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US4153441A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for making magnesium potassium ammonium phosphate

Assignee: Sumitomo Corp
•
Filing: 1978-08-01
•
Granted: 1979-05-08
•
Expires: 1998-08-01
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Abstract

Abstract Process for making magnesium potassium ammonium phosphate, using ammonia, urea, potassium hydroxide, magnesium hydroxide, and phosphoric acid with specified maxima of iron, alumina, and sulfate.

Inventors

  • 👤 William L. Guithues
  • 👤 Casimer C. Legal, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 22:43
CPC Classifications
C; C05; C05B; C05B9/00

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 140 words
In the method of making magnesium potassium ammonium phosphate having a water soluble nitrogen of not more than 2% by the steps of (a) preparing an aqueous reaction slurry by reacting together phosphoric acid of 40-61% P 2 O 5 , ammonia, urea, potassium hydroxide, and magnesium hydroxide in a reactor-granulating zone, thereby to form granules; (b) screening the said granules to give granulated product and fines; (c) recycling the fines from (b) to the granulating zone in (a); the improvement comprising using, as the phosphoric acid reactant, phosphoric acid which is not furnace grade, but has the following analysis (basis, 60% P 2 O 5 ): So 4 (as H 2 SO 4 ) not more than about 3% Fe 2 O 3 , not more than about 0.5% Al 2 O 3 , not more than about 0.3%.
Claim 2
Dependent Claim 140 words
In the method of making magnesium potassium ammonium phosphate having a water soluble nitrogen of not more than 2% by the steps of (a) preparing an aqueous reaction slurry by reacting together phosphoric acid of 40-61% P 2 O 5 , ammonia, urea, potassium hydroxide, and magnesium hydroxide in a reactor-granulating zone, thereby to form granules; (b) screening the said granules to give granulated product and fines; (c) recycling the fines from (b) to the granulating zone in (a); the improvement comprising using, as the phosphoric acid reactant, phosphoric acid which is not furnace grade, but has the following analysis (basis, 60% P 2 O 5 ): So 4 (as H 2 SO 4 ) not more than about 3% Fe 2 O 3 , not more than about 0.5% Al 2 O 3 , not more than about 0.3%.
Claim 3
Dependent Claim 39 words
Method according to claim 1 in which the phosphoric acid has the following analysis: ______________________________________ % ______________________________________ H.sub.2 O 14.3-16.0 P.sub.2 O.sub.5 59.0-61.0 Fe.sub.2 O.sub.3 0.3-0.5 Al.sub.2 O.sub.3 0.1-0.3 F 0.2-0.4 H.sub.2 SO.sub.4 1.5-3.0 MgO 0.3-1.0 Solids 0.1-0.5. ______________________________________

References Cited (Backward Citations)

US3125411A Cited
US3126254A Cited
US3141732A Cited
US3285731A Cited
US3320048A Cited
US3476510A Cited
US3490892A Cited
DE1924284A1 Cited
JPS478974U Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-05-07 1982-11-06 1983-05-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-05-07 1986-11-06 1987-05-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-05-07 1990-11-06 1991-05-08 $7700.00 Window Closed / Lapsed

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