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JPS6237005B2 - - Google Patents
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JPS6237005B2 - - Google Patents

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Publication number
JPS6237005B2
JPS6237005B2 JP56109263A JP10926381A JPS6237005B2 JP S6237005 B2 JPS6237005 B2 JP S6237005B2 JP 56109263 A JP56109263 A JP 56109263A JP 10926381 A JP10926381 A JP 10926381A JP S6237005 B2 JPS6237005 B2 JP S6237005B2
Authority
JP
Japan
Prior art keywords
dicalcium phosphate
crystals
reaction
phosphate dihydrate
solution
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.)
Expired
Application number
JP56109263A
Other languages
Japanese (ja)
Other versions
JPS5815014A (en
Inventor
Hiromi Sasaki
Tadashi Tanaka
Hiromi Kawamoto
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.)
Central Glass Co Ltd
Original Assignee
Central Glass 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 Central Glass Co Ltd filed Critical Central Glass Co Ltd
Priority to JP10926381A priority Critical patent/JPS5815014A/en
Publication of JPS5815014A publication Critical patent/JPS5815014A/en
Publication of JPS6237005B2 publication Critical patent/JPS6237005B2/ja
Granted legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61QSPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q11/00Preparations for care of the teeth, of the oral cavity or of dentures; Dentifrices, e.g. toothpastes; Mouth rinses
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/19Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
    • A61K8/24Phosphorous; Compounds thereof

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Birds (AREA)
  • Epidemiology (AREA)
  • Oral & Maxillofacial Surgery (AREA)
  • Cosmetics (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は歯磨用に好適なリン酸二石灰2水塩
(分子式、CaHPO4・2H2O)組成物、およびそれ
を製造する方法に関するものである。 従来、リン酸二石灰2水塩はリン酸液とカルシ
ウム塩を反応させる直接法およびアルカリ金属リ
ン酸塩とカルシウム塩の水溶液反応による複分解
法の二方法により製造されている。後者の複分解
法によるリン酸二石灰の製造法として、例えば特
公昭45−8643号公報の方法で製造したリン酸二石
灰2水塩の結晶は扁平晶で厚みが1〜2μと薄
く、このものを粉砕して歯磨基剤として用いた場
合、嵩比重は0.6g/cc以下と小さいため、ダイ
ラタントの性質が現われる上、研磨性が劣るとい
う欠点があつた。 一方、嵩比重があまり大きいと練り上り製品の
肌が汚なくなるため、一般的に歯磨用リン酸二石
灰2水塩の嵩比重は0.7〜1.0g/ccの範囲が好ま
しいとされており、従来は原料リン酸カルシウム
の大きさ、粉砕方式及び分級等によつて調整して
いる。 本発明者等は歯磨用基材として好適な物性を有
するリン酸二石灰2水塩について研究を重ねた結
果、アルカリ金属リン酸塩とカルシウム塩との反
応により得られるリン酸二石灰2水塩の嵩比重お
よび研磨性は、リン酸二石灰2水塩粒子の形状に
左右されるところが大であることを見出し、あわ
せて上記アルカリ金属リン酸塩とカルシウム塩を
反応温度40℃以下にて反応させてリン酸二石灰2
水塩を製造する際、リン酸二石灰2水塩の形状と
して、PH2.5〜3.5では柱状晶〜板状晶が、またPH
3.5〜5.0では扁平晶が得られることを見出したも
のである。このたび、本発明者等はこの柱状晶〜
板状晶と扁平晶との混合物が、歯磨用としてすぐ
れていることを見出し、本発明に到達したもので
ある。 すなわち、本発明は柱状晶〜板状晶のリン酸二
石灰・2水塩および扁平晶のリン酸二石灰・2水
塩の混合物を含む、歯磨用リン酸二石灰・2水塩
組成物に関する。上記柱状晶〜板状晶は厚み10〜
15μm、扁平晶は厚み1〜2μmのものを指し、
これらは前記のようにアルカリ金属リン酸塩とカ
ルシウム塩の40℃以下での反応において、各々、
PH2.5〜3.5、PH3.5〜5.0とすることによつて得ら
れる。柱状〜板状晶と扁平晶との混合比は5:5
〜9:1の範囲が好ましく、より好ましくは6:
4〜8:2である。本発明者等はまた、上記リン
酸二石灰・2水塩の柱状〜板状晶と扁平晶に混合
物が、上記の如く、各々の形状の結晶を別個につ
くつて混合する他に、アルカリ金属リン酸塩とカ
ルシウム塩とから一連の方法で好適に製造される
ことを見出した。すなわち、アルカリ金属リン酸
塩とカルシウム塩を反応温度40℃以下にて、第一
段でPHを2.5〜3.5にて反応させ、第2段でアルカ
リ物質を添加してPHを3.5〜5.0とするものであ
る。該反応の第1段と第2段のPHを調整すること
により、柱状〜板状晶と扁平晶の混合比を適宜、
調整することができる。 本発明反応をより具体的に説明すると、アルカ
リ金属リン酸塩とカルシウム塩との溶液反応にお
いて、第1段階では鉱酸などの酸を添加してPHを
2.5〜3.5に調節し、撹拌機で撹拌しながら反応を
行なわせる。このときの反応温度は40℃以下に保
つのが好ましい。複分解反応が進行してリン酸二
石灰2水塩結晶が生成して反応が完了すると、第
2段階としてアルカリ物質を添加してスラリーの
PHを3.5〜5.0に上昇せしめ、リン酸二石灰2水塩
の溶解度を減少せしめ、更にリン酸二石灰2水塩
の結晶を析出させる。その後、第1段階、第2段
階にて析出したリン酸二石灰2水塩結晶を通常の
分離手段、例えば過機にて分離した後、乾燥を
行なう。このようにして得られるリン酸二石灰2
水塩は、第1段階にて析出する柱状〜板状晶と、
第2段階にて析出する扁平晶が混り合つたもの
で、平均的には厚みが5〜10μm、嵩比重が0.85
g/cc程度であり、研磨力、練り特性共に極めて
優れたものである。 本発明方法での反応条件で重要な因子は反応PH
と温度である。アルカリ金属リン酸塩とカルシウ
ム塩との溶液反応でのPHについては、第1反応槽
は2.5〜3.5の範囲が適当で、これ以下にすると第
1反応槽で生成するリン酸二石灰2水塩の溶解度
が増加し、第2反応槽でPHを3.5〜5.0にした時晶
出する扁平晶が多くなる為、歯磨特性が悪くな
る。一方、反応PH3.5以上にすると扁平晶ばかり
となり、前記同様、歯磨特性が悪くなる。従つ
て。第1反応槽のPH範囲は2.5〜3.5で好ましくは
2.7〜3.2である。次に、第2反応槽でのPH範囲は
3.5〜5.0であり、5.0以上にするとカルシウムアパ
タイトが一部生成する為、歯磨特性が非常に悪く
なる。又、反応PH4.5〜5.0の範囲でも局部的にア
ルカリ物質を添加するとカルシウムアパタイトが
一部生成するが、このアルカリ物質の添加を反応
槽全体に噴霧する等の工夫をすればカルシウムア
パタイトの生成を防ぐ事が出来る。従つて第2反
応槽のPH範囲は3.5〜5.0で好ましくは4.0〜4.5で
ある。反応温度については、40℃を越えるとリン
酸二石灰の無水塩が生成する。特に、第1反応槽
のPHを3.0以下で反応を行なう時は、温度は35℃
以下で行なわなければならない。一方、反応PH
3.0以上だと40℃以下で行なえば良い。 本発明方法においては反応をPH2.5〜3.5で行な
わせて、柱状〜板状晶を晶出させた後、アルカリ
物質を用いてスラリーPHを3.5〜5.0に上昇させる
ことによりスラリー中に溶解しているリン酸二石
灰の2水塩の扁平晶を晶出させる。このようにし
て主として板状〜柱状晶からなる扁平晶の混つた
リン酸二石灰・2水塩が得られる。その混合比は
第1および第2段のPHによつて柱〜板状晶:扁平
晶≒5:5〜9:1のものが得られるが、例えば
第1段にてPHを2.7、第2段にてPHを4.2に調節し
た場合で、柱状〜板状晶:扁平晶=8:2程度で
ある。 本発明の柱状〜板状晶と扁平晶の混つたリン酸
二石灰・2水塩組成物を原料として歯磨とした場
合、扁平晶ばかりのリン酸二石灰・2水塩とは異
なり練り特性も良好で、しかも研磨性も非常に優
れたものであつた。またPH2.5〜3.5で晶出した柱
状〜板状結晶のリン酸二石灰2水塩のみの場合
は、研磨性は優れているものの練り特性が悪く、
グリセリン等と練つたとき肌が粗く、しかも初期
の混合性が悪いものであつた。 このように本発明は夫々異なる結晶形状のリン
酸二石灰・2水塩を混合、混成させることによ
り、研磨性、練り特性共に良好な、歯磨に適した
ものが得られるものである。 なお本発明のPH2段階調整によりリン酸二石灰
2水塩組成物を連続的に得ようとした場合には第
1第2の反応槽でそれぞれPHを調整するものであ
るが、もちろんバツチ操作にても適用しうるもの
である。 上記のようにPHを2段階調整することにより、
柱状晶〜板状晶と扁平晶の混在したリン酸二石
灰・2水塩組成物を好適に得ることができるが、
前記の如く、勿論、それぞれのPHで別個に反応を
行なつてそれぞれの結晶形状のものを得、これを
適当な混合比にて混合し歯磨用基材とすることも
可能で、この場合の混合物の物性は、上記一連の
二段階反応で得たものと同程度となるが、個別に
製造して混合する方式は工程が煩雑となり経済的
でないという難点がある。 本発明で用いられるアルカリ金属リン酸塩とし
ては、リン酸ソーダ、リン酸カリ、リン酸アンモ
ニウムナトリウム、リン酸アンモニウムカリウ
ム、リン酸リチウム等があり、カルシウム塩とし
ては塩化カルシウム、硝酸カルシウム、消石灰、
炭酸カルシウム等が用いられる。 実施例 1 湿式リン酸より製造したリン酸水素アンモニウ
ムナトリウム(以下リン塩とする)を7%P2O5
になる様に温水で希釈したリン塩溶液と20%
CaCl2溶液をCa/Pモル比1.10、反応温度30℃で
連続的に第1反応槽に添加し、同時に35%HCl溶
液を反応PHが2.7になる様に調節しながら加え、
さらに第2反応槽では20%Ca(OH)2スラリーで
PH4.3に調節し、連続的にリン酸二石灰2水塩の
スラリーを得る。そして、母液から分離、洗浄、
脱水して50℃で乾燥した。このものは厚みが平均
10〜15μm程度の厚い柱状〜板状晶がほとんど
で、若干の1〜2μm程度の厚みの扁平晶が存在
するものであつた。このものの柱状〜板状晶:扁
平晶は8:2程度である。この顕微鏡写真を第1
図に示す。 実施例 2 14%P2O5リン塩溶液と14%CaCl2溶液をCa/P
モル比1.10、反応温度30℃で連続的に第1反応槽
に添加し、同時に35%HCl溶液で反応PHが2.7に
なる様に加え、さらに第2反応槽では20%NaOH
溶液でPH4.5に調節しながら連続的にリン酸二石
灰2水塩のスラリーを得る。以下、実施例1と同
様な操作を行なつた。このものの混合比は8:2
程度であつた。 実施例 3 14%P2O5リン塩溶液と14%CaCl2溶液をCa/P
モル比1.00、反応温度35℃で連続的に第1反応槽
に添加し、同時に35%HCl溶液で反応PHが3.3に
なる様に加え、さらに第2反応槽では20%Ca
(OH)2スラリーでPHが4.3になる様に添加し、連
続的にリン酸二石灰2水塩スラリーを得る。以
下、実施例1と同様な操作を行なつた。このもの
の混合比は6:4程度であつた。 実施例 4 25%リン酸−水素アンモニウム溶液と10%
CaCl2溶液をCa/Pモル比1.0、反応温度35℃で
連続的に第1反応槽に添加し、同時に35%HCl溶
液で反応PHが3.0になる様に加え、さらに第2反
応槽では30%NaOH溶液でPH4.0に調節しながら
連続的にリン酸二石灰2水塩のスラリーを得る。
以下、実施例1と同様な操作を行なつた。このも
のの混合比は7:3であつた。 実施例 5 10%リン酸水素二ナトリウム溶液と10%炭酸カ
ルシウムスラリーをCa/Pモル比1.2、反応温度
32℃で連続的に第1反応槽に添加し、同時に35%
HCl溶液で反応PHが2.6になる様に加え、さらに
第2反応槽では30%NaOH溶液でPH4.3に調節し
ながら連続的にリン酸二石灰2水塩のスラリーを
得る。以下、実施例1と同様な操作を行なつた。
このものの混合比は8:2であつた。 実施例 6 20%リン酸水素二ナトリウム溶液と10%硝酸カ
ルシウム溶液を、Ca/Pモル比1.1、反応温度35
℃で連続的に第1反応槽に添加し、同時に35%
HCl溶液で反応PH3.0になる様に加え、さらに第
2反応槽では10%Ca(OH)2スラリーでPH4.5に調
節しながら連続的にリン酸二石灰2水塩のスラリ
ーを得る。以下、実施例1と同様な操作を行なつ
た。このものの混合比は7:3であつた。 実施例 7 リン塩を7%P2O5となる様に温水で希釈した
リン塩溶液と20%CaCl溶液をCa/Pモル比
1.10、反応温度30℃で連続的に反応槽に添加す
る。同時に35%HCl溶液を反応PHが2.7になるよ
うに調節しながら加えて、連続的にリン酸二石灰
2水塩のスラリーを得る。そして母液から分離、
洗浄、脱水して50℃で乾燥した。更にリン酸二石
灰2水塩を分離した母液と20%Ca(OH)2スラリ
ーを連続的に反応槽に添加する。このときの20%
Ca(OH)2はPH4.3になる様に添加し連続的にリン
酸二石灰2水塩のスラリーを得た。そしてリン酸
二石灰2水塩を分離、洗浄、脱水して50℃で乾燥
した。前者、後者のリン酸二石灰2水塩を7:3
の比率で配合し、V型混合機でよく混合した。 比較例 1 14%P2O5リン塩溶液と14%CaCl2溶液をCa/P
モル比1.10、反応温度30℃で反応槽に加え、同時
に35%HCl溶液で反応PHが2.7になる様に加え、
連続的にリン酸二石灰2水塩スラリーを得る。次
に母液を分離、洗浄、脱水して50℃で乾燥した。
このものは平均厚み10〜15μm程度の厚みを有す
る柱状〜板状晶のみであつた。この顕微鏡写真を
第2図に示す。 比較例 2 比較例1と同様の操作で反応PHは4.5とした。
得られた結晶は平均厚み1〜2μm程度の扁平晶
のみであつた、この顕微鏡写真を第3図に示す。 比較例 3 25%リン酸−水素アンモニウム溶液と10%
CaCl2溶液をCa/Pモル比1.0、反応温度35℃で
反応槽に加え、同時に35%HCl溶液で反応PHが
3.0になる様に加え、連続的にリン酸二石灰2水
塩スラリーを得る。次に母液を分離、洗浄、脱水
して50℃で乾燥した。 比較例 4 比較例3と同様の操作で反応PHは4.0とした。 比較例 5 10%リン酸水素二ナトリウム溶液と10%炭酸カ
ルシウムスラリーをCa/Pモル比1.2、反応温度
32℃で連続的に反応槽に加え、同時に35%HCl溶
液で反応PHが2.6になる様に加え、連続的にリン
酸二石灰2水塩スラリーを得る。次に母液を分
離、洗浄、脱水して50℃で乾燥した。 比較例 6 比較例5と同様の操作で反応PHは4.3とした。 比較例 7 リン塩を7%P2O5となる様に温水で希釈した
リン塩溶液と20%CaCl2溶液をCa/Pモル比
1.10、反応温度30℃で連続的に第1反応槽に添加
し、同時に35%HCl溶液を反応PHが2.0になるよ
うに調節しながら加え、更に第2反応槽では20%
Ca(OH)2スラリーでPHを4.5に調節し、連続的に
リン酸二石灰2水塩のスラリーを得る。母液分離
のために真空過機を使用したが、結晶が非常に
微細なために過に極めて長時間を要した。結晶
は50℃にて脱水した。分析の結果、無水リン酸二
石灰は35%生成していた。 以上の実施例及び比較例で−製造したリン酸二
石灰2水塩を擂潰機で粉砕、350#パスしたもの
を試料とし、次に示す物性試験を行なつた。 (a) 平均粒径……空気透過法による。 (b) 嵩比重……細川鉄工所製パウダーテスターを
用い、タツピング回数50回後の測定値。 (c) 分散性……試料と80%グリセリンのベースト
を作り、JISK−5101のグラインドメーターを
用い測定。 (d) 練りの状態……試料と80%グリセリンを絞つ
時の状態。 (e) 吸油量……試料30gを80%グリセリンで練
り、一定の粘度になつた時のグリセリン量。 (f) 研磨力……試料を30%グリセリン溶液に懸濁
させ、懸濁液中で硬度一定の歯刷子を用いAl
片を一定時間研磨した際の減量。 この結果を第1表に示す。 また実施例1、比較例1、2の生成物それぞれ
を擂潰機にて粉砕、350#パスしたものの顕微鏡
写真を各々、第4,5,6図に示す。
The present invention relates to a dicalcium phosphate dihydrate (molecular formula: CaHPO 4 .2H 2 O) composition suitable for tooth brushing, and a method for producing the same. Conventionally, dicalcium phosphate dihydrate has been produced by two methods: a direct method in which a phosphoric acid solution and a calcium salt are reacted, and a double decomposition method in which an alkali metal phosphate and a calcium salt are reacted in an aqueous solution. As a method for producing dicalcium phosphate using the latter double decomposition method, for example, the crystals of dicalcium phosphate dihydrate produced by the method disclosed in Japanese Patent Publication No. 45-8643 are oblate crystals with a thickness of 1 to 2 μm. When crushed and used as a toothpaste base, the bulk specific gravity is as small as 0.6 g/cc or less, so it exhibits dilatant properties and has the disadvantage of poor abrasiveness. On the other hand, if the bulk specific gravity is too high, the kneaded product will not stain the skin, so it is generally said that the preferred bulk specific gravity of dicalcium phosphate dihydrate for toothpaste is in the range of 0.7 to 1.0 g/cc. is adjusted by the size of the raw material calcium phosphate, grinding method, classification, etc. As a result of repeated research on dicalcium phosphate dihydrate, which has physical properties suitable as a toothpaste base material, the present inventors found that dicalcium phosphate dihydrate obtained by the reaction of an alkali metal phosphate and a calcium salt. It was discovered that the bulk specific gravity and abrasiveness of dicalcium phosphate were largely influenced by the shape of the dicalcium phosphate dihydrate particles, and that the above-mentioned alkali metal phosphate and calcium salt were reacted at a reaction temperature of 40°C or less. dicalcium phosphate 2
When producing water salt, the shape of dicalcium phosphate dihydrate is columnar to plate crystal at pH 2.5 to 3.5, and
It was found that flat crystals can be obtained in the range of 3.5 to 5.0. The present inventors have recently discovered that this columnar crystal ~
It was discovered that a mixture of plate crystals and flat crystals is excellent for toothpaste, and the present invention was developed based on this discovery. That is, the present invention relates to a dicalcium phosphate dihydrate composition for toothpaste containing a mixture of columnar to plate-like dicalcium phosphate dihydrate and flat crystal dicalcium phosphate dihydrate. . The thickness of the above columnar crystals to plate crystals is 10~
15 μm, flat crystals are 1 to 2 μm thick,
As mentioned above, in the reaction of alkali metal phosphate and calcium salt at below 40℃,
Obtained by adjusting the pH to 2.5 to 3.5 and 3.5 to 5.0. The mixing ratio of columnar to plate crystals and flat crystals is 5:5
The range is preferably 9:1, more preferably 6:1.
The ratio is 4 to 8:2. The present inventors have also discovered that a mixture of columnar to plate-like crystals and flat crystals of dicalcium phosphate dihydrate can be obtained by separately producing crystals of each shape as described above and mixing them. It has been found that it can be suitably produced from a phosphate and a calcium salt by a series of methods. That is, an alkali metal phosphate and a calcium salt are reacted at a reaction temperature of 40° C. or less at a pH of 2.5 to 3.5 in the first stage, and an alkali substance is added in the second stage to adjust the pH to 3.5 to 5.0. It is something. By adjusting the pH of the first and second stages of the reaction, the mixing ratio of columnar to plate crystals and flat crystals can be adjusted as appropriate.
Can be adjusted. To explain the reaction of the present invention more specifically, in the solution reaction between an alkali metal phosphate and a calcium salt, in the first step, an acid such as a mineral acid is added to adjust the pH.
Adjust the temperature to 2.5 to 3.5 and allow the reaction to proceed while stirring with a stirrer. The reaction temperature at this time is preferably kept at 40°C or lower. When the metathesis reaction progresses and dicalcium phosphate dihydrate crystals are formed and the reaction is completed, an alkaline substance is added in the second step to make the slurry.
The pH is raised to 3.5 to 5.0, the solubility of dicalcium phosphate dihydrate is decreased, and crystals of dicalcium phosphate dihydrate are precipitated. Thereafter, the dicalcium phosphate dihydrate crystals precipitated in the first and second stages are separated using a conventional separation means, such as a filter, and then dried. Dicalcium phosphate 2 obtained in this way
Water salt has columnar to plate-like crystals precipitated in the first stage,
It is a mixture of flat crystals precipitated in the second stage, with an average thickness of 5 to 10 μm and a bulk specific gravity of 0.85.
g/cc, and has extremely excellent polishing power and kneading properties. An important factor in the reaction conditions in the method of the present invention is the reaction pH.
and temperature. Regarding the pH in the solution reaction between alkali metal phosphate and calcium salt, a range of 2.5 to 3.5 is appropriate for the first reaction tank; if the pH is lower than this, the dicalcium phosphate dihydrate produced in the first reaction tank is The solubility of the tooth powder increases, and when the pH is set to 3.5 to 5.0 in the second reaction tank, more flat crystals crystallize, resulting in poor tooth brushing properties. On the other hand, if the reaction pH is 3.5 or higher, the crystals become mostly oblate crystals, and the dentifrice properties deteriorate as described above. Follow. The pH range of the first reaction tank is preferably 2.5 to 3.5.
It is 2.7-3.2. Next, the PH range in the second reaction tank is
It is 3.5 to 5.0, and if it is over 5.0, some calcium apatite will be generated, resulting in very poor tooth brushing properties. In addition, even if the reaction pH is within the range of 4.5 to 5.0, some calcium apatite will be produced if an alkaline substance is added locally, but if the addition of this alkaline substance is sprayed over the entire reaction tank, calcium apatite will be formed. can be prevented. Therefore, the pH range of the second reaction tank is 3.5 to 5.0, preferably 4.0 to 4.5. Regarding the reaction temperature, when it exceeds 40°C, anhydrous salt of dicalcium phosphate is produced. In particular, when performing the reaction at a pH of 3.0 or less in the first reaction tank, the temperature should be 35℃.
The following must be done. On the other hand, the reaction PH
If it is 3.0 or higher, it should be done at 40℃ or below. In the method of the present invention, the reaction is carried out at a pH of 2.5 to 3.5 to crystallize columnar to plate-shaped crystals, and then the slurry is dissolved in the slurry by raising the slurry pH to 3.5 to 5.0 using an alkaline substance. Crystallizes oblate crystals of dihydrate dicalcium phosphate. In this way, dicalcium phosphate dihydrate containing flat crystals mainly consisting of plate-shaped to columnar crystals is obtained. Depending on the pH of the first and second stages, a mixture ratio of columnar to plate crystals: flat crystals ≒ 5:5 to 9:1 can be obtained. When the pH is adjusted to 4.2 in the step, the ratio of columnar to plate crystals: flat crystals is about 8:2. When the dicalcium phosphate dihydrate composition of the present invention containing columnar to plate-like crystals and flat crystals is used as a toothpaste as a raw material, unlike dicalcium phosphate dihydrate, which has only flat crystals, it has good kneading properties. The polishing properties were good, and the polishability was also very excellent. In addition, in the case of only dicalcium phosphate dihydrate in columnar to plate-like crystals crystallized at pH 2.5 to 3.5, the polishing properties are excellent, but the kneading properties are poor.
When kneaded with glycerin etc., the texture was rough and the initial mixability was poor. As described above, in the present invention, by mixing and blending dicalcium phosphate dihydrate having different crystal shapes, a product suitable for tooth brushing and having good polishing properties and kneading properties can be obtained. In addition, when attempting to continuously obtain the dicalcium phosphate dihydrate composition by the two-step pH adjustment of the present invention, the pH is adjusted in the first and second reaction tanks, respectively, but of course, batch operation is not required. It can also be applied. By adjusting the pH in two stages as described above,
A dicalcium phosphate dihydrate composition containing a mixture of columnar crystals to plate crystals and flat crystals can be suitably obtained, but
As mentioned above, of course, it is also possible to carry out the reaction separately at each pH to obtain each crystal shape, and then mix them at an appropriate mixing ratio to make a toothpaste base material. The physical properties of the mixture are comparable to those obtained by the series of two-step reactions described above, but the method of individually producing and mixing them has the disadvantage that the process is complicated and uneconomical. Alkali metal phosphates used in the present invention include sodium phosphate, potassium phosphate, sodium ammonium phosphate, potassium ammonium phosphate, lithium phosphate, etc., and calcium salts include calcium chloride, calcium nitrate, slaked lime,
Calcium carbonate etc. are used. Example 1 Sodium ammonium hydrogen phosphate (hereinafter referred to as phosphorus salt) produced from wet phosphoric acid was added to 7% P 2 O 5
Phosphate salt solution diluted with warm water to give 20%
A CaCl 2 solution was continuously added to the first reaction tank at a Ca/P molar ratio of 1.10 and a reaction temperature of 30°C, and at the same time, a 35% HCl solution was added while adjusting the reaction pH to 2.7.
Furthermore, in the second reaction tank, 20% Ca(OH) 2 slurry was added.
Adjust the pH to 4.3 and continuously obtain a slurry of dicalcium phosphate dihydrate. Then, it is separated from the mother liquor, washed,
It was dehydrated and dried at 50°C. This one has an average thickness
Most of the crystals were columnar to plate-like crystals with a thickness of about 10 to 15 μm, and some flat crystals with a thickness of about 1 to 2 μm were present. The ratio of columnar to plate-like crystals to flat crystals is about 8:2. This micrograph is the first
As shown in the figure. Example 2 14% P 2 O 5 phosphorus salt solution and 14% CaCl 2 solution were mixed with Ca/P
Continuously added to the first reaction tank at a molar ratio of 1.10 and a reaction temperature of 30°C, simultaneously added 35% HCl solution to make the reaction pH 2.7, and further added 20% NaOH to the second reaction tank.
A slurry of dicalcium phosphate dihydrate is continuously obtained while adjusting the pH to 4.5 with a solution. Hereinafter, the same operations as in Example 1 were performed. The mixing ratio of this is 8:2
It was moderately hot. Example 3 14% P 2 O 5 phosphorus salt solution and 14% CaCl 2 solution were mixed with Ca/P
It was added continuously to the first reaction tank at a molar ratio of 1.00 and a reaction temperature of 35°C, and at the same time, 35% HCl solution was added so that the reaction pH was 3.3, and in the second reaction tank, 20% Ca was added.
(OH) 2 is added to the slurry so that the pH becomes 4.3 to continuously obtain dicalcium phosphate dihydrate slurry. Hereinafter, the same operations as in Example 1 were performed. The mixing ratio of this product was about 6:4. Example 4 25% phosphoric acid-ammonium hydrogen solution and 10%
A CaCl 2 solution was continuously added to the first reaction tank at a Ca/P molar ratio of 1.0 and a reaction temperature of 35°C, and at the same time, a 35% HCl solution was added so that the reaction pH was 3.0. % NaOH solution to continuously obtain a slurry of dicalcium phosphate dihydrate while adjusting the pH to 4.0.
Hereinafter, the same operations as in Example 1 were performed. The mixing ratio of this was 7:3. Example 5 10% disodium hydrogen phosphate solution and 10% calcium carbonate slurry at Ca/P molar ratio 1.2 and reaction temperature
Continuously added to the first reaction tank at 32℃, simultaneously 35%
A slurry of dicalcium phosphate dihydrate is continuously obtained by adding HCl solution so that the reaction pH becomes 2.6, and further adjusting the pH to 4.3 with 30% NaOH solution in the second reaction tank. Hereinafter, the same operations as in Example 1 were performed.
The mixing ratio of this was 8:2. Example 6 A 20% disodium hydrogen phosphate solution and a 10% calcium nitrate solution were mixed at a Ca/P molar ratio of 1.1 and a reaction temperature of 35
℃ continuously added to the first reaction tank and simultaneously 35%
A HCl solution is added to adjust the reaction pH to 3.0, and in the second reaction tank, a 10% Ca(OH) 2 slurry is added to adjust the pH to 4.5 to continuously obtain a slurry of dicalcium phosphate dihydrate. Hereinafter, the same operations as in Example 1 were performed. The mixing ratio of this was 7:3. Example 7 A phosphorus salt solution prepared by diluting phosphorus salt with warm water to give a concentration of 7% P 2 O 5 and a 20% CaCl solution were mixed at a Ca/P molar ratio.
1.10, continuously added to the reaction tank at a reaction temperature of 30℃. At the same time, 35% HCl solution is added while adjusting the reaction pH to 2.7 to continuously obtain a slurry of dicalcium phosphate dihydrate. and separated from the mother liquor,
It was washed, dehydrated, and dried at 50°C. Further, a mother liquor from which dicalcium phosphate dihydrate was separated and a 20% Ca(OH) 2 slurry are continuously added to the reaction tank. 20% at this time
Ca(OH) 2 was added to adjust the pH to 4.3 to continuously obtain a slurry of dicalcium phosphate dihydrate. Then, dicalcium phosphate dihydrate was separated, washed, dehydrated, and dried at 50°C. The former and the latter dicalcium phosphate dihydrate at a ratio of 7:3
They were mixed well using a V-type mixer. Comparative example 1 14% P 2 O 5 phosphorus salt solution and 14% CaCl 2 solution were mixed with Ca/P
Add it to the reaction tank at a molar ratio of 1.10 and a reaction temperature of 30℃, and at the same time add 35% HCl solution so that the reaction pH becomes 2.7.
Continuously obtain dicalcium phosphate dihydrate slurry. The mother liquor was then separated, washed, dehydrated and dried at 50°C.
This material consisted of only columnar to plate crystals having an average thickness of about 10 to 15 μm. This micrograph is shown in FIG. 2. Comparative Example 2 The reaction pH was set to 4.5 using the same procedure as in Comparative Example 1.
The obtained crystals were only flat crystals with an average thickness of about 1 to 2 μm. A micrograph of this is shown in FIG. 3. Comparative Example 3 25% phosphoric acid-ammonium hydrogen solution and 10%
Add CaCl 2 solution to the reaction tank at a Ca/P molar ratio of 1.0 and a reaction temperature of 35℃, and at the same time adjust the reaction pH with 35% HCl solution.
3.0 to obtain a continuous slurry of dicalcium phosphate dihydrate. The mother liquor was then separated, washed, dehydrated and dried at 50°C. Comparative Example 4 The reaction pH was set to 4.0 using the same procedure as in Comparative Example 3. Comparative Example 5 10% disodium hydrogen phosphate solution and 10% calcium carbonate slurry at Ca/P molar ratio 1.2 and reaction temperature
Continuously add it to the reaction tank at 32°C, and at the same time add 35% HCl solution so that the reaction pH becomes 2.6 to continuously obtain dicalcium phosphate dihydrate slurry. The mother liquor was then separated, washed, dehydrated and dried at 50°C. Comparative Example 6 The reaction pH was set to 4.3 using the same procedure as in Comparative Example 5. Comparative Example 7 A phosphorus salt solution prepared by diluting phosphorus salt with warm water to give a concentration of 7% P 2 O 5 and a 20% CaCl 2 solution were mixed at different Ca/P molar ratios.
1.10, continuously added to the first reaction tank at a reaction temperature of 30℃, and simultaneously added 35% HCl solution while adjusting the reaction pH to 2.0, and further added 20% to the second reaction tank.
Adjust the pH to 4.5 with Ca(OH) 2 slurry to obtain a slurry of dicalcium phosphate dihydrate continuously. A vacuum filtration machine was used to separate the mother liquor, but it took an extremely long time because the crystals were very fine. The crystals were dehydrated at 50°C. As a result of analysis, 35% of anhydrous dicalcium phosphate was produced. The dicalcium phosphate dihydrate produced in the above Examples and Comparative Examples was crushed in a crusher and passed 350 # as a sample, and the following physical property tests were conducted. (a) Average particle size...by air permeation method. (b) Bulk specific gravity: Measured value after 50 tappings using a powder tester manufactured by Hosokawa Iron Works. (c) Dispersibility...Made a base of the sample and 80% glycerin and measured using a JISK-5101 grind meter. (d) Condition of kneading... Condition when squeezing the sample and 80% glycerin. (e) Oil absorption amount...Amount of glycerin when 30g of sample is kneaded with 80% glycerin to reach a constant viscosity. (f) Polishing power...The sample was suspended in a 30% glycerin solution, and a toothbrush of constant hardness was used to polish the Al
Weight loss when a piece is polished for a certain period of time. The results are shown in Table 1. Further, micrographs of the products of Example 1 and Comparative Examples 1 and 2, which were crushed using a crusher and passed through a 350# crusher, are shown in Figures 4, 5, and 6, respectively.

【表】【table】

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

第1〜第3図は本発明および比較例のリン酸二
石灰2水塩の顕微鏡写真であり、第4〜6図は
各々第1〜3図のものの粉砕後の写真である。
Figures 1 to 3 are microscopic photographs of dicalcium phosphate dihydrate of the present invention and comparative examples, and Figures 4 to 6 are photographs of the materials in Figures 1 to 3 after pulverization, respectively.

Claims (1)

【特許請求の範囲】 1 板状〜柱状晶のリン酸二石灰2水塩と、扁平
晶のリン酸二石灰2水塩との比率が5:5〜9:
1である混合物からなる歯磨用リン酸二石灰2水
塩組成物。 2 アルカリ金属リン酸塩とカルシウム塩を反応
温度40℃以下にて、第1段でPHを2.5〜3.5にて反
応させ、第2段でPHを第1段より上昇せしめて
3.5〜5.0として、得られる結晶と分離することを
特徴とする、板状〜柱状晶のリン酸二石灰2水塩
と扁平晶のリン酸二石灰2水塩との混合物からな
る歯磨用リン酸二石灰2水塩組成物の製造方法。
[Scope of Claims] 1. The ratio of plate-like to columnar crystal dicalcium phosphate dihydrate to flat crystal dicalcium phosphate dihydrate is 5:5 to 9:
A dentifrice dicalcium phosphate dihydrate composition comprising a mixture of 1. 2. React the alkali metal phosphate and calcium salt at a reaction temperature of 40°C or less at a pH of 2.5 to 3.5 in the first stage, and raise the pH in the second stage from the first stage.
Phosphoric acid for toothpaste consisting of a mixture of dicalcium phosphate dihydrate in plate-like to columnar crystals and dicalcium phosphate dihydrate in flat crystals, characterized in that it separates from the crystals obtained as 3.5 to 5.0. A method for producing a dicalcium dihydrate composition.
JP10926381A 1981-07-15 1981-07-15 Calcium dihydrogen phosphate dihydrate for toothpaste and its manufacture Granted JPS5815014A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10926381A JPS5815014A (en) 1981-07-15 1981-07-15 Calcium dihydrogen phosphate dihydrate for toothpaste and its manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10926381A JPS5815014A (en) 1981-07-15 1981-07-15 Calcium dihydrogen phosphate dihydrate for toothpaste and its manufacture

Publications (2)

Publication Number Publication Date
JPS5815014A JPS5815014A (en) 1983-01-28
JPS6237005B2 true JPS6237005B2 (en) 1987-08-10

Family

ID=14505732

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Country Link
JP (1) JPS5815014A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2879269B2 (en) * 1991-03-25 1999-04-05 昭和電工株式会社 Ruminant granules
JP5521979B2 (en) * 2009-12-16 2014-06-18 ライオン株式会社 Oral composition and method for stabilizing oral composition containing many oil components
CN108910853B (en) * 2018-09-11 2020-07-31 云南磷化集团有限公司 Method for producing granular calcium dihydrogen phosphate by one-step granulation of concentrated phosphoric acid

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US3066056A (en) * 1959-06-30 1962-11-27 Victor Chemical Works Stabilized dicalcium phosphate dihydrate

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