GB484037A - Method of producing dicalcium phosphate and calcium nitrate solution - Google Patents
Method of producing dicalcium phosphate and calcium nitrate solutionInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B11/00—Fertilisers 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
- C05B11/04—Fertilisers 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
- C05B11/06—Fertilisers 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.
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)
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 |
-
1937
- 1937-05-25 GB GB14518/37A patent/GB484037A/en not_active Expired
Cited By (4)
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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