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US3976752A Expired / Lapsed US ⏱️ 0.0 years remaining

Manufacture of water-insoluble ammonium polyphosphate

Assignee: Wyeth Holdings LLC
•
Filing: 1974-11-18
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Granted: 1976-08-24
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Expires: 1994-11-18
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Abstract

Abstract A continuous process for preparing crystalline, water-insoluble ammonium polyphosphates of controlled pH utilizing a continuous reaction arena, is disclosed.

Inventors

  • 👤 Hans A. Corver
  • 👤 Allan J. Robertson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 12:33
CPC Classifications
C; C01; C01B; C01B25/00; C01B25/16; C01B25/26; C01B25/28; C01B25/38; C01B25/40; C01B25/405

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 186 words
A continuous process for the production of crystalline, water-insoluble ammonium polyphosphate of a pH ranging from about 4.5-6.5 which comprises (1) admixing either a. a condensed phosphoric acid of P 2 O 5 /H 2 O mole ratio of at least about 0.155 and a combined ammoniating and condensing agent at a mole ratio of about 1.0-3.0 moles of agent per mole of acid, or b. urea phosphate and a combined ammoniating and condensing agent at a ratio of about 0.5-1.05 moles of agent per mole of phosphate, 2. heating the resultant admixture to from about 75°-90°C. to form a melt, 3. contacting the resultant melt with a clean endless moving belt which is preheated to a temperature of from about 150°-200°C. to immediately foam the melt, 4. passing the belt having the resultant foam thereon through a zone heated to from about 180° to about 360°C. to cause ammonia gas to evolve therefrom, 5. venting off said ammonia gas at a rate controlled by the measured pH of the resultant ammonium polyphosphate and 6. recovering the resultant crystalline, water-insoluble ammonium polyphosphate of the above pH.
Claim 2
Dependent Claim 186 words
A continuous process for the production of crystalline, water-insoluble ammonium polyphosphate of a pH ranging from about 4.5-6.5 which comprises (1) admixing either a. a condensed phosphoric acid of P 2 O 5 /H 2 O mole ratio of at least about 0.155 and a combined ammoniating and condensing agent at a mole ratio of about 1.0-3.0 moles of agent per mole of acid, or b. urea phosphate and a combined ammoniating and condensing agent at a ratio of about 0.5-1.05 moles of agent per mole of phosphate, 2. heating the resultant admixture to from about 75°-90°C. to form a melt, 3. contacting the resultant melt with a clean endless moving belt which is preheated to a temperature of from about 150°-200°C. to immediately foam the melt, 4. passing the belt having the resultant foam thereon through a zone heated to from about 180° to about 360°C. to cause ammonia gas to evolve therefrom, 5. venting off said ammonia gas at a rate controlled by the measured pH of the resultant ammonium polyphosphate and 6. recovering the resultant crystalline, water-insoluble ammonium polyphosphate of the above pH.
Claim 3
Dependent Claim 22 words
A process according to claim 1 wherein step (1) comprises admixing a condensed phosphoric acid and a combined ammoniating and condensing agent.
Claim 4
Dependent Claim 20 words
A process according to claim 1 wherein step (1) comprises admixing urea phosphate and a combined ammoniating and condensing agent.
Claim 5
Dependent Claim 14 words
A process according to claim 1 wherein said ammonium polyphosphate is cooled before recovery.

References Cited (Backward Citations)

US3419349A Cited
US3495937A Cited
US3653821A Cited
US3723074A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-24 1980-02-23 1980-08-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-24 1984-02-23 1984-08-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-24 1988-02-23 1988-08-24 $7700.00 Window Closed / Lapsed

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