JPH01203206A - Production of octacalcium phosphate - Google Patents

Production of octacalcium phosphate

Info

Publication number
JPH01203206A
JPH01203206A JP2667788A JP2667788A JPH01203206A JP H01203206 A JPH01203206 A JP H01203206A JP 2667788 A JP2667788 A JP 2667788A JP 2667788 A JP2667788 A JP 2667788A JP H01203206 A JPH01203206 A JP H01203206A
Authority
JP
Japan
Prior art keywords
water
ocp
phosphoric acid
soln
salt
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.)
Granted
Application number
JP2667788A
Other languages
Japanese (ja)
Other versions
JP2584267B2 (en
Inventor
Seikichi Tabei
田部井 清吉
Mitsuharu Mori
森 充玄
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.)
Nippon Chemical Industrial Co Ltd
Original Assignee
Nippon Chemical Industrial Co Ltd
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 Nippon Chemical Industrial Co Ltd filed Critical Nippon Chemical Industrial Co Ltd
Priority to JP63026677A priority Critical patent/JP2584267B2/en
Publication of JPH01203206A publication Critical patent/JPH01203206A/en
Application granted granted Critical
Publication of JP2584267B2 publication Critical patent/JP2584267B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/32Phosphates of magnesium, calcium, strontium, or barium
    • C01B25/322Preparation by neutralisation of orthophosphoric acid

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To produce a large quantity of octacalcium phosphate (OCP) at a time by a simple process, by mixing and reacting phosphoric acid, water-soluble Ca salt and one or more kinds of carbonate salt and bicarbonate salt of Na, K and NH4 in a specified pH range. CONSTITUTION:An aq. soln. as A, lig., is prepd. by preferably dissolving phosphoric acid and a aq. soln. of water-soluble Ca such as CaCl2. On the other hand, an aq. soln., as B, liq., of carbonate, etc. of Na, etc., (Na2CO3), is prepd. The A) and B) liqs. are mixed and reacted at 20-100 deg.C preferably for about 0.5-4hr while keeping the pH value at 4-7. Then, after the reaction, the product is aged, thereafter separated and washed in an usual manner, filtered and dried to obtain OCP. The confirmation of OCP can be carried out by an X-ray diffraction method.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、オクタカルシウムホスフェートの〈以下rO
cPJ )の新規な製造法に関する。
Detailed Description of the Invention <Industrial Application Field> The present invention provides octacalcium phosphate (rO
cPJ).

〈従来の技術〉 従来より知られているOCPの製造法は以下の通りであ
る。
<Prior Art> Conventionally known methods for producing OCP are as follows.

■極稀薄なH3PO4−NaOH溶液(燐酸濃度51I
lof、 pH= 7.5)にCaCl2を加えて約4
0℃で24時間反応熟成させて青る方法■極稀薄なCa
b−P205−H2o余水溶液。
■Extremely dilute H3PO4-NaOH solution (phosphoric acid concentration 51I)
lof, pH = 7.5) with CaCl2 to approx.
How to turn blue by reacting and aging at 0℃ for 24 hours■Ultra dilute Ca
b-P205-H2o residual water solution.

(Ca1度0.4〜4m mof、P濃度0.8〜10
11I101)にアルカリを滴下して得られたものを回
収する方法。
(Ca1 degree 0.4~4m mof, P concentration 0.8~10
A method of dropping an alkali onto 11I101) and collecting the resulting product.

■0.048− Ca (No  >  と00.3+
4−N 82 HPO4をpl−16,5〜 6.6の
 0.28−CH3C0ONa中に同時に添加し、50
〜60℃で数時間熟成して得る方法。
■0.048- Ca (No > and 00.3+
4-N 82 HPO4 was added simultaneously into 0.28-CH3COONa at pl-16,5~6.6, and 50
A method of aging at ~60°C for several hours.

■CaHPO・21−1 0を0.58−CH3c。■CaHPO・21-1 0 to 0.58-CH3c.

ONa中でpH<6.1の条件で加水分解して得る方法
A method of obtaining by hydrolysis in ONa under conditions of pH < 6.1.

■Ca  (PO4)2をD He付近で加水分解して
得る方法。
■A method of obtaining Ca (PO4)2 by hydrolyzing it near D He.

〈発明が解決しようとする問題点〉 しかしながら、上記■、■の方法は、大量の水処理、大
量生産からみた問題があり、■、■の方法は排水処理の
問題や原料コストの問題及び■の方法は、容易にOCP
への転換が難しく単一相として製造するのは問題があり
、上記の方法はいずれも、−度に多量のOCPを製造す
ることはできず、工業的な製造法としては欠点がありて
、今日まで確立した工業的製法は皆無であった。
<Problems to be solved by the invention> However, the above methods (1) and (2) have problems from the perspective of large amounts of water treatment and mass production; The method of OCP
It is difficult to convert to OCP and producing it as a single phase is problematic, and all of the above methods cannot produce a large amount of OCP at once, and have drawbacks as an industrial production method. Until now, no industrial manufacturing method has been established.

そこで、本発明者は、Na等の炭酸塩、虫炭M塩を用い
て反応系のpHを5前後に保つと反応が容易に進み、−
度に多量のOCRを製造すφことができることを知見し
本発明を得た。
Therefore, the present inventor found that if the pH of the reaction system was maintained at around 5 using carbonate such as Na or insect charcoal M salt, the reaction would proceed easily and -
The present invention was achieved by discovering that it is possible to manufacture a large amount of OCR at a time.

く問題点を解決するための手段〉 即ち本発明は、リン酸、水溶性カルシウム塩及びNa、
に、NH4の炭酸塩、重炭酸塩(以下rNa等の炭酸塩
等」)から選ばれた1種以上を、pI−14〜7で混合
して反応させることを特徴とするOCPの製造法である
Means for Solving the Problems〉 That is, the present invention solves the following problems: phosphoric acid, water-soluble calcium salt and Na,
A method for producing OCP, which is characterized in that one or more selected from carbonates and bicarbonates of NH4 (hereinafter referred to as "carbonates of rNa etc.") are mixed and reacted at a pI of -14 to 7. be.

ここで、OCRとはCa  H(PO4)6−5.82
0の組成を有し、Ca/P=1.33のちのである。
Here, OCR is CaH(PO4)6-5.82
It has a composition of 0 and Ca/P=1.33.

本発明に係る水溶性カルシウム塩としては、CaCl 
 、Ca (NO3)2、 (CH3COO)2Ca等が挙げられる。
The water-soluble calcium salt according to the present invention includes CaCl
, Ca (NO3)2, (CH3COO)2Ca, and the like.

又、本発明に係るNa等の炭i![!塩等としては、N
a2 CO3、NaHCO3、K2 CO3、KHCO
、(NH)  Co  、(NH4)HCO3が挙げら
れる。
Moreover, charcoal i! such as Na according to the present invention! [! As salt etc., N
a2 CO3, NaHCO3, K2 CO3, KHCO
, (NH) Co , and (NH4)HCO3.

本発明は、リン酸、水溶性カルシウム及びNa等の炭M
馬等を混合して反応させるのであるが、上記の原料の混
合の順序は特に制限はない。しかしながら、多くの場合
リン酸及び水溶性カルシウム塩を水に溶して水溶液とし
たものをA液とし、Na等の炭酸塩等の水溶液をB液と
なし、脱塩水あるいは予め用意しておいたNaCjを含
んだ生成母液にA液とB液を同時に添加するのが好適で
ある。
The present invention utilizes phosphoric acid, water-soluble calcium, and carbon M such as Na.
The reaction is carried out by mixing the raw materials, but there is no particular restriction on the order in which the above raw materials are mixed. However, in many cases, phosphoric acid and water-soluble calcium salts are dissolved in water to make an aqueous solution, which is called solution A, and an aqueous solution of carbonates such as Na is used as solution B, and desalinated water or prepared in advance is used. It is preferable to add liquid A and liquid B simultaneously to the produced mother liquor containing NaCj.

なお、A液におけるリン酸と水溶性カルシウム塩の所用
量は、最終製品であるOCPの理論量のCa/P= 1
.33又は、その前後の割合であり、A液はかかる組成
の混合溶液として調製されたものである。
In addition, the amount of phosphoric acid and water-soluble calcium salt required in liquid A is calculated based on the theoretical amount of OCP, which is the final product, Ca/P = 1
.. 33 or around it, and Solution A was prepared as a mixed solution with such a composition.

その理由は、リン酸と水溶性カルシウム塩を混合するこ
とによって、まず、CaとPが完全に均一に混合され、
これをNa等の炭M塩等によって中和すると部分的にp
Hが極端に高くなる事を防げるので、OCPが生成しや
すくなると考えられる。
The reason is that by mixing phosphoric acid and water-soluble calcium salt, Ca and P are mixed completely and uniformly.
When this is neutralized with charcoal M salts such as Na, some p
It is thought that since H can be prevented from becoming extremely high, OCP is more likely to be generated.

この時、混合液のpHを4〜7に保つことが重要である
At this time, it is important to maintain the pH of the mixture at 4 to 7.

その理由は、pH7以上ではヒドロキシアパタイトが生
成されてしまうためであり、又、1)H4以下ではCa
HPO−21−120等が生成するからである。
The reason for this is that hydroxyapatite is produced at pH 7 or higher, and 1) at pH 7 or lower, Ca
This is because HPO-21-120 and the like are generated.

本発明において、A液及びB液の添加時間は特に限定は
ないが、反応温度は20〜100℃が好ましい。
In the present invention, the addition time of liquid A and liquid B is not particularly limited, but the reaction temperature is preferably 20 to 100°C.

その理由は、20℃より低いときには冷Wが必要となる
ばかりか、生成物がゲル状となり取り扱いが困難となり
100℃を越えるとハイドロキシアパタイトが生成し易
くなる為である。
The reason for this is that when the temperature is lower than 20°C, not only cold W is required, but also the product becomes gel-like and difficult to handle, and when the temperature exceeds 100°C, hydroxyapatite is likely to be formed.

また、反応時間は、添加量、添加時間等に関連してくる
が、一般に0.5〜4時間位が好ましい。
The reaction time is related to the amount added, the addition time, etc., but is generally preferably about 0.5 to 4 hours.

次いで、反応終了後は、生成物を熟成した後、常法によ
り分離、水洗等を行ない濾過乾燥してOCRを青る。
After the reaction is completed, the product is aged, separated, washed with water, filtered and dried in a conventional manner to make the OCR blue.

OCRの確認はX線回折図により行なうことができる。OCR can be confirmed by X-ray diffraction diagram.

〈実施例〉 実施例1 85%リン!72gとCaCI  ・2H20122,
4gを水に溶して0.6.I!としてものをA液とする
<Example> Example 1 85% phosphorus! 72g and CaCI ・2H20122,
Dissolve 4g in water and make 0.6. I! Let this be liquid A.

NaHCO3140gを水に溶して1.2Jlとしたも
のをB液とする。
Solution B was prepared by dissolving 140 g of NaHCO3 in water to make 1.2 Jl.

2Jビーカーに脱塩水 1Jを入れ、NaC,954g
を溶解して温度を65℃にする。
Put 1J of demineralized water in a 2J beaker and add 954g of NaC.
Dissolve and bring the temperature to 65°C.

このNaC+溶液中にA液を5時間かけて滴下し、同時
にB液で1)H=5.0を維持する。A液の滴下終了時
のB液の残分は29dであった。
Solution A is dropped into this NaC+ solution over 5 hours, and at the same time, 1) H=5.0 is maintained with solution B. The remaining amount of B solution at the end of dropping A solution was 29 d.

滴下終了後15分間熟成したのち生成物を濾過乾燥した
After the addition was completed, the product was aged for 15 minutes and then filtered and dried.

生成物のX@回折図はOCPの単一相を示し、又、Ca
/P(−Eル比) ハ1.33 テアツl’:。
The X@ diffractogram of the product shows a single phase of OCP and also Ca
/P (-E ratio) H1.33 T':.

実施例2 85%リン酸72gとCaC1−2H20122,4g
を水に溶して0.6.gとしてものをA液とする。
Example 2 72g of 85% phosphoric acid and 4g of CaCl-2H20122.
Dissolve 0.6 in water. Let g be the liquid A.

Na2CO388gを水に溶して1.21としたものを
B液とする。
Solution B was prepared by dissolving 388 g of Na2CO in water to a concentration of 1.21.

2.1!ビーカーに脱塩水IJを入れ温度65℃にする
2.1! Pour demineralized water IJ into a beaker and bring the temperature to 65°C.

この液中にA液を5時間かけて滴下し、同時にB液でp
H=5を維持する。
Add liquid A dropwise into this liquid over 5 hours, and at the same time add liquid B to p.
Maintain H=5.

滴下終了後15分間熟成したのち生成物を濾過乾燥した
After the addition was completed, the product was aged for 15 minutes and then filtered and dried.

生成物のX線回折図はOCPの単一相を示し、又、Ca
/P (モル比) Get 1.33 テ’lyッだ。
The X-ray diffraction pattern of the product shows a single phase of OCP and also Ca
/P (molar ratio) Get 1.33 Te'ly.

〈発明の効果〉 本発明の方法によれば、OCRを簡単な工程で一度に多
量に製造することができるので、工業的な製造法として
有利である。
<Effects of the Invention> According to the method of the present invention, OCR can be produced in large quantities at once in a simple process, so it is advantageous as an industrial production method.

又、本発明により製造されたOCPはヒドロキシアパタ
イトの合成の出発物質として特に、従来は困難とされて
いた各種の隣又は陰イオンヲ含有するヒドロキシアパタ
イトの合成の出発物質とすることができる利点がある。
Furthermore, the OCP produced according to the present invention has the advantage that it can be used as a starting material for the synthesis of hydroxyapatite, particularly for the synthesis of hydroxyapatite containing various neighbors or anions, which has been considered difficult in the past. .

Claims (1)

【特許請求の範囲】[Claims] リン酸、水溶性カルシウム塩及びNa、K、NH_4の
炭酸塩、重炭酸塩から選ばれた1種以上を、pH4〜7
で混合して反応させることを特徴とするオクタカルシウ
ムホスフェートの製造法。
One or more selected from phosphoric acid, water-soluble calcium salts, and carbonates and bicarbonates of Na, K, and NH_4 at pH 4 to 7.
A method for producing octacalcium phosphate, which comprises mixing and reacting the octacalcium phosphate.
JP63026677A 1988-02-09 1988-02-09 Production method of octacalcium phosphate Expired - Fee Related JP2584267B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63026677A JP2584267B2 (en) 1988-02-09 1988-02-09 Production method of octacalcium phosphate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63026677A JP2584267B2 (en) 1988-02-09 1988-02-09 Production method of octacalcium phosphate

Publications (2)

Publication Number Publication Date
JPH01203206A true JPH01203206A (en) 1989-08-16
JP2584267B2 JP2584267B2 (en) 1997-02-26

Family

ID=12200025

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63026677A Expired - Fee Related JP2584267B2 (en) 1988-02-09 1988-02-09 Production method of octacalcium phosphate

Country Status (1)

Country Link
JP (1) JP2584267B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0383568A2 (en) * 1989-02-17 1990-08-22 Norian Corporation Calcium phosphate fibers
JP2008222506A (en) * 2007-03-14 2008-09-25 Tokyo Institute Of Technology Octacalcium phosphate crystal containing biologically active substance, method of producing the same and medical composition comprising same
CN106745628A (en) * 2016-12-19 2017-05-31 中国矿业大学 A kind of production method of carbon doping hydroxyapatite defluoridation filter material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0383568A2 (en) * 1989-02-17 1990-08-22 Norian Corporation Calcium phosphate fibers
EP0383568A3 (en) * 1989-02-17 1991-09-04 Norian Corporation Calcium phosphate fibers
JP2008222506A (en) * 2007-03-14 2008-09-25 Tokyo Institute Of Technology Octacalcium phosphate crystal containing biologically active substance, method of producing the same and medical composition comprising same
CN106745628A (en) * 2016-12-19 2017-05-31 中国矿业大学 A kind of production method of carbon doping hydroxyapatite defluoridation filter material

Also Published As

Publication number Publication date
JP2584267B2 (en) 1997-02-26

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