United States Patent (19) (11) 4,411,876 Sherif 45) Oct
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United States Patent (19) (11) 4,411,876 Sherif 45) Oct. 25, 1983 54 PROCESS FOR THE MANUFACTURE OF 636182 12/1978 U.S.S.R. .............................. 423A311 TRIMAGNESUM PHOSPHATE OCTAHYDRATE OF HIGH PURTY OTHER PUBLICATIONS Bhaunagary et al., "Preparation of Tricalcium Phos phate by Hydrolysis of Dicalcium Phosphate with Cal (75) Inventor: Fawzy G. Sherif, Stony Point, N.Y. cium Hydroxide", J. Appl. Chem. Biotechnol., (1977), (73) Assignee: Stauffer Chemical Company, 27, 393-398. Westport, Conn. Chemical Abstracts, 81 (12), 71959c. 21 Appl. No.: 454,395 Chemical Abstracts, 78(22) 138447t. Primary Examiner-Edward J. Meros 22 Filed: Dec. 30, 1982 Assistant Examiner-Wayne A. Langel (51) Int. Cl. .............................................. CO1B 25/26 Attorney, Agent, or Firm-Vivienne T. White 52) U.S. Cl. .................................................... 423/311 (58) Field of Search ................................ 423/308, 311 57 ABSTRACT The invention is the production of crystalline tertiary 56) References Cited magnesium phosphate octahydrate having uniform and U.S. PATENT DOCUMENTS perfect crystal shape. The process comprises adding a 991,096 5/1911 Schrödter ........................... 423/31 monomagnesium phosphate solution to a magnesium 2,095,994 10/1937 MacIntire ...... ... 42.331 hydroxide slurry at a sufficient temperature and for a 3,194,632 7/1965 Baniel et al. ........................ 423/311 sufficient time to form the highly pure crystalline prod uct within a specified pH range. FOREIGN PATENT DOCUMENTS 44-4649 2/1969 Japan ................................... 423.31 9 Claims, No Drawings 4,411,876 1 2 phate compatibility of various samples of dicalcium PROCESS FOR THE MANUFACTURE OF phosphate dihydrate, TRIMAGNESUM PHOSPHATE The prior art teaches that dicalcium phosphate dihy OCTAHYDRATE OF HIGH PURITY drate may be stabilized by adding a small amount of an alkali metal pyrophosphate or tertiary magnesium phos BACKGROUND OF THE INVENTION phate to the mother liquor, at a controlled pH, during the preparation of the dicalcium phosphate. Specifi 1. Field of the Invention cally, it is taught that after precipitation of the dical The invention relates to a process for the production cium phosphate in the mother liquor, a small amount of of tertiary magnesium phosphate octahydrate and in O alkali metal pyrophosphate or tertiary magnesium phos particular to a process for the production of highly pure phate should be added and the entire slurry then heated crystalline tertiary magnesium phosphate octahydrate. for a short period of time, while maintaining the pH of 2. Related Art the mother liquor above 7. It is known to use tertiary magnesium phosphate The alkali metal pyrophosphate or tertiary magne (a/k/a tribasic magnesium, phosphate or trimagnesium 5 sium phosphate coats the surface of the dicalcium phos phosphate), or an alkali metal pyrophosphate as a stabi phate such that the coating significantly eliminates the lizer for dibasic calcium phosphate. reaction of the dicalcium phosphate with the mono It is well known that hardness and particle shape fluorophosphate thereby resulting in a dicalcium phos make dibasic calcium phosphate suitable for use as a phate which remains in the water soluble state. base for dentifrices. The required properties of a base The effect of tertiary magnesium phosphate as a stabi for a toothpaste are that, even when kept in the tube for lizer for dibasic calcium phosphate varies greatly with a long time, it does not harden, remains homogeneous, the method used for its production. does not form a coagulated mass, and does not separate Tertiary magnesium phosphate containing 0, 4, 8, and into a liquid and solid phase. However, the dihydrate of 22 molecules of water of crystallization has so far been dibasic calcium phosphate, when used as a base for a 25 reported, but only the octahydrate is used as a stabilizer toothpaste is so unstable that it often tends to harden, for dicalcium phosphate. It is also known to use tribasic coagulate, causing the toothpaste to separate into a magnesium phosphate as a fertilizer because of its high liquid and a solid phase. The water of crystallization of P2O5 content, and as an antacid. It has also been dis dibasic calcium phosphate is normally thermally unsta closed to use tribasic magnesium phosphate as a water ble and tends to evaporate readily when the compound 30 insoluble neutralizing agent in the growing of acid pro is allowed to stand in dry air at room temperature, leav ducing bacteria cultures. ing the anhydrous salt behind. The known production methods for the octahydrate With the advent of the use of monofluorophosphate include one in which an aqueous solution of magnesium additives in toothpaste formulations another problem sulfate and dibasic sodium phosphate is made weakly was encountered. It was found that the monofluoro alkaline with sodium bicarbonate and is then allowed to phosphate components would react with the dicalcium stand. Another method is one in which dibasic magne phosphate whereby the monofluorophosphate compo sium phosphate is boiled for a long time in a large quan nent was converted from a water/soluble form to a tity of water. water insoluble form. Since the beneficial effect of It has been disclosed to produce Mg3(PO4)2.8H2O by 40 the dehydration of Mg2(PO4)2.22H2O or by the hydro monofluorophosphate additives in toothpaste is under lysis of Mg2HPO4.3H2O. stood to be derived principally from the water-soluble It has also been disclosed to produce Mg3(PO4)2.8- form, it has become important to develop toothpaste H2O by reacting orthophosphoric acid, added drop formulations which permit an effective amount of wise, to magnesium oxide powder or magnesium hy monofluorophosphate component to remain in the 45 droxide powder with energetic stirring; see Japanese water-soluble state, Patent Application No. 39-57557/1964. This order of The term "monofluorophosphate compatibility' has addition, i.e., the acid to the base, is disclosed to be been used as a term-of-art to describe the tendency of necessary to produce the trimagnesium but not the such formulations to permit the monofluorophosphate dimagnesium phosphate. However, it is common to component to remain in the water soluble state. SO produce trimagnesium phosphate by this method, The monofluorophosphate compatibility of a particu which product is contaminated with unreacted lar formulation may be determined by a variety of meth Mg(OH)2 or with dimagnesium phosphate. These unde ods. Preferably, the monofluorophosphate compatibil sired components lead to caking. They may also alter ity of a formulation is determined by actually preparing the functional properties of the trimagnesium phos the toothpaste formulation, comprising a fluoride stabi- ss phate. Furthermore, the addition of the very strong acid lizer, placing it in storage for a predetermined period of to Mg(OH)2 has to occur at a very slow rate, otherwise time under controlled conditions, and then determining the pH falls very quickly forming the dimagnesium the amount of water-soluble monofluorophosphate phosphate. Therefore, this process takes several hours, which remains in the formulation. Alternatively, a sinnu normally 10-14 hours, to complete. lated formulation, such as the dicalcium phosphate di hydrate to be tested, glycerine, a known amount of a SUMMARY OF THE INVENTION monofluorophosphate component, such as sodium A novel process of producing trimagnesium phos monofluorophosphate and a stabilizer can be "quick phate octahydrate has been discovered which produces aged' by maintaining it at an elevated temperature for Mg3(PO4)2.8H2O crystals having good crystal shapes. one or more hours, and then determining the amount of 65 The process of the invention comprises the reaction of water-soluble monofluorophosphate remaining after monobasic monomagnesium phosphate with magne such conditioning. There are, of course, many other sium hydroxide at a temperature of from about 35 C. to methods for measuring the relative monofluorophos about 70° C. for a period of hours wherein the pH is 4,411,876 3 4. maintained at from about 6.7 to about 6.9 during the A terminal pH of from about 6.7 to about 6.9 for the process and the process pH is preferably 6.8. reaction slurry is generally acceptable with a pH of 6.8 being particularly desirable. At lower a pH of 4 or 6, for DETALED DESCRIPTION OF THE example, dimagnesium phosphate is formed instead of INVENTION trimagnesium phosphate. At higher a pH free untreated The invention is a process of producing highly pure Mg(OH)2 remains in the product. trimagnesium phosphate. The monomagnesium phosphate solution is generally Broadly the invention comprises the preparation of a added to the slurry over a period of time sufficient to monomagnesium phosphate solution followed by the complete the reaction and produce the pure trimagne addition of the monomagnesium phosphate solution to a 10 sium phosphate octahydrate product. A total reaction magnesium hydroxide slurry wherein the temperature time of from 5 to 7 hours is generally required. After the of the slurry is maintained at from about 35 to about 70 reaction is completed, the white solid product is filtered C. and preferably from about 40' to about 50 C. from the mother liquor. The reactions are thought to be as follows: Mg(OH)2 In practicing the invention it is desirable to use a and excess H3PO4 are mixed together to produce the 15 monomagnesium phosphate solution having as high a following: concentration of Mg and H3PO4 as possible to reduce the amount of filtrate recycled in the commercial pro cess and therefore reduce cost. At lower concentrations of Mg and H3PO4, the ratio of the filtered product to The clear slightly acidic monomagnesium phosphate the mother liquor will be too small, requiring larger solution produced has a pH of about 3 to about 3.5. It is equipment in handling of the filtrate. This is not eco then added to a slurry of Mg(OH)2 as shown.