US4147758A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of aluminum polyphosphate
Assignee: Hoechst AG
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Filing: 1977-05-09
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Granted: 1979-04-03
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Expires: 1997-05-09
Abstract
Abstract Aluminum polyphosphate is made. To this end, solid aluminum hydroxide and polyphosphoric acid which are used in proportions corresponding to an Al:P molar ratio of 1:2.5 to 1:3.5, are introduced separately from, but concurrently with, one another into a reaction zone kept at 150° to 200° C. A moist friable consistency of the starting materials is maintained in the reaction zone by continuously mixing, kneading and comminuting them over substantially the entire period during which they are introduced into the reaction zone. The reaction is continued until a dry sandy powder is formed; and the powder is annealed at 400° to 600° C. over a period sufficient to yield a product undergoing a 0.5 to 1% weight loss on ignition.
Inventors
- 👤 Renate Adrian
- 👤 Raban VON Schenck
- 👤 Bernd Cox
- 👤 Peter Wirtz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 10:19
CPC Classifications
C; C04; C04B; C04B12/00; C04B12/02; C04B12/022; C01; C01B; C01B25/00; C01B25/16; C01B25/26; C01B25/38; C01B25/40
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
132 words
A process of producing long chain aluminium polyphosphates as defined in ASTM 13-266, which comprises step (A) of introducing into a reaction zone as starting materials aluminum hydroxide and polyphosphoric acid containing 75 to 85 weight % of P 2 O 5 in amounts corresponding to a molar ratio of Al:P of 1:2.5 to 1:3.5; continuously mixing, kneading and comminuting the starting materials in the reaction zone and heating the resulting mixture at a temperature of 150° to 200° C. for as long as necessary to ensure conversion to a dry, sandy, pulverulent intermediate product; and step (B) of dehydrating said intermediate product by annealing it at temperatures within the range 400° to 600° C. for a period sufficient to yield a final product undergoing 0.5 to 1% weight loss on ignition.
Claim 2
Dependent Claim
132 words
A process of producing long chain aluminium polyphosphates as defined in ASTM 13-266, which comprises step (A) of introducing into a reaction zone as starting materials aluminum hydroxide and polyphosphoric acid containing 75 to 85 weight % of P 2 O 5 in amounts corresponding to a molar ratio of Al:P of 1:2.5 to 1:3.5; continuously mixing, kneading and comminuting the starting materials in the reaction zone and heating the resulting mixture at a temperature of 150° to 200° C. for as long as necessary to ensure conversion to a dry, sandy, pulverulent intermediate product; and step (B) of dehydrating said intermediate product by annealing it at temperatures within the range 400° to 600° C. for a period sufficient to yield a final product undergoing 0.5 to 1% weight loss on ignition.
Claim 3
Dependent Claim
26 words
The process as claimed in claim 1, wherein the proportions of the aluminum hydroxide and polyphosphoric acid corresponding to an Al:P molar ratio of substantially 1:3.
Claim 4
Dependent Claim
22 words
The process as claimed in claim 1, wherein the polyphosphoric acid used contains substantially 84 weight% of P 2 O 5 .
Claim 5
Dependent Claim
19 words
The process as claimed in claim 1, wherein the reaction is effected at a temperature of approximately 170° C.
Claim 6
Dependent Claim
20 words
The process as claimed in claim 1, wherein the annealing treatment is effected at a temperature of approximately 500° C.
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) | 1982-04-02 | 1982-10-02 | 1983-04-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-04-02 | 1986-10-02 | 1987-04-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-04-02 | 1990-10-02 | 1991-04-03 | $7700.00 | Window Closed / Lapsed |