device into which ammonia is also fed.
Claim 9
Dependent Claim
23 words
A process as claimed in claim 4 wherein the returned off-gases provide substantially all of the ammonia fed to the first ammoniation stage.
Claim 10
Dependent Claim
57 words
A process as claimed in claim 4 wherein the returned off-gases are passed in heat exchange contact with liquid ammonia so as to vapourise the liquid ammonia to provide gaseous ammonia for use in the second ammoniation stage and so as to condense out water from the off-gases before they are fed to the first ammoniation stage.
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) | 1979-08-10 | 1980-02-09 | 1980-08-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-08-10 | 1984-02-09 | 1984-08-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-08-10 | 1988-02-09 | 1988-08-10 | $7700.00 | Window Closed / Lapsed |