JPH04198007A - Hydroxyapatite and production thereof - Google Patents
Hydroxyapatite and production thereofInfo
- Publication number
- JPH04198007A JPH04198007A JP2333127A JP33312790A JPH04198007A JP H04198007 A JPH04198007 A JP H04198007A JP 2333127 A JP2333127 A JP 2333127A JP 33312790 A JP33312790 A JP 33312790A JP H04198007 A JPH04198007 A JP H04198007A
- Authority
- JP
- Japan
- Prior art keywords
- hydroxyapatite
- alkali
- solution
- bones
- treated
- 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.)
- Pending
Links
- 229910052588 hydroxylapatite Inorganic materials 0.000 title claims abstract description 54
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 title claims abstract description 54
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 210000000988 bone and bone Anatomy 0.000 claims abstract description 49
- 241000251468 Actinopterygii Species 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000003513 alkali Substances 0.000 claims abstract description 13
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 9
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 9
- 102000004190 Enzymes Human genes 0.000 claims abstract description 7
- 108090000790 Enzymes Proteins 0.000 claims abstract description 7
- 239000007864 aqueous solution Substances 0.000 claims abstract description 4
- 238000010304 firing Methods 0.000 claims description 23
- 238000005406 washing Methods 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 abstract description 28
- 239000000243 solution Substances 0.000 abstract description 22
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract description 17
- 238000003756 stirring Methods 0.000 abstract description 9
- 238000010828 elution Methods 0.000 abstract description 8
- 108091005804 Peptidases Proteins 0.000 abstract description 7
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 abstract description 6
- 230000001590 oxidative effect Effects 0.000 abstract description 4
- 229910000391 tricalcium phosphate Inorganic materials 0.000 abstract description 4
- 235000019731 tricalcium phosphate Nutrition 0.000 abstract description 4
- 239000004365 Protease Substances 0.000 abstract description 3
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract 4
- 235000019688 fish Nutrition 0.000 description 26
- 238000000034 method Methods 0.000 description 15
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 238000001354 calcination Methods 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 8
- 239000002994 raw material Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 102000035195 Peptidases Human genes 0.000 description 5
- 239000012620 biological material Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000008187 granular material Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 150000007524 organic acids Chemical class 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000001506 calcium phosphate Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 244000144972 livestock Species 0.000 description 3
- 235000013372 meat Nutrition 0.000 description 3
- 150000007522 mineralic acids Chemical class 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 229940078499 tricalcium phosphate Drugs 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 241000276498 Pollachius virens Species 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 210000001519 tissue Anatomy 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 238000004438 BET method Methods 0.000 description 1
- 108090000145 Bacillolysin Proteins 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 108091005658 Basic proteases Proteins 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000555825 Clupeidae Species 0.000 description 1
- 241001149724 Cololabis adocetus Species 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241001313700 Gadus chalcogrammus Species 0.000 description 1
- 102000035092 Neutral proteases Human genes 0.000 description 1
- 108091005507 Neutral proteases Proteins 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 241000269821 Scombridae Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 239000000560 biocompatible material Substances 0.000 description 1
- 239000000316 bone substitute Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 235000020640 mackerel Nutrition 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000002459 porosimetry Methods 0.000 description 1
- -1 porosity Chemical compound 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Materials For Medical Uses (AREA)
- Dental Prosthetics (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、骨充填材などの生体材料に適したアルカリ成
分不溶出性ヒドロキシアパタイト及びその製造方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an alkali-insoluble hydroxyapatite suitable for biomaterials such as bone filling materials and a method for producing the same.
[従来の技術]
ヒドロキシアパタイトはを推動物の骨や歯を構成する生
体硬組織の主要成分である。そのため、生体親和性に優
れたセラミックス材料として注目されており、人工骨、
人工歯根、人工歯、骨充填剤などの生体材料への応用が
活発に進められている。[Prior Art] Hydroxyapatite is a major component of biological hard tissue that constitutes the bones and teeth of moving animals. Therefore, it is attracting attention as a ceramic material with excellent biocompatibility, and it is used for artificial bones,
Applications to biomaterials such as artificial tooth roots, artificial teeth, and bone fillers are being actively pursued.
通常、ヒドロキシアパタイトはカルシウム塩とリン酸塩
を原料として、
(1)必要に応じて水蒸気雰囲気中で、約1000℃の
高温で反応させる(乾式法)、
(2)特定pHの溶液中で約100℃の温度で反応させ
る(湿式法)、
(3)約400℃の高温、数千気圧以上の高圧下に水蒸
気中で反応させる(水熱合成法)などで合成することが
できる。Normally, hydroxyapatite is produced using calcium salts and phosphates as raw materials, (1) reacting at a high temperature of about 1000°C in a steam atmosphere as necessary (dry method), (2) reacting in a solution with a specific pH about It can be synthesized by reacting at a temperature of 100°C (wet method), or (3) reacting in water vapor at a high temperature of approximately 400°C and under high pressure of several thousand atmospheres or more (hydrothermal synthesis method).
このようにして合成されたヒドロキシアパタイトは、極
めて純粋である為、天然骨、歯などの硬組織に含まれる
カルシウム及びリン以外の微量金属を含んでいないので
、生体適合性は天然骨に比べて劣る6
一方、天然骨由来のヒドロキシアパタイトの開発も進め
られているが、家畜骨を原料として用いる方法は、家畜
の成育環境が必ずしも清浄とは言い難く、そのために、
家畜骨には有害元素の含有という生体材料への応用に際
して基本的な問題を有する。The hydroxyapatite synthesized in this way is extremely pure and does not contain trace metals other than calcium and phosphorus that are found in hard tissues such as natural bones and teeth, so it has better biocompatibility than natural bone. Inferior 6 On the other hand, the development of hydroxyapatite derived from natural bones is progressing, but the method of using livestock bones as a raw material does not necessarily have a clean environment in which livestock grow.
Livestock bones have a fundamental problem when applied to biomaterials: they contain harmful elements.
本発明者らは、清浄な環境で成育する魚の骨を利用して
、天然骨由来のヒドロキシアパタイトを提供すべく、鋭
意研究を重ね、精製魚骨を原料とし、酵素処理、アルカ
リ処理して蛋白質成分を除去し、1200℃以下の温度
で焼成することによりヒドロキシアパタイトを製造する
方法を提案した(特願平1−306051号)。The present inventors have conducted extensive research in order to provide natural bone-derived hydroxyapatite using fish bones that grow in a clean environment, and have used purified fish bones as a raw material, enzyme-treated and alkali-treated to produce protein. proposed a method for producing hydroxyapatite by removing the components and firing at a temperature of 1200° C. or lower (Japanese Patent Application No. 306051/1999).
しかしながら、この方法で得られるヒドロキシアパタイ
トの粉末又は顆粒を水中に分散すると、ヒドロキシアパ
タイトからアルカリ成分が溶出し、液のpHが上昇する
という現象が起きることが判明した。このようなアルカ
リ溶出現象は生体材料として使用する際の障害になり、
このような現象を生じない魚骨を原料としたヒドロキア
パタイトの開発が要望されている。However, it has been found that when the hydroxyapatite powder or granules obtained by this method are dispersed in water, a phenomenon occurs in which alkaline components are eluted from the hydroxyapatite and the pH of the liquid increases. Such alkali elution phenomenon becomes an obstacle when used as a biomaterial.
There is a demand for the development of hydroxyapatite made from fish bones that does not cause this phenomenon.
[発明が解決しようとする課題]
本発明は、このような事情に鑑みてなされたもので、本
発明の目的は、魚骨を原料として用いたアルカリ溶出現
象の生じない生体適合性の優れたヒドロキシアパタイト
及びその製造方法を提供することにある。[Problems to be Solved by the Invention] The present invention has been made in view of the above circumstances, and an object of the present invention is to provide an excellent biocompatible material that does not cause alkali elution using fish bones as a raw material. An object of the present invention is to provide hydroxyapatite and a method for producing the same.
[課題を解決するための手段]
本発明は5R製魚骨を原料とした、アルカリ成分不溶出
性ヒドロキシアパタイトを提供する。[Means for Solving the Problems] The present invention provides alkali-insoluble hydroxyapatite made from 5R fish bones.
本発明のヒドロキシアパタイトは、その粉末又は顆粒1
重量部を10重量部の水に分散した分散液のpHは10
未満である。The hydroxyapatite of the present invention is powder or granule 1
The pH of a dispersion prepared by dispersing 1 part by weight in 10 parts by weight of water is 10.
less than
このようなアルカリ成分不溶出のヒドロキシアパタイト
は、本発明方法によって製造することができる。Such hydroxyapatite that does not elute alkaline components can be produced by the method of the present invention.
すなわち、本発明のヒドロキシアパタイトの製造方法は
、精製魚骨を酵素処理しで残存する蛋白質を除去し、次
いでアルカリ処理し水洗して得られる粗製ヒドロキシア
パタイトを350℃〜1200°Cの温度で一次焼成し
た後、pH2以上10未満の水性洗浄液で洗浄処理し、
350℃〜600℃の温度で二次焼成することを特徴と
している。That is, in the method for producing hydroxyapatite of the present invention, purified fish bones are treated with enzymes to remove remaining proteins, and then treated with alkali and washed with water. After baking, cleaning with an aqueous cleaning solution with a pH of 2 or more and less than 10,
It is characterized by secondary firing at a temperature of 350°C to 600°C.
本発明に用いる魚骨としては、原料供給量が多く且つ安
定しているスケトウダラ、イワシ、サバ、サンマなどの
骨が好適であり、特に成育海域が清浄で、有害成分を殆
ど含んでいないスケトウダラの骨が好ましい。As the fish bones used in the present invention, bones of pollock, sardines, mackerel, saury, etc., which have a large and stable supply of raw materials, are suitable.In particular, bones of pollock, which have clean growing waters and contain almost no harmful components, are suitable. Bone is preferred.
本発明において、精製魚骨が原料として用いられる。精
製魚骨は、魚肉の付着している魚骨を酵素処理して魚肉
及び蛋白質を出来るだけ取除き、更に殺菌処理、例えば
05〜3%の過酸化水素溶液で20〜180分間煮沸し
て後、十分に水洗し乾燥して得られる、有機物含有量が
約30%以下の一般生菌数の少ない保存性の良好な魚骨
精製物である。In the present invention, purified fish bones are used as a raw material. Purified fish bones are obtained by enzymatically treating the fish bones with fish meat attached to remove as much of the fish meat and protein as possible, and then sterilizing them, for example by boiling them in a 0.5 to 3% hydrogen peroxide solution for 20 to 180 minutes. It is a purified fish bone product obtained by thorough washing with water and drying, which has an organic matter content of about 30% or less, has a low number of viable bacteria, and has a good shelf life.
上記精製魚骨を、更に蛋白質分解酵素で処理して残存す
る蛋白質を除去する。The purified fish bone is further treated with a proteolytic enzyme to remove remaining proteins.
すなわち、精製魚骨を純水中に入れ、−旦煮沸した後、
温度を50〜70℃に下げ、撹拌しながら蛋白質分解酵
素を精製魚骨中の蛋白質量の0.1重量%〜2重量%、
好ましくは、0.4〜1.0重量%添加して反応させる
。蛋白質分解酵素の作用により蛋白質のペプチド結合が
分解していくにつれて反応液が酸性となりpHが低下す
るので、水酸化ナトリウム水溶液を適宜添加してpHを
7〜9に保持して酵素活性を維持する。That is, after putting purified fish bones in pure water and boiling it,
Lower the temperature to 50-70°C and purify the proteolytic enzyme while stirring. 0.1% to 2% by weight of the protein in the fish bone.
Preferably, it is added in an amount of 0.4 to 1.0% by weight for reaction. As the peptide bonds in the protein are broken down by the action of the protease, the reaction solution becomes acidic and the pH decreases, so add an aqueous sodium hydroxide solution as appropriate to maintain the pH at 7 to 9 to maintain enzyme activity. .
蛋白質分解酵素としては、動物、植物及び微生物を起源
とするものを用いることができる。これら蛋白質分解酵
素のうちアルカリプロテアーゼ又は中性プロテアーゼが
好ましい。更に、その至適温度が35℃以上のものが好
ましい。As the proteolytic enzyme, those originating from animals, plants, and microorganisms can be used. Among these proteases, alkaline protease or neutral protease is preferred. Further, it is preferable that the optimum temperature is 35°C or higher.
精製魚骨を再度酵素処理することにより、残存有機物量
を10%以下にする。残存有機物量が多すぎると、次に
行なう焼成工程で適切な温度制御が不可能となり、過昇
温する事故が多発するので好ましくない。By enzymatically treating purified fish bones again, the amount of residual organic matter is reduced to 10% or less. If the amount of residual organic matter is too large, it becomes impossible to properly control the temperature in the next firing step, which is undesirable because accidents of excessive temperature rise occur frequently.
精製魚骨を酵素処理した後、アルカリ処理を施して粗製
ヒドロキシアパタイトを得る。After enzymatically treating purified fish bones, they are treated with alkali to obtain crude hydroxyapatite.
アルカリ処理は、上記蛋白質分解酵素による分解反応が
緩慢になった時点で、反応液中に水酸化ナトリウム水溶
液を添加し、水酸化ナトリウム濃度を1〜4重量%にし
、液温を90℃〜98℃に上昇し、約30〜60分間撹
拌することにより行なう。In the alkaline treatment, when the decomposition reaction by the proteolytic enzyme becomes slow, an aqueous sodium hydroxide solution is added to the reaction solution to make the sodium hydroxide concentration 1 to 4% by weight, and the temperature of the solution is adjusted to 90°C to 98°C. C. and stirring for about 30-60 minutes.
アルカリ処理は、酵素の失活及び残存有機物の分解ばか
りでなく、次に行なわれる焼成工程中に燐酸三カルシウ
ムが生成するのを抑制する効果がある。このアルカリ処
理により焼成後のヒドロキシアパタイトの燐酸三カルシ
ウム含有量を15%以下、好ましくは10%以下、更に
好ましくは5%以下に減少させることができる。Alkaline treatment not only deactivates enzymes and decomposes residual organic matter, but also has the effect of suppressing the formation of tricalcium phosphate during the subsequent firing process. This alkali treatment can reduce the tricalcium phosphate content of hydroxyapatite after firing to 15% or less, preferably 10% or less, and more preferably 5% or less.
アルカリ処理が完了して後、反応液を冷却し、骨分を分
離し、純水で十分洗浄して粗製ヒドロキシアパタイトを
得る。After the alkaline treatment is completed, the reaction solution is cooled, the bones are separated and thoroughly washed with pure water to obtain crude hydroxyapatite.
上記のようにして得られた粗製ヒドロキシアパタイトを
一次焼成処理する。The crude hydroxyapatite obtained as described above is subjected to a primary firing treatment.
一次焼成処理は、粗製ヒドロキシアパタイトに残存する
少量の有機物を完全に焼却除去し、最終目的物であるヒ
ドロキシアパタイトの気孔率、比表面積、結晶性などの
物性を所定の値に調整する目的で実施される。The primary firing treatment is carried out to completely incinerate and remove the small amount of organic matter remaining in the crude hydroxyapatite, and to adjust the physical properties of the final target hydroxyapatite, such as porosity, specific surface area, and crystallinity, to predetermined values. be done.
一次焼成温度は350℃〜1200℃の温度範囲で適宜
選択される。焼成温度が低過ぎると有機物の焼却除去が
不完全で、最終製品が生体材料として適切でなくなり、
一方、焼成温度が高過ぎてもヒドロキシアパタイトが分
解し、燐酸三カルシウムなどが生成し好ましくない。焼
成時間は通常約30〜300分間である。The primary firing temperature is appropriately selected within the temperature range of 350°C to 1200°C. If the calcination temperature is too low, the removal of organic matter by incineration will be incomplete and the final product will not be suitable as a biomaterial.
On the other hand, if the firing temperature is too high, hydroxyapatite will decompose and tricalcium phosphate will be produced, which is not preferable. Firing time is usually about 30 to 300 minutes.
焼成工程は、酸化雰囲気、即ち、酸素ガスを多量に含む
雰囲気中、例えば大気雰囲気中で行なわれる。酸素濃度
は、焼成工程の全ての段階で、5%以上、好ましくは1
5%以上である。酸素濃度が5%未満であると、焼成時
に残存有機物を完全に焼却することができず、未燃焼有
機物や炭素が残留するので好ましくない。The firing step is performed in an oxidizing atmosphere, that is, an atmosphere containing a large amount of oxygen gas, for example, in an air atmosphere. The oxygen concentration is 5% or more, preferably 1% at all stages of the firing process.
It is 5% or more. If the oxygen concentration is less than 5%, residual organic matter cannot be completely incinerated during firing, and unburned organic matter and carbon remain, which is not preferable.
一次焼成が終了したヒドロキシアパタイトをpH2以上
10未満、好ましくはpH3〜8、更に好ましくはpH
3,5〜5の水性洗浄液で洗浄処理する。この洗浄処理
を施すことにより、最終的に得られるヒドロキシアパタ
イトからアルカリ成分が溶出しなくなるという驚くべき
効果が得られる6
洗浄液のpHが2より低過ぎるとヒドロキシアパタイト
が溶解し好ましくなく、一方pHが10以上になると洗
浄処理の効果が得られない。The pH of the hydroxyapatite after primary firing is 2 or more and less than 10, preferably 3 to 8, and more preferably
3. Clean with aqueous cleaning solution from step 5 to step 5. This cleaning process has the surprising effect of preventing alkaline components from eluting from the hydroxyapatite that is finally obtained.6 If the pH of the cleaning solution is too low than 2, the hydroxyapatite will dissolve, which is undesirable; When it is 10 or more, the effect of cleaning treatment cannot be obtained.
洗浄処理は、−次焼成処理終了後のヒドロキシアパタイ
トを水中に分散させ静置又は撹拌することにより実施さ
れ、液のpHが所定の値を保つように無機酸、有機酸又
はこれらの混合物を添加して行なわれる。The cleaning treatment is carried out by dispersing the hydroxyapatite in water after the secondary calcination treatment and leaving it standing or stirring, and then adding an inorganic acid, an organic acid, or a mixture thereof so that the pH of the liquid remains at a predetermined value. It is done as follows.
洗浄処理は好ましくは撹拌下で行なわれ、ボールミルな
どを用いて攪拌して分散と同時に粉砕を行なうのが効果
的である。The washing treatment is preferably carried out under stirring, and it is effective to use a ball mill or the like to stir and simultaneously disperse and pulverize.
洗浄液を所定のpHに保つ目的で、無機酸、有機酸、又
はこれらの混合物を添加するが、次の工程の二次焼成時
に用いられる焼成炉の損耗を避けるために酢酸、蓚酸、
蟻酸、クエン酸などの有機酸のみを添加するのが望まし
い。An inorganic acid, an organic acid, or a mixture thereof is added to keep the cleaning solution at a predetermined pH, but acetic acid, oxalic acid,
It is desirable to add only organic acids such as formic acid and citric acid.
洗浄処理は、洗浄液のpHが更に酸を添加しなくとも、
所定のpHを一定に維持するようになるまで行なう必要
があり、洗浄時間は条件により異なるが約10〜100
分間である。The cleaning process is such that the pH of the cleaning solution changes even without adding acid.
It is necessary to perform the cleaning until the specified pH is maintained constant, and the cleaning time varies depending on the conditions, but it is approximately 10 to 100 minutes.
It is a minute.
洗浄処理が終了したヒドロキシアパタイトを二次焼成す
る。After the cleaning treatment, the hydroxyapatite is subjected to secondary firing.
二次焼成は、洗浄工程で不可避的に付着する有機酸、無
機酸などを加熱により完全に除去するために実施し、通
常350〜600°C1好ましくは400〜500℃の
温度で通常約30〜300分間行なわれる。二焼成温度
が一次焼成温度を越えると、経済的負担が大きいばかり
でなく、最終生成物の物性も変化するので、二次焼成温
度は一次焼成温度よりも低い温度が好ましい。Secondary firing is carried out to completely remove organic acids, inorganic acids, etc. that inevitably adhere during the cleaning process by heating, and is usually at a temperature of 350 to 600°C, preferably 400 to 500°C, and usually about 30 to 30°C. It will be held for 300 minutes. If the secondary calcination temperature exceeds the primary calcination temperature, it will not only impose a heavy economic burden but also change the physical properties of the final product, so the secondary calcination temperature is preferably lower than the primary calcination temperature.
二次焼成も一次焼成と同様、酸化雰囲気中で行なわれる
。The secondary firing is also performed in an oxidizing atmosphere like the primary firing.
このようにして得られたヒドロキシアパタイトは、アル
カリ成分の水中への溶出が抑制されている。すなわち、
上記ヒドロキシアパタイトの粉末又は顆粒1重量部を水
10重量部に分散した分散液のpHは10未満である。In the hydroxyapatite thus obtained, elution of alkaline components into water is suppressed. That is,
The pH of a dispersion prepared by dispersing 1 part by weight of the hydroxyapatite powder or granules in 10 parts by weight of water is less than 10.
本発明の精製魚骨を原料としたヒドロキシアパタイトは
、粉末又は分級した顆粒状物として、そのまま骨充環材
及び骨増量材などに用いることができる。更に、そのま
ま又は微粉砕した後、通常のセラミックスの成形方法、
例えば、鋳込成形法、プレス成形法、押出成形法などに
より賦形・ し、次いで脱脂填結して緻密体あるいは
多孔体に成形し、人工骨、人工歯、人工歯根などに使用
することができる。The hydroxyapatite made from purified fish bones of the present invention can be used as it is as a powder or classified granules for bone filling materials, bone bulking materials, and the like. Furthermore, the usual ceramic forming method, either as it is or after finely pulverizing,
For example, it can be shaped by casting, press molding, extrusion, etc., then degreased and filled into a dense or porous body, which can be used for artificial bones, artificial teeth, artificial tooth roots, etc. can.
[発明の効果]
上記のように、本発明の魚骨を原料としヒドロキシアパ
タイトは、アルカリ成分を溶出しないので、生体骨代用
材料として治療用に用いるのに好適であり、本発明の方
法は、−次焼成処理後にpH2以上10未満の水性洗浄
液で洗浄し、更に二次焼成処理を施すことにより、精製
魚骨を原料として用いてアルカリ成分の溶出現象の生じ
ないヒドロキシアパタイトを製造できるという効果があ
る。[Effects of the Invention] As described above, the hydroxyapatite made from fish bones of the present invention does not elute alkaline components, so it is suitable for use as a biological bone substitute material for treatment, and the method of the present invention - By washing with an aqueous cleaning solution with a pH of 2 or more and less than 10 after the secondary calcination treatment, and further performing the secondary calcination treatment, it is possible to produce hydroxyapatite without the elution of alkaline components using purified fish bones as a raw material. be.
[実施例]
次に、参考例及び実施例により本発明を更に詳細に説明
する。[Example] Next, the present invention will be explained in more detail by reference examples and examples.
参考例
スケトウダラを3枚に下ろし、得られた魚肉が付着して
いる魚骨を0.3%の天然酵素デイスクリン−PT水溶
液に1=3の重量比となるように添加し、液温を50℃
で20分間撹拌し、更に2時間煮沸した後、骨分を取出
し水洗した。次いで、これを1%過酸化水素水溶液に浸
して2時間煮沸した後、骨分な取出して水洗し、105
℃で4時間乾燥することにより、精製魚骨を作製した。Reference Example Walleye pollock was cut into three pieces, and the obtained fish bones with the fish meat attached were added to a 0.3% aqueous solution of the natural enzyme Discrin-PT in a weight ratio of 1=3, and the temperature of the solution was lowered. 50℃
After stirring for 20 minutes and boiling for an additional 2 hours, the bones were taken out and washed with water. Next, this was immersed in a 1% aqueous hydrogen peroxide solution and boiled for 2 hours, and then the bones were taken out and washed with water.
Purified fish bones were prepared by drying at ℃ for 4 hours.
実施例1
参考例で得られた精製魚骨を純水中で一旦煮沸し、5分
後温度を50℃に下げ、魚骨の0.5重量%のデイスク
リン−NTを添加し、I N−NaOHを適宜添加して
pHを8に保持しつつ2時間撹拌した。Example 1 The purified fish bones obtained in Reference Example were once boiled in pure water, and after 5 minutes, the temperature was lowered to 50°C, and 0.5% by weight of the fish bones was added with Disclin-NT. The mixture was stirred for 2 hours while maintaining the pH at 8 by appropriately adding -NaOH.
次いで、水酸化ナトリウムを反応系の3重量%になるよ
うに添加し、95℃で1時間保持した。Next, sodium hydroxide was added to the reaction system in an amount of 3% by weight, and the mixture was maintained at 95° C. for 1 hour.
冷却後、骨分な取出し、水洗して、105℃で4時間乾
燥して粗製ヒドロキシアパタイトを作製した。After cooling, the bones were taken out, washed with water, and dried at 105° C. for 4 hours to produce crude hydroxyapatite.
このようにして作製した粗製ヒドロキシアパタイトをガ
ス炉を用いて900℃で2時間に亙って一次焼成を行な
った。The crude hydroxyapatite thus produced was primarily fired at 900° C. for 2 hours using a gas furnace.
一次焼成を終えて得られたヒドロキシアパタイトを水性
洗浄液で次のようにして洗浄処理した。The hydroxyapatite obtained after the primary firing was washed with an aqueous washing solution as follows.
すなわち、ヒドロキシアパタイトをボールミル中でT)
Hを酢酸又はアンモニア水で第1表に示す所定の値に調
整した水性洗浄液と重量比で1=10となるように混合
し、1時間撹拌し、固形分を分離し、純水で洗浄して1
05℃で4時間乾燥した。なお、第1表のpH2の水溶
液を調製する際は、酢酸と共に硝酸を添加した。That is, hydroxyapatite is produced in a ball mill (T)
Mix H with an aqueous cleaning solution adjusted to the specified value shown in Table 1 with acetic acid or aqueous ammonia so that the weight ratio is 1=10, stir for 1 hour, separate the solid content, and wash with pure water. te1
It was dried at 05°C for 4 hours. In addition, when preparing the aqueous solution of pH 2 shown in Table 1, nitric acid was added together with acetic acid.
洗浄処理を終えたヒドロキシアパタイトをガス炉を用い
て400℃で2時間加熱処理して、二次焼成を行なった
。After the cleaning treatment, the hydroxyapatite was heat-treated at 400° C. for 2 hours using a gas furnace to perform secondary firing.
得られたヒドロキシアパタイト及び上記の洗浄処理及び
二次焼成を行なわなかったヒドロキシアパタイト(No
、1)について、次のようにして、アルカリ溶出テスト
を実施した。The obtained hydroxyapatite and the hydroxyapatite that was not subjected to the above washing treatment and secondary firing (No.
, 1), an alkali elution test was conducted as follows.
すなわち、ヒドロキシアパタイト1重量部を純水10重
量部に添加し、1時間攪拌した後、上澄液のpHを測定
した。p)]の値が8以下のものを(−)、8より高く
10より低いものを(±)、10以上のものを(+)と
判定した。得られた結果を第1表に示す。That is, 1 part by weight of hydroxyapatite was added to 10 parts by weight of pure water, and after stirring for 1 hour, the pH of the supernatant liquid was measured. p)] values of 8 or less were determined as (-), those with a value higher than 8 and lower than 10 were determined as (±), and those with a value of 10 or more were determined as (+). The results obtained are shown in Table 1.
第1表に示すように、洗浄処理を行なわなかったヒドロ
キシアパタイト及び水性洗浄液のpHが10では溶出テ
ストの結果は十で、水性洗浄液のpHが10未満の場合
が洗浄効果を上げる限界であることが判明した。また、
水性洗浄液のpHが2の場合は、洗浄工程でヒドロキシ
アパタイトの溶解現象が若干認められた。従って、水性
洗浄液のpHは2以上10未満でなければならず、好ま
しくは3〜8、更に好ましくは3.5〜5である。As shown in Table 1, when hydroxyapatite was not subjected to cleaning treatment and the pH of the aqueous cleaning solution was 10, the elution test result was ten, and when the pH of the aqueous cleaning solution was less than 10, this was the limit for increasing the cleaning effect. There was found. Also,
When the pH of the aqueous cleaning solution was 2, some dissolution of hydroxyapatite was observed during the cleaning process. Therefore, the pH of the aqueous cleaning solution must be 2 or more and less than 10, preferably 3-8, more preferably 3.5-5.
実施例2
粗製ヒドロキシアパタイトを第2表に示す所定の温度で
一次焼成し、450℃で二次焼成する以外は全て実施例
1と同様にしてヒドロキシアパタイトを作製した。実験
N009及びNo、11においては洗浄処理を行なわな
かった。得られたヒドロキシアパタイトのアルカリ溶出
テストを実施例1と同様の方法で行ない、物性として比
表面積をBET法で、気孔率を水銀圧入法で測定し、結
果を第2表に示す。Example 2 Hydroxyapatite was produced in the same manner as in Example 1, except that crude hydroxyapatite was primarily fired at a predetermined temperature shown in Table 2 and secondly fired at 450°C. In Experiments No. 009 and No. 11, no cleaning treatment was performed. The obtained hydroxyapatite was subjected to an alkali elution test in the same manner as in Example 1, and the physical properties were measured by the BET method for specific surface area and by the mercury porosimetry method, and the results are shown in Table 2.
第2表から明らかなように、最終ヒドロキシアパタイト
の物性は、−次焼成後に洗浄処理を施しても殆ど変化し
ていない。As is clear from Table 2, the physical properties of the final hydroxyapatite hardly change even after the cleaning treatment after the second firing.
Claims (2)
ドロキシアパタイト。(1) Alkali-insoluble hydroxyapatite made from purified fish bones.
、次いでアルカリ処理し水洗して得られる粗製ヒドロキ
シアパタイトを350℃〜1200℃の温度で一次焼成
した後、pH2以上10未満の水性洗浄液で洗浄処理し
、350℃〜600℃の温度で二次焼成することを特徴
とするヒドロキシアパタイトの製造方法。(2) Purified fish bones are treated with enzymes to remove remaining proteins, then treated with alkali and washed with water. The crude hydroxyapatite obtained is first calcined at a temperature of 350°C to 1200°C, and then an aqueous solution with a pH of 2 or more and less than 10 A method for producing hydroxyapatite, which comprises washing with a washing liquid and performing secondary firing at a temperature of 350°C to 600°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2333127A JPH04198007A (en) | 1990-11-28 | 1990-11-28 | Hydroxyapatite and production thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2333127A JPH04198007A (en) | 1990-11-28 | 1990-11-28 | Hydroxyapatite and production thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04198007A true JPH04198007A (en) | 1992-07-17 |
Family
ID=18262597
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2333127A Pending JPH04198007A (en) | 1990-11-28 | 1990-11-28 | Hydroxyapatite and production thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04198007A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1994021556A1 (en) * | 1993-03-24 | 1994-09-29 | Children's Medical Center Corporation | Isolation of the calcium-phosphate crystals of bone |
| WO1996014886A1 (en) * | 1994-11-10 | 1996-05-23 | Merck Patent Gmbh | Process for producing spongiosa bone ceramics having a low calcium oxide content |
| US5565502A (en) * | 1993-03-24 | 1996-10-15 | Children's Medical Center Corporation | Isolation of the calcium-phosphate crystals of bone |
| EP0657178A3 (en) * | 1993-11-30 | 2000-02-02 | CORIMED GmbH | Method for making implant ceramic material especially hydroxyapatite containing implant ceramic material |
| EP2075231A1 (en) * | 2007-12-28 | 2009-07-01 | Universidad de Vigo | Biphasic calcium phosphate and method for obtaining same from fish bones |
| CN108471788A (en) * | 2016-01-26 | 2018-08-31 | 泰万盛集团(大众)有限公司 | A method of preparing fishbone dust |
| CN109264690A (en) * | 2018-12-06 | 2019-01-25 | 湖南三友环保科技股份有限公司 | A method of purifying fish waste Central Plains form hydroxyapatite |
| JP2021042090A (en) * | 2019-09-06 | 2021-03-18 | 株式会社日本バリアフリー | Method for producing hydroxyapatite for biocompatible material |
| JP2024050785A (en) * | 2019-08-30 | 2024-04-10 | セルコ インコーポレイテッド | Foraminifera-derived bone graft material |
-
1990
- 1990-11-28 JP JP2333127A patent/JPH04198007A/en active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5691397A (en) * | 1993-03-24 | 1997-11-25 | Children's Medical Center Corporation | Isolation of the calcium-phosphate crystals of bone |
| US5439951A (en) * | 1993-03-24 | 1995-08-08 | Children's Medical Center Corporation | Isolation of the calcium-phosphate crystals of bone |
| WO1994021556A1 (en) * | 1993-03-24 | 1994-09-29 | Children's Medical Center Corporation | Isolation of the calcium-phosphate crystals of bone |
| US5565502A (en) * | 1993-03-24 | 1996-10-15 | Children's Medical Center Corporation | Isolation of the calcium-phosphate crystals of bone |
| JPH08510984A (en) * | 1993-03-24 | 1996-11-19 | チルドレンズ メディカル センター コーポレイション | Isolation of bone calcium phosphate crystals |
| EP0657178A3 (en) * | 1993-11-30 | 2000-02-02 | CORIMED GmbH | Method for making implant ceramic material especially hydroxyapatite containing implant ceramic material |
| WO1996014886A1 (en) * | 1994-11-10 | 1996-05-23 | Merck Patent Gmbh | Process for producing spongiosa bone ceramics having a low calcium oxide content |
| EP2075231A1 (en) * | 2007-12-28 | 2009-07-01 | Universidad de Vigo | Biphasic calcium phosphate and method for obtaining same from fish bones |
| CN108471788A (en) * | 2016-01-26 | 2018-08-31 | 泰万盛集团(大众)有限公司 | A method of preparing fishbone dust |
| JP2019502387A (en) * | 2016-01-26 | 2019-01-31 | タイ ユニオン グループ パブリック カンパニー リミテッド | Method for preparing fish bone powder |
| EP3407737A4 (en) * | 2016-01-26 | 2019-09-25 | Thai Union Group Public Company Limited | PROCESS FOR PREPARING FISH BONE POWDER |
| CN109264690A (en) * | 2018-12-06 | 2019-01-25 | 湖南三友环保科技股份有限公司 | A method of purifying fish waste Central Plains form hydroxyapatite |
| JP2024050785A (en) * | 2019-08-30 | 2024-04-10 | セルコ インコーポレイテッド | Foraminifera-derived bone graft material |
| JP2021042090A (en) * | 2019-09-06 | 2021-03-18 | 株式会社日本バリアフリー | Method for producing hydroxyapatite for biocompatible material |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0522547B2 (en) | ||
| JPH04198007A (en) | Hydroxyapatite and production thereof | |
| JP2785245B2 (en) | Natural hydroxyapatite and the like and method for producing the same | |
| WO1990005461A1 (en) | Process for purifying blood plasma | |
| JPH04265214A (en) | Production of hydroxyapatite | |
| JPH0818829B2 (en) | Method for producing calcium material mainly composed of natural calcium compound | |
| US3083194A (en) | Montmorillonite adsorption of fibrin from bovine blood plasma | |
| CN109880875B (en) | A kind of selenium-enriched tuna bone collagen peptide and preparation method thereof | |
| JPH073263A (en) | Soil conditioner for eggshell powder that is well compatible with soil and its manufacturing method | |
| JP2563186B2 (en) | Method for producing calcium phosphate-based cured product | |
| KR102743575B1 (en) | Manufacturing Method of Low Molecular Collagen Peptide Using Fish By-products | |
| JPH03164411A (en) | Novel fired apatite | |
| KR100452410B1 (en) | Process for preparing porous bioceramic materials | |
| RU1834644C (en) | Method for receiving photo-protein | |
| JP5328077B2 (en) | Method for producing low endotoxinized gelatin | |
| JPH11318389A (en) | Production of odorless fish calcium agent | |
| JPS58138360A (en) | Preparation of powdered bones having both protein and calcium from fresh fish body | |
| JPH03109210A (en) | Production of natural hydroxyapatite(hap), and production of source material for hap | |
| JPS61115458A (en) | Preparation of powdery protein food utilizing bean curd refuse | |
| JPH06305870A (en) | Treatment of waste blood of livestock, etc. | |
| KR102249137B1 (en) | A Method of Synthesis of Hydroxyapatite from Bio-waste Eggshells via Ultra-sonication and Use of Hydroxyapatite therefrom | |
| JP2006240976A (en) | Method for manufacturing phosphorus-calcium composite material, and phosphorus-calcium composite material as well as heavy metal scavenger using phosphorus-calcium composite material | |
| KR870000954B1 (en) | Manufacturing method of natural organic fertilizer | |
| US5776843A (en) | Process for the production of spongiosa bone ceramic having low calcium oxide content | |
| JPH08104508A (en) | Production of various apatite compound obtained by heat treatment, alkali treatment and acid-alkali treatment using scale of fish as starting material |