US4260592A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Manufacture of water-insoluble ammonium polyphosphate
Assignee: Cyanamid Canada Inc
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Filing: 1979-08-24
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Granted: 1981-04-07
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Expires: 1999-08-24
Abstract
Abstract Preparation of crystalline water-insoluble ammonium polyphosphate through processing a melt of urea and phosphoric acid or alternatively processing solid urea phosphate. Contact between the exiting product and recycled gaseous by-products ensures proper pH.
Inventors
- 👤 Hans A. Corver
- 👤 Allan J. Robertson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 07:54
CPC Classifications
C; C01; C01B; C01B25/00; C01B25/16; C01B25/26; C01B25/38; C01B25/40; C01B25/405
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
215 words
A process for preparing a crystalline water-insoluble ammonium polyphosphate of the general formula: H.sub.(n-m+2) (NH.sub.4).sub.m P.sub.n O.sub.(3n+2) wherein n is an integer having an average value greater than 10, m /n has an average value in the range of about 0.7 to 1.1, and the maximum value of m is equal to n+2, which process comprises feeding a melt of urea and a condensed phosphoric acid or a solid urea phosphate into the inlet of a jacketed oval-shaped tubular shell reaction zone maintained at a temperature in the range of about 285° C. to about 400° C. to provide a fuming viscous melt which adheres to surfaces of said reaction zone; venting gaseous products from said fuming viscous melt from a vent in the entry end of said reaction zone; constantly removing adherents from said surfaces to provide a powdery solid and advancing said solid to an exit end of said reaction zone at a rate consistent with formation of ammonium polyphosphate by driven paddles; and controlling release of said solid from said exit while recycling said gaseous products vented from said entry end of said reaction zone to said exit end thereof to provide a solid product having a pH in the range of about 4.5 to 6.5 as it exits said reaction zone.
Claim 2
Dependent Claim
215 words
A process for preparing a crystalline water-insoluble ammonium polyphosphate of the general formula: H.sub.(n-m+2) (NH.sub.4).sub.m P.sub.n O.sub.(3n+2) wherein n is an integer having an average value greater than 10, m /n has an average value in the range of about 0.7 to 1.1, and the maximum value of m is equal to n+2, which process comprises feeding a melt of urea and a condensed phosphoric acid or a solid urea phosphate into the inlet of a jacketed oval-shaped tubular shell reaction zone maintained at a temperature in the range of about 285° C. to about 400° C. to provide a fuming viscous melt which adheres to surfaces of said reaction zone; venting gaseous products from said fuming viscous melt from a vent in the entry end of said reaction zone; constantly removing adherents from said surfaces to provide a powdery solid and advancing said solid to an exit end of said reaction zone at a rate consistent with formation of ammonium polyphosphate by driven paddles; and controlling release of said solid from said exit while recycling said gaseous products vented from said entry end of said reaction zone to said exit end thereof to provide a solid product having a pH in the range of about 4.5 to 6.5 as it exits said reaction zone.
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) | 1984-04-06 | 1984-10-06 | 1985-04-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-04-06 | 1988-10-06 | 1989-04-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-04-06 | 1992-10-06 | 1993-04-07 | $7700.00 | Window Closed / Lapsed |