PROCESS FOR THE PREPARATION OF CALCIUM PHOSPHATE GRANULES OF THE HYDROXYAPATITE TYPE
The objective of the present innovation is a new process for the preparation of calcium phosphate granules of the hydroxyapatite type. The preparation process of a business for the said granules based on the invention is a hydrolysis process of a brushite dicalcium phosphate, in a basic milieu which is characterised by the fact that an aqueous suspension of brushite dicalcium phosphate is treated with lime, in the presence of an effective quantity of a carboxylic acid.
1 . A process for preparation of a calcium phosphate in the form of granules displaying an X-ray diffraction pattern of hydroxyapatite by hydrolysis of a brushite dicalcium phosphate, in a basic milieu wherein an aqueous suspension of brushite dicalcium phosphate is treated with lime in the presence of an effective quantity of a carboxylic acid.
2 . Process according to claim 1 wherein the brushite calcium phosphate has a granulometric distribution such that 90% by weight of the particles are less than about 300 microns and that at least 90% by weight of the particles are larger than about 10 microns.
3 . Process according to claim 2 wherein the size of the brushite dicalcium phosphate particles is such that the median diameter (d 50 ) is between 100 μm and 250 μm, preferably between 150 μm and 190 μm.
4 . Process according to claim 1 wherein the aqueous suspension of brushite has a concentration between 20 and 40% by weight.
5 . Process according to claim 1 wherein the lime is in solid form or in the form of milk of lime with a concentration between 5 and 20 g/l, preferably 10 g/l.
6 . Process according to claim 1 wherein the quantity of lime used is such that the Ca/P ratio is between 1.5 and 1.7, preferably about 1.6.
7 . Process according to claim 1 wherein carboxylic acid used is a carboxylic acid whose calcium salt is soluble or partially soluble under the reaction conditions.
8 . Process according to claim 7 wherein the carboxylic acid is an aliphatic carboxylic acid with 1 to 7 carbon atoms and preferably 1 to 4 carbon atoms.
9 . Process according to claim 8 wherein the carboxylic acid is methanoic acid, acetic acid, or propionic acid, preferably acetic acid.
10 . Process according to claim 1 wherein the carboxylic acid is used in a manner to lower the pH of the reaction milieu to between 6 and 10, preferably about pH 7.0.
11 . Process according to claim 1 wherein the reaction temperature is between 50° C. and 100° C., preferably between 90° C. and 95° C.
12 . Process according to claim 1 wherein the reaction is carried out under atmospheric pressure.
13 . Process according to claim 1 wherein lime is introduced into the suspension of brushite dicalcium phosphate and the pH is adjusted to the above mentioned range by the introduction of carboxylic acid.
14 . Process according to claim 13 wherein the process is carried out in a discontinuous or continuous mode.
15 . Process according to claim 1 wherein the milieu is maintained at a reaction temperature for a period of time sufficient to obtain the transformation of brushite dicalcium phosphate into calcium phosphate hydroxyapatite.
16 . Process according to claim 1 wherein the calcium phosphate hydroxyapatite obtained is separated, preferably by filtration and that one or more water washings are carried out.
17 . Process according to claim 1 wherein the calcium phosphate hydroxyapatite is dried at a temperature between 80 and 120° C., preferably in the region of 110° C.
18 . Calcium phosphate in granular form displaying an X-ray diffraction pattern of hydroxyapatite obtained according to the process claim 1 .
19 . Phosphate according to claim 18 wherein it contains no anions or cations different from the composition of the hydroxyapatite.
20 . Utilisation of calcium phosphate hydroxyapatite in the granular form obtained according to the process described in claim 1 as sources of phosphorus and calcium and/or as excipients in tablets.