Production of dicalcium phosphate or monocalcium phosphate
OwnerJan Christoffel De Waalinventor
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OwnerJan Christoffel De Waalinventor
Estimating the term…
A process is provided for the production of dicalcium phosphate form a phosphate source material in which a solution of phosphoric acid is produced by the action of a suitable mineral acid, generally sulphuric acid, on a phosphate source material. Calcium fluoride is precipitated at a pH of between 3,5 and 4,5 followed by hydrolysing the solution by diluting it with water to a ratio of approximately 1:7 to about 1:10 monocalcium phosphate to water at a temperature of approximately 40 degrees Centigrade to form a primary precipitate containing substantially all of the fluoride present as CaF2 together with some dicalcium phosphate and a primary calcium and phosphate containing solution. The primary precipitate is dissolved, the pH adjusted to form 3,5 to 4,5 and the hydrolyzation repeated to form a secondary precipitate containing substantially all of the fluoride present as CaF2 together with some dicalcium phosphate and a secondary calcium and phosphate containing solution. The secondary precipitate can optionally, if required, by again processed in the same way to recover more phosphates. The product dicalcium phosphate is recovered from the combined calcium and phosphate containing solutions.
A process for the production of dicalcium phosphate from a phosphate source material comprising the steps of:
A process as claimed in any one of the preceding claims in which the alkaline calcium material used in step iii is calcium carbonate.
A process as claimed in any one of the preceding claims in which the pH referred to in step iii is about 4,0.
A process as claimed in any one of the preceding claims in which the ratio referred to in step iv is about 1:7,5.
A process as claimed in any one of the preceding claims in which the temperature of the water in step iv is about 40 degrees Centigrade.
A process as claimed in any one of the preceding claims in which the dissolution of step vi and, where applicable step vii, is effected using a portion of the phosphoric acid produced in step i.
A process as claimed in any one of the preceding claims in which the pH in step viii is firstly adjusted to about 4,0 to precipitate residual fluoride together with a small amount of dicalcium phosphate which is optionally recycled to the neutralisation of step iii followed by further neutralisation to a pH of about 4 using calcium carbonate and thereafter using hydroxide to a pH of about 7,0.
A process as claimed in any one of the preceding claims in which the calcium fluoride present in the final precipitate formed in step vi or vii is recovered as a byproduct.
A process as claimed in any one of the preceding claims in which the product dicalcium phosphate is converted to monocalcium phosphate.
A process substantially as herein and exemplified with reference to the accompanying drawing.
Dependencies are inferred from the claim text.