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US4017588A Expired / Lapsed US ⏱️ 0.0 years remaining

Manufacture of solid ammonium phosphate

Assignee: Scottish Agricultural Industries Ltd
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Filing: 1975-09-02
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Granted: 1977-04-12
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Expires: 1995-09-02
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Abstract

Abstract The invention relates to a process for the manufacture of solid monammonium phosphate with good granulation properties suitable for use in compound fertiliser manufacture. An improvement in product quality is obtained when between 20% and 80% of an aqueous slurry of ammonium phosphate, formed by the ammoniation of wet-process phosphoric acid, is mixed with a second acid prior to entry into a moisture disengagement unit. This treatment precipitates some monammonium phosphate crystals which provide nuclei for further crystal growth. After a short time delay to allow crystals to form, the remainder of the slurry is then added separately to the moisture disengagement unit.

Inventors

  • 👤 Eric Davidson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-10 01:34
CPC Classifications
C; C05; C05B; C05B7/00

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 215 words
A process for the production of a particulate solid product comprising ammonium phosphate of N:P atomic ratio 0.95 to 1.05 wherein a primary phosphoric acid-containing feed and ammonia are added to an aqueous slurry of ammonium phosphate of flowable consistency at the temperature of working and having an N:P atomic ratio of between 1.3 and 1.5 to form more slurry of substantially the same composition and concentration and flowable consistency, removing an amount of said slurry substantially equivalent to that produced by the addition of the phosphoric acid and ammonia and thereafter mixing the removed slurry with a secondary acid feed to reduce the N:P ratio to 0.95 to 1.05, wherein between 20% and 80% by volume of the removed slurry is mixed with the secondary acid feed, followed by the addition to the mixture of the remainder of the slurry, so that the ammonium phosphate of the resulting product has an N:P atomic ratio in the range 0.95 to 1.05, the water contents of the removed aqueous slurry and the secondary acid feed being such that the resulting product starts to solidify in a moisture disengagement unit where it is treated for a sufficient period of time for said product to be solid at ambient temperature whereby extra milling of the product is avoided.
Claim 2
Dependent Claim 215 words
A process for the production of a particulate solid product comprising ammonium phosphate of N:P atomic ratio 0.95 to 1.05 wherein a primary phosphoric acid-containing feed and ammonia are added to an aqueous slurry of ammonium phosphate of flowable consistency at the temperature of working and having an N:P atomic ratio of between 1.3 and 1.5 to form more slurry of substantially the same composition and concentration and flowable consistency, removing an amount of said slurry substantially equivalent to that produced by the addition of the phosphoric acid and ammonia and thereafter mixing the removed slurry with a secondary acid feed to reduce the N:P ratio to 0.95 to 1.05, wherein between 20% and 80% by volume of the removed slurry is mixed with the secondary acid feed, followed by the addition to the mixture of the remainder of the slurry, so that the ammonium phosphate of the resulting product has an N:P atomic ratio in the range 0.95 to 1.05, the water contents of the removed aqueous slurry and the secondary acid feed being such that the resulting product starts to solidify in a moisture disengagement unit where it is treated for a sufficient period of time for said product to be solid at ambient temperature whereby extra milling of the product is avoided.
Claim 3
Dependent Claim 16 words
A process as claimed in claim 1, wherein the primary acid feed is wet-process phosphoric acid.
Claim 4
Dependent Claim 31 words
A process as claimed in claim 1, wherein the secondary acid feed is a mineral acid selected from the group consisting of phosphoric acid, nitric acid, sulphuric acid and mixtures thereof.
Claim 5
Dependent Claim 15 words
A process as claimed in claim 3, wherien the phosphoric acid is wet-process phosphoric acid.
Claim 6
Dependent Claim 15 words
A process as claimed in claim 1, wherein the secondary acid feed is partially ammoniated.
Claim 7
Dependent Claim 39 words
A process as claimed in claim 1, wherein a nitrogen compound, selected from the group consisting of ammonium salts, urea, and mixtures thereof, is added to the removed slurry during or following the addition of the secondary acid feed.
Claim 8
Dependent Claim 27 words
A process as claimed in claim 1, wherein a potassium compound is added to the removed slurry during or following the addition of the secondary acid feed.
Claim 9
Dependent Claim 19 words
A process as claimed in claim 1, wherein a part of the solid end-product is recycled to the process.
Claim 10
Dependent Claim 192 words
A process for producing a particulate solid product comprising ammonium phosphate of N:P atomic ratio in the range 0.95 to 1.05 is performed by mixing wet-process phosphoric acid of P 2 O 5 content in the range 30% to 54% P 2 O 5 and gaseous ammonia to form an aqueous slurry of ammonium phosphate, the N:P atomic ratio of the slurry being fixed in the range 1.3 to 1.5 and the moisture content of the slurry being fixed in the range 10% to 20%, in such proportions as to form more slurry of substantially the same composition, simultaneously removing from the slurry an amount substantially eqivalent to that produced from the phosphoric acid and ammonia, and mixing 20% to 80% by volume of the removed amount of slurry with further wet-process phosphoric acid, thereafter adding the remainder of the slurry, whereby the product so formed solidifies and is of the desired N:P atomic ratio, the moisture disengagement being carried out under such conditions that the moisture content of the product is so reduced by evaporation that the product is solid at ambient temperature whereby extra milling of the product is avoided.
Claim 11
Dependent Claim 192 words
A process for producing a particulate solid product comprising ammonium phosphate of N:P atomic ratio in the range 0.95 to 1.05 is performed by mixing wet-process phosphoric acid of P 2 O 5 content in the range 30% to 54% P 2 O 5 and gaseous ammonia to form an aqueous slurry of ammonium phosphate, the N:P atomic ratio of the slurry being fixed in the range 1.3 to 1.5 and the moisture content of the slurry being fixed in the range 10% to 20%, in such proportions as to form more slurry of substantially the same composition, simultaneously removing from the slurry an amount substantially eqivalent to that produced from the phosphoric acid and ammonia, and mixing 20% to 80% by volume of the removed amount of slurry with further wet-process phosphoric acid, thereafter adding the remainder of the slurry, whereby the product so formed solidifies and is of the desired N:P atomic ratio, the moisture disengagement being carried out under such conditions that the moisture content of the product is so reduced by evaporation that the product is solid at ambient temperature whereby extra milling of the product is avoided.

References Cited (Backward Citations)

US3226184A Cited
US3313614A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-04-11 1980-10-11 1981-04-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-04-11 1984-10-11 1985-04-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-04-11 1988-10-11 1989-04-12 $7700.00 Window Closed / Lapsed

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