GB484037A - Method of producing dicalcium phosphate and calcium nitrate solution - Google Patents

Method of producing dicalcium phosphate and calcium nitrate solution

Info

Publication number
GB484037A
GB484037A GB14518/37A GB1451837A GB484037A GB 484037 A GB484037 A GB 484037A GB 14518/37 A GB14518/37 A GB 14518/37A GB 1451837 A GB1451837 A GB 1451837A GB 484037 A GB484037 A GB 484037A
Authority
GB
United Kingdom
Prior art keywords
solution
dicalcium phosphate
limestone
lime
calcium nitrate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB14518/37A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KUNSTDUENGER PATENT VERWERTUNG
Original Assignee
KUNSTDUENGER PATENT VERWERTUNG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by KUNSTDUENGER PATENT VERWERTUNG filed Critical KUNSTDUENGER PATENT VERWERTUNG
Publication of GB484037A publication Critical patent/GB484037A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05BPHOSPHATIC FERTILISERS
    • C05B11/00Fertilisers produced by wet-treating or leaching raw materials either with acids in such amounts and concentrations as to yield solutions followed by neutralisation, or with alkaline lyes
    • C05B11/04Fertilisers produced by wet-treating or leaching raw materials either with acids in such amounts and concentrations as to yield solutions followed by neutralisation, or with alkaline lyes using mineral acid
    • C05B11/06Fertilisers produced by wet-treating or leaching raw materials either with acids in such amounts and concentrations as to yield solutions followed by neutralisation, or with alkaline lyes using mineral acid using nitric acid (nitrophosphates)

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

In the production of dicalcium phosphate and calcium nitrate solution by dissolving phosphate rock in nitric acid and neutralizing the solution by lime or limestone, the addition of the neutralizing agent is regulated so that the dissolved iron and aluminium are to an essential part precipitated from the solution before precipitation of the dicalcium phosphate occurs, this latter being effected by continued addition of the neutralizing agent. Easily filterable crystals of dicalcium phosphate are thereby obtained. Unless a pure product is required, the iron and aluminium precipitate need not be removed prior to the precipitation of the dicalcium phosphate. The solution to be neutralized should have a free P205 content not exceeding 8 grms. per 100 cc., and preferably below 7 grms. per 100 cc. solution, the concentration being adjusted by adding calcium nitrate solution and/or water at or after the dissolving of the rock. The first stage of the neutralization should be effected by supplying the acid solution and lime or limestone simultaneously to a reaction vessel. After the first stage, the free P2O5 content should be at least 1 grm. per 100 cc. Small portions of lime or limestone are then supplied to batches of the partly neutralized solution until the remaining impurities are precipitated, whereupon the addition of the neutralizing agent may be accelerated to precipitate dicalcium phosphate. The ratio of H2SiF6 to Al2O3 should be from 2 : 1 to 3 : 1. If the ratio is too low, a fluor compound is added on or after dissolving the rock; if too high, a complex salt containing aluminium and fluorine is precipitated from the solution according to the method disclosed in Specification 467,843. Reaction is conveniently effected at 30-35 DEG C., a temperature up to 40 DEG C. being however permissible at the beginning. The limestone used is preferably mixed with calcium nitrate solution. The last precipitation may be made with lime or ammonia if the limestone is not sufficiently finely ground. Four examples are given, one demonstrating that small needle-shaped badly-separating crystals of dicalcium phosphate are obtained when the first neutralizing stage is carried so far that the solution then contains less than 1 grm. free P2O5 per 100 cc. solution.
GB14518/37A 1936-06-13 1937-05-25 Method of producing dicalcium phosphate and calcium nitrate solution Expired GB484037A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE484037X 1936-06-13

Publications (1)

Publication Number Publication Date
GB484037A true GB484037A (en) 1938-04-29

Family

ID=20310512

Family Applications (1)

Application Number Title Priority Date Filing Date
GB14518/37A Expired GB484037A (en) 1936-06-13 1937-05-25 Method of producing dicalcium phosphate and calcium nitrate solution

Country Status (1)

Country Link
GB (1) GB484037A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1122557B (en) * 1959-05-28 1962-01-25 Wolfen Filmfab Veb Device for the continuous production of dicalcium phosphate
US3391993A (en) * 1965-03-18 1968-07-09 Diamond Shamrock Corp Method for preparing feed grade dicalcium phosphate
US4039624A (en) * 1974-07-30 1977-08-02 National Process Industries (Proprietary) Limited Method of producing phosphoric acid from high iron and aluminum content phosphate rocks using nitric acid
US4088738A (en) * 1975-11-24 1978-05-09 United States Gypsum Company Process for producing phosphoric acid using mixed acid feed and a dicalcium phosphate intermediate

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1122557B (en) * 1959-05-28 1962-01-25 Wolfen Filmfab Veb Device for the continuous production of dicalcium phosphate
US3391993A (en) * 1965-03-18 1968-07-09 Diamond Shamrock Corp Method for preparing feed grade dicalcium phosphate
US4039624A (en) * 1974-07-30 1977-08-02 National Process Industries (Proprietary) Limited Method of producing phosphoric acid from high iron and aluminum content phosphate rocks using nitric acid
US4088738A (en) * 1975-11-24 1978-05-09 United States Gypsum Company Process for producing phosphoric acid using mixed acid feed and a dicalcium phosphate intermediate

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