JPS59217610A - Production of calcium-phosphorus based apatite - Google Patents

Production of calcium-phosphorus based apatite

Info

Publication number
JPS59217610A
JPS59217610A JP8928883A JP8928883A JPS59217610A JP S59217610 A JPS59217610 A JP S59217610A JP 8928883 A JP8928883 A JP 8928883A JP 8928883 A JP8928883 A JP 8928883A JP S59217610 A JPS59217610 A JP S59217610A
Authority
JP
Japan
Prior art keywords
calcium
water
apatite
organic solvent
phosphorus
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
JP8928883A
Other languages
Japanese (ja)
Other versions
JPS6344683B2 (en
Inventor
Akihiko Nakamura
明彦 中村
Kensaku Maruyama
丸山 謙作
Shinji Iino
飯野 信二
Koji Nakamura
浩二 中村
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP8928883A priority Critical patent/JPS59217610A/en
Priority to GB08328249A priority patent/GB2132991B/en
Priority to US06/544,361 priority patent/US4481175A/en
Priority to DE19833339232 priority patent/DE3339232A1/en
Priority to FR8317298A priority patent/FR2537558B1/en
Publication of JPS59217610A publication Critical patent/JPS59217610A/en
Publication of JPS6344683B2 publication Critical patent/JPS6344683B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To produce the titled apatite of high quality by easy method, by reacting a calcium compound with a phosphorus compound in a reaction medium containing water and a water-miscible organic solvent. CONSTITUTION:A calcium compound and a phosphorus compound, e.g. Ca(H2PO4)2.H2O, CaHPO4.2H2O, CaHPO4, Ca(OH)2 or CaCO3, are preferably mixed to give 1.30-1.90 desired ratio (Ca/P) and charged previously into a reaction tank, and an adequate amont of water is then added thereto to slurry the compounds. A water-miscible organic solvent, e.g. iso-propanol or tert- butanol, is then added thereto, and the resultant mixture is heated under refluxing. About 2hr refluxing time is sufficient. The titled apatite is then deposited in a slurrylike form and separated by filtration Thus, the titled aimed apatite can be produced with high reproducibility by the easy method.

Description

【発明の詳細な説明】 本発明はカルシウム−リン系アパタイトの新しい製造方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a new method for producing calcium-phosphorus apatite.

一般に、アパタイトとは、一般式Mだ(ZOjつ。In general, apatite has the general formula M (ZOj).

Ylで表わされる。 この式で MはCa、 Pb、 Sr、 Ba、 Mg、 Na、
 K、 Ni、 Fe、 klその他金属原子を、 20、はPO4、As04 、 VO4、SOa、 、
 S i 04 、 CO3その他の酸根を、 Yは、F、OH,C1,Br、私0. 弘CO3その他
の陰イオン性原子(団)で表わされる広範囲な化合物群
の総称である。
It is represented by Yl. In this formula, M is Ca, Pb, Sr, Ba, Mg, Na,
K, Ni, Fe, kl and other metal atoms, 20, are PO4, As04, VO4, SOa, ,
S i 04 , CO3 and other acid radicals, Y is F, OH, C1, Br, I0. A general term for a wide range of compounds represented by CO3 and other anionic atoms (groups).

本発明においては、上記一般式においてMが実質的にC
aであり、20.が実質的にPO,である化合物群を対
象としているので、「カルシウムIJン系アパタイト」
の語を用い、これを以下の説明中では、Apと略記した
In the present invention, M in the above general formula is substantially C
a, and 20. Since the target is a group of compounds in which is essentially PO, it is called "calcium IJ-based apatite".
This is abbreviated as Ap in the following explanation.

Ap群の中で、Yが実質的にOHであるヒドロキシアパ
タイト(以下ヒドロキシアパタイトをHApと略記する
)は近年バイオセラミックスの原料として注目され人工
骨や人工歯等への適用が検討されている。さらに、Ap
はレーザー材料、アルコールの脱水等の触媒、螢光体材
料、電子材料や無機イオン交換体、及び特にHApで顕
著にその効果がみられる◇タンパク質、核酸、酵素、ウ
ィルス等の生体高分子物質を、生体親和性の良さを利用
して分離、精製するクロマトグラフィー用の充填剤とし
ても有望視されている。
Among the Ap group, hydroxyapatite (hereinafter hydroxyapatite is abbreviated as HAp) in which Y is substantially OH has recently attracted attention as a raw material for bioceramics, and its application to artificial bones, artificial teeth, etc. is being considered. Furthermore, Ap
The effect is noticeable in laser materials, catalysts for alcohol dehydration, fluorescent materials, electronic materials, inorganic ion exchangers, and especially HAp. It is also seen as a promising packing material for chromatography for separation and purification by taking advantage of its good biocompatibility.

Apについては、古くから多くの特許や文献にその製法
が発表されている。主要なものとしては次の様なものが
ある。
Regarding Ap, the manufacturing method has been published in many patents and documents for a long time. The main ones are as follows.

(1)  オートクレーブ中で無水リン酸水素カルシウ
ムとリン酸を100〜500℃、1〜500気圧の条件
下で約48時間反応させる水熱合成法。
(1) A hydrothermal synthesis method in which anhydrous calcium hydrogen phosphate and phosphoric acid are reacted in an autoclave under conditions of 100 to 500°C and 1 to 500 atm for about 48 hours.

(2)900〜1300℃の高温でリン酸三カルシウム
と酸化カルシウムを水蒸気流下約3時間反応させる乾式
合成法。
(2) A dry synthesis method in which tricalcium phosphate and calcium oxide are reacted at a high temperature of 900 to 1300°C for about 3 hours under a stream of steam.

(3)水溶性のリン酸塩とカルシウム塩とを水溶液中3
7℃pH7〜8で20日以上反応させ、化学量論比に近
ずける湿式合成法。
(3) Water-soluble phosphate and calcium salt in an aqueous solution
A wet synthesis method that approaches stoichiometric ratio by reacting at 7°C and pH 7 to 8 for 20 days or more.

しかしながら上記(1)の方法も(2)の方法も共に高
温や高圧で反応を行なう為装置が高価なものとなり、さ
らに装置の操作も複雑かつ消費するエネルギーも莫大な
ものである。(3)の方法にお?     いては、僅
かな条件の違いにより生成物の組成が大きく影響され、
さらに化学量論比組成のApを得るには20日以上とい
う凡そ産業的実施にな操作が必要とされ、得られる結果
も再現性が良くない。
However, both methods (1) and (2) require expensive equipment because the reaction is carried out at high temperature and pressure, and furthermore, the equipment is complicated to operate and consumes an enormous amount of energy. How about method (3)? However, slight differences in conditions can greatly affect the composition of the product.
Furthermore, in order to obtain Ap with a stoichiometric composition, an operation of 20 days or more is required, which is almost an industrial practice, and the obtained results are not very reproducible.

これらの事から従来の技術でApの実用的な量を定量的
に合成する事は大変に困難な事であった。それ故にAp
のその優れた物性が知られているにも拘わらず、製造上
の難点から高価なものとなり、非常に限定された用途に
しか使用λ されていないと些うのが実情である。
For these reasons, it has been extremely difficult to quantitatively synthesize a practical amount of Ap using conventional techniques. Therefore Ap
Despite its excellent physical properties, it is difficult to manufacture, making it expensive, and the reality is that it is only used for very limited purposes.

本発明者らは品位の優れたApを多量に、簡便に得る方
法を研究した結果本発明に到達した。
The present inventors have arrived at the present invention as a result of research into a method for easily obtaining a large amount of Ap with excellent quality.

即ち本発明は、カルシウム−リン系アパタイトの製造方
法であって、その技術的特徴は特許請求の範囲に記載の
通りであるが、水と混合し均一相となりうる有機溶媒の
一種以上を含む反む反応媒体とさらに必要に応じて適当
量の水を反応時に存在させて、カルシウム化合物とリン
化合物を反応させる技術に関し、この技術によれば常圧
下の比較的低温度で、しかも短時間に再現性良く、目的
に応じた微粉のもしくは、凝集体のApを得る事が可能
である。
That is, the present invention is a method for producing calcium-phosphorus apatite, the technical features of which are as described in the claims. This technology allows a calcium compound and a phosphorus compound to react by using a reaction medium and an appropriate amount of water as necessary during the reaction, and can be reproduced at a relatively low temperature under normal pressure and in a short time. It is possible to obtain Ap in the form of fine powder or aggregates depending on the purpose with good properties.

本発明を実施するにあたっては、カルシウム化合物とリ
ン化合物を所望のCa/ p比に予め反応槽内に仕込み
、適度の水を添加し、スラリー化する。次に水と混合し
うる有機。溶媒を加え加熱還流する。還流時間は約2時
間もあれば十分である。なお加熱還流時間及び、反応槽
への有機溶媒を含む原料の仕込順序は、通常上記の通如
実施されるが、必ずしもこれに限定する必要はない。
In carrying out the present invention, a calcium compound and a phosphorus compound are charged in advance into a reaction tank at a desired Ca/p ratio, and an appropriate amount of water is added to form a slurry. Next are organics that can be mixed with water. Add a solvent and heat to reflux. A reflux time of about 2 hours is sufficient. Note that the heating reflux time and the order of charging raw materials containing organic solvents to the reaction tank are generally carried out as described above, but are not necessarily limited thereto.

加熱終了後は、生成したApが析出しスラリー状となっ
ているので、これを分離すると良い。
After the heating is completed, the produced Ap precipitates and becomes a slurry, which should be separated.

分離方法は通常実施される炉別のみによる方法と水を有
機溶媒と共に蒸発させた後にApを戸別する方法が適用
できる。
As for the separation method, the usual method using only separate furnaces and the method of separating Ap after evaporating water together with the organic solvent can be applied.

特に後者では、留出した水と有機溶媒に相当する容量の
有機溶媒を加えながら脱水を行い、脱水が終了した後有
機溶媒とApを戸別により分離する方法である。Apの
脱水を完全に行いうる点では後者の方法が好ましい。
In particular, in the latter method, dehydration is performed while adding an organic solvent in a volume corresponding to the distilled water and the organic solvent, and after the dehydration is completed, the organic solvent and Ap are separated from each other. The latter method is preferred in that Ap can be completely dehydrated.

本発明において使用可能なカルシウム化合物及びリン化
合物としては、H3PO4、’ Ca (H2PO4)
2H20,Ca (POa )2 、 CaHPO4%
CaHPO4e2H2伝Ca2 Px 07 、Ca3
(PO+)2s Cab、 CaCA、、 、Ca(O
H)2、CacOa 、Ca F2 、Ca (NO3
)2 、Ca (Coo )2等が使用可能である。し
かし本発明において使用可能な原料はこれらに限定され
る趣旨のものではない。
Calcium compounds and phosphorus compounds that can be used in the present invention include H3PO4, 'Ca (H2PO4)
2H20, Ca(POa)2, CaHPO4%
CaHPO4e2H2den Ca2 Px 07, Ca3
(PO+)2s Cab, CaCA, , Ca(O
H)2, CacOa, Ca F2, Ca (NO3
)2, Ca(Coo)2, etc. can be used. However, the raw materials that can be used in the present invention are not limited to these.

上記の化合物の2種類以上を適宜選択してカルシウムと
リンの原子比(Ca/P)が1.30乃至1.90とな
る様に配合すれば好条件で本発明が実施される。使用す
る原料は用途・目的に応じて選択するとよく、フッ素を
含んだカルシウムIJン系アパタイトを得るにはCaF
2を使用すれば良く、また塩素を含んだカルシウム−リ
ン系アパタイトを得たい場合にはCa C12を使用す
れば良い。これらノ・ロゲン化合物を用いずにHApを
得る事もできる。
The present invention can be carried out under favorable conditions by appropriately selecting two or more of the above compounds and blending them so that the atomic ratio of calcium to phosphorus (Ca/P) is 1.30 to 1.90. The raw materials to be used should be selected depending on the use and purpose. CaF
2 may be used, and if a calcium-phosphorus apatite containing chlorine is desired to be obtained, Ca C12 may be used. HAp can also be obtained without using these norogen compounds.

使用するカルシウム化合物及びリン化合物の純度が高い
程、純度の高い製品が得やすく、反応が短時間ですみ好
ましいが、本発明の実施にあたっては特に純度の高い原
料が求められるものでなく、目的物について要求される
純度に応じて適当な純度の原料を選択するとよい。なお
生体材料とする場合にはFe、Ni、Znなどの不純物
や重金属その他の生体有害物の含有量の低い原料を選択
することが好ましい。一般的には工業グレードの原料で
も充分に使用可能である。
The higher the purity of the calcium compound and phosphorus compound used, the easier it is to obtain a product with high purity, and the reaction time is short, which is preferable. It is advisable to select raw materials of appropriate purity depending on the purity required for the material. In addition, when using it as a biomaterial, it is preferable to select a raw material with a low content of impurities such as Fe, Ni, and Zn, heavy metals, and other biohazardous substances. In general, industrial grade raw materials can be used satisfactorily.

本発明において反応時のカルシウムとリンの仕込量をC
a /Pの原子比で1.30乃至1.90の範囲、好ま
しくは1.45乃至1.75の範囲とすると得られるA
pに未反応物が殆んどなくなり、好都合である。目的と
するApQ原子比(Ca/P)ば、理論的には5/3で
あるので、仕込時のCa/P比も5/3が最適であるは
ずであるが、実際の反応に際しては、原子比が上記の範
囲内であれば好条件でApを合成することができる。さ
らにCa / P比が1.30以下乃至1.90以上の
場合で・2     あっても他のApの用途にも十分
な物性のApが得られることも確認されている。
In the present invention, the amount of calcium and phosphorus charged during the reaction is C
A obtained when the a/P atomic ratio is in the range of 1.30 to 1.90, preferably in the range of 1.45 to 1.75.
This is convenient because there are almost no unreacted substances in p. The target ApQ atomic ratio (Ca/P) is theoretically 5/3, so the optimal Ca/P ratio at the time of preparation should be 5/3, but in actual reaction, If the atomic ratio is within the above range, Ap can be synthesized under favorable conditions. Furthermore, it has been confirmed that even if the Ca/P ratio is from 1.30 or less to 1.90 or more, Ap with sufficient physical properties can be obtained for other Ap uses.

し 本発明で使用する有機溶媒は水と混合X均一相となシう
るものであればよい。状態変数の選択により使用する有
機溶媒の適否が異なる場合もあシうるが、一般的に本発
明の実施に好都合す有機溶媒としては、n−プロピルア
ルコール、1so−プロピルアルコール、  tert
−フチルアルコール及ヒエチレンクリコール、ジエチレ
ングリコール、トリエチレングリコール等の各種アルコ
ール類、メチルセロソルブ、プチルセロンルフ等の各種
セロソルブ類、メチルカルピトール、ジエチルカルピト
ール等のカルピトール類などの水と混合する各種のエー
テル類、ジアセトンアルコール、アセチルアセトン等の
ケトン類、トリエチルアミン、トリフ8f−ルアミン、
ピリジン等のアミン類、メチルセロンルブアセテート、
メチルカルピトールアセテート、カルピトールアセテー
ト等のエステル類、酢酸、プロピオン酸、酪酸、乳酸等
の有機酸類、その他ジメチルホルムアミド、アセトニト
リル、ジメチルスルホキシド等の水と混合しうる有機溶
媒があげられるが、これらは本発明において使用可能な
有機溶媒の一例にすぎず、これらに限定する趣旨ではな
い。
However, the organic solvent used in the present invention may be any organic solvent as long as it can form a homogeneous phase when mixed with water. Although the suitability of the organic solvent to be used may differ depending on the selection of state variables, organic solvents that are generally convenient for carrying out the present invention include n-propyl alcohol, 1so-propyl alcohol, tert.
- Various alcohols such as phthyl alcohol and hyethylene glycol, diethylene glycol, and triethylene glycol, various cellosolves such as methyl cellosolve and butyl selonulf, and calpitols such as methyl calpitol and diethyl calpitol, which can be mixed with water. Ethers, diacetone alcohol, ketones such as acetylacetone, triethylamine, trif-8f-ruamine,
Amines such as pyridine, methylcerone rubacetate,
Examples include esters such as methyl carpitol acetate and carpitol acetate, organic acids such as acetic acid, propionic acid, butyric acid, and lactic acid, and organic solvents that are miscible with water such as dimethylformamide, acetonitrile, and dimethyl sulfoxide. These are only examples of organic solvents that can be used in the present invention, and the present invention is not intended to be limited thereto.

有機溶媒の添加量は、その種類、反応時のカルシウム、
リン両化合物の種類、反応時の諸条件などによりそれぞ
れ適正値が異なるが、いずれの条件においてもスラリー
濃度として50%以下となる量を加えることが望ましい
The amount of organic solvent added depends on its type, calcium during the reaction,
Although the appropriate value differs depending on the type of phosphorus compound and various conditions during the reaction, it is desirable to add an amount such that the slurry concentration is 50% or less under all conditions.

以上のことから従来のApの製造方法が、高温、高圧、
長時間等の工業的実施の観点から考えるに、エネルギー
の莫大な消費、高価な装置、煩雑な操作などの不合理な
所が多かったのに対し、本発明では、有機溶媒を共存さ
せて、低温で反応させ、得られた結晶を戸別・乾燥する
方法のみであるため、熱エネルギーの消費も極めて少な
く、また製造装置も簡素でかつ安価なものですみ、原則
としては通常のガラスまだはステンレス製の材質でも充
分である。
From the above, the conventional method of manufacturing Ap is at high temperature, high pressure,
From the viewpoint of industrial implementation over a long period of time, there were many unreasonable aspects such as enormous consumption of energy, expensive equipment, and complicated operations.However, in the present invention, by coexisting an organic solvent, Because the only method is to react at a low temperature and then dry the resulting crystals from door to door, thermal energy consumption is extremely low, and the manufacturing equipment is simple and inexpensive. A manufactured material is also sufficient.

以上の様に従来法では、簡素、簡便には製造困難であっ
だApを、本発明では、安価に再現性良く定量的に製造
する事を可能にしたもので、工業的にも大きな価値があ
る。
As described above, the present invention makes it possible to quantitatively produce Ap with good reproducibility at low cost, which is difficult to produce simply and conveniently using conventional methods, and has great industrial value. be.

以下実施例に従って本発明の詳細な説明する。The present invention will be described in detail below with reference to Examples.

実施例1 リン酸水素カルシウム拳2水塩(リン酸2カルシウム・
2水塩)1o3.2oy、水酸化カルシウム28.12
@、水12o7、tert−ブタノール400グ、を1
tのフラスコに仕込み、攪拌しながら昇温させ還流温度
(81℃)以下で約2時間加熱した後、反応系内の水分
とtert−ブタノールを蒸発させ、留出したtert
−ブタノールと水に相当する容量のtert−ブタノー
ルを系内に加えながら脱水を行なった。脱水が進行する
に従って内温か上昇し83℃を越えた時点で加熱をやめ
、冷却後生成物(沈殿)を溶媒よシ戸別し、これを乾燥
して白色の粉末を得た。この粉末のX線回折図を図面に
示す。
Example 1 Calcium hydrogen phosphate dihydrate (dicalcium phosphate)
dihydrate) 1o3.2oy, calcium hydroxide 28.12
@, 12o7 water, 400 g tert-butanol, 1
The water and tert-butanol in the reaction system were evaporated, and the distilled tert
Dehydration was carried out while adding tert-butanol in a volume equivalent to -butanol and water into the system. As the dehydration progressed, the internal temperature rose, and when it exceeded 83°C, heating was stopped, and after cooling, the product (precipitate) was separated from the solvent and dried to obtain a white powder. The X-ray diffraction pattern of this powder is shown in the drawing.

図面よシ明らかなように回折角度2θ=31.7.32
.2−132.8に主ピークを有し、ASTMカー)”
9−432 K記載のヒドロキシアパタイト特性回折ピ
ークと一致した。この図は得られたI−(Apが非晶質
型の粉末であることを示している。
As is clear from the drawing, the diffraction angle 2θ = 31.7.32
.. 2-132.8, with a main peak at 2-132.8 (ASTM car)”
This coincided with the characteristic diffraction peak of hydroxyapatite described at 9-432K. This figure shows that the obtained I-(Ap) is an amorphous powder.

実施例2〜4 リン酸水素カルシウム・2水塩、無水リン酸水素カルシ
ウム、炭酸カルシウム、水酸化カルシウム、水、有機溶
媒を第1表に示したそれぞれの条件で仕込み、第1表に
示した以外の条件については実施例1と同様な操作によ
り本発明のカルシウム−リン系アパタイトを得た。
Examples 2 to 4 Calcium hydrogen phosphate dihydrate, anhydrous calcium hydrogen phosphate, calcium carbonate, calcium hydroxide, water, and organic solvent were prepared under the respective conditions shown in Table 1. The calcium-phosphorus apatite of the present invention was obtained by the same operation as in Example 1 except for the following conditions.

第1表に併記した結果のように、本発明の技術によりい
ずれも200℃以下の比較的低温度で、しかも短時間で
カルシウム−リン系アパタイトが定量的に得られた。
As shown in the results shown in Table 1, calcium-phosphorus apatite was quantitatively obtained using the technique of the present invention at a relatively low temperature of 200°C or less and in a short period of time.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は、本発明の実施(実施例1)によって得られたカ
ルシウム−リン系アノシタイトのX線回折図をその−1
:’]ニドレースしたものである。 特許出願人 三井東圧化学株式会社 手  続  補  正  書(自発) 昭和58年10月z1日 特許庁長官若杉和夫殿 1、事件の表示 昭和58年特許願第89288 号 2、発明の名称 カルシウム−リン系アパタイトの製造方法3、補正をす
る者 明細書の「発明の詳細な説明」の欄 5、補正の内容 1)明細書、第6頁、第2〜3行目の[I−I、PO4
、Ca (HzPO*)2I−12,OJを「H3PO
4、H,P、O?、l−lPO3、PI Os、Pct
、、PCl5、Ca (HaP O+) ・HzOjと
補正する。 2)同じく、第10頁、下策1朽目から第11頁、1行
目〆「この図は得られたI−IAp  が非晶質型の粉
末であることを示している。」を削除する。 μ上
The drawing shows the X-ray diffraction diagram of calcium-phosphorus anositite obtained by implementing the present invention (Example 1).
:'] It's made with Nidorase. Patent applicant Mitsui Toatsu Chemical Co., Ltd. Procedural amendment (voluntary) October 1, 1980 Kazuo Wakasugi, Commissioner of the Patent Office1, Indication of the case Patent Application No. 89288, 19892, Name of the invention Calcium- Method for producing phosphorus apatite 3, Person making the amendment Column 5 of “Detailed Description of the Invention” of the specification, Contents of the amendment 1) Specification, page 6, lines 2-3 [I-I, PO4
, Ca (HzPO*)2I-12, OJ as “H3PO
4. H, P, O? , l-lPO3, PI Os, Pct
,,PCl5,Ca (HaP O+) ·HzOj. 2) Similarly, on page 10, page 1, page 11, line 1, delete "This figure shows that the obtained I-IAp is an amorphous powder." . on μ

Claims (2)

【特許請求の範囲】[Claims] (1)水と混合し均一相となりうる有機溶媒を含む反応
媒体中でカルシウム化合物とリン化合物とを反一応させ
る事を特徴とするカルシウム−リン系アパタイトの製造
方法。
(1) A method for producing calcium-phosphorus apatite, which comprises reacting a calcium compound and a phosphorus compound in a reaction medium containing an organic solvent that can be mixed with water to form a homogeneous phase.
(2)  カルシウムとリンの原子比をCa / Pと
して1.30乃至1.90の範囲で行う事を特徴とする
特許請求の範囲第1項に記載の方法。
(2) The method according to claim 1, characterized in that the atomic ratio of calcium to phosphorus is Ca/P in the range of 1.30 to 1.90.
JP8928883A 1982-12-14 1983-05-23 Production of calcium-phosphorus based apatite Granted JPS59217610A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP8928883A JPS59217610A (en) 1983-05-23 1983-05-23 Production of calcium-phosphorus based apatite
GB08328249A GB2132991B (en) 1982-12-14 1983-10-21 Process for preparing apatite
US06/544,361 US4481175A (en) 1982-12-14 1983-10-21 Process for preparing apatite
DE19833339232 DE3339232A1 (en) 1982-12-14 1983-10-28 METHOD FOR PRODUCING A CALCIUM PHOSPHORUS APATIT
FR8317298A FR2537558B1 (en) 1982-12-14 1983-10-28 PROCESS FOR THE MANUFACTURE OF APATITIS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8928883A JPS59217610A (en) 1983-05-23 1983-05-23 Production of calcium-phosphorus based apatite

Publications (2)

Publication Number Publication Date
JPS59217610A true JPS59217610A (en) 1984-12-07
JPS6344683B2 JPS6344683B2 (en) 1988-09-06

Family

ID=13966507

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8928883A Granted JPS59217610A (en) 1982-12-14 1983-05-23 Production of calcium-phosphorus based apatite

Country Status (1)

Country Link
JP (1) JPS59217610A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1986003733A1 (en) * 1984-12-18 1986-07-03 Kanto Kagaku Kabushiki Kaisha Calcium-phosphorus type apatite having novel properties and process for its production
JPS63117904A (en) * 1986-10-31 1988-05-21 Asahi Optical Co Ltd Production of calcium phosphate
JPH06206713A (en) * 1993-01-11 1994-07-26 Agency Of Ind Science & Technol Production of plate-like hydroxyapatite
JP2007250273A (en) * 2006-03-14 2007-09-27 Ueno Mineshige Light guide plate unit

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1986003733A1 (en) * 1984-12-18 1986-07-03 Kanto Kagaku Kabushiki Kaisha Calcium-phosphorus type apatite having novel properties and process for its production
JPS63117904A (en) * 1986-10-31 1988-05-21 Asahi Optical Co Ltd Production of calcium phosphate
US4897250A (en) * 1986-10-31 1990-01-30 Asahi Kogaku Kabushiki Kaisha Process for producing calcium phosphate
JPH06206713A (en) * 1993-01-11 1994-07-26 Agency Of Ind Science & Technol Production of plate-like hydroxyapatite
JP2007250273A (en) * 2006-03-14 2007-09-27 Ueno Mineshige Light guide plate unit

Also Published As

Publication number Publication date
JPS6344683B2 (en) 1988-09-06

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