JPS62867B2 - - Google Patents
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- Publication number
- JPS62867B2 JPS62867B2 JP15488978A JP15488978A JPS62867B2 JP S62867 B2 JPS62867 B2 JP S62867B2 JP 15488978 A JP15488978 A JP 15488978A JP 15488978 A JP15488978 A JP 15488978A JP S62867 B2 JPS62867 B2 JP S62867B2
- Authority
- JP
- Japan
- Prior art keywords
- gypsum
- calcium silicate
- silicate
- petal
- molar ratio
- 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
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Description
本発明は、石膏と珪酸アルカリから非常に大き
な嵩容積及び吸油量をもつ花弁状集合体構造の珪
酸カルシウムまたは珪酸カルシウム―石膏複合体
の製造方法に係る。
従来、珪酸カルシウムの製造方法に関する研究
は古くから行なわれ、特に建材用としてのトバモ
ライト、ゾーノトライトの研究が多い。本発明者
等は、先に珪酸アルカリ(sio2/R2O(但しRは
NaまたはKである)モル比1.55〜6.5)と水溶性
カルシウム化合物とを150〜250℃の温度下に、且
つ溶媒比が得られる珪酸カルシウムに対して5〜
100重量部の範囲で反応させ、一般式
2CaO・3siO2・nSiO2・mH2O ……(A)
(但し、n,mは正の数でn=0.1〜10)で示
される花弁状集合体構造(以下単に〓花弁状〓と
も称する)の珪酸カルシウムが得られることを見
い出し、Na特願昭52−160031号として提案し
た。
上記一般式(A)で示される珪酸カルシウムはジヤ
イロライト型珪酸カルシウム即ち2CaO・
3SiO2・2H2Oと無定形2酸化珪素即ちnSiO2・
mH2Oで構成されるが無定形2酸化珪素は単なる
ブレンド形状ではなくジヤイロライト型珪酸カル
シウムの生成時に無定形2酸化珪素を含有してな
るものである。ジヤイロライト型珪酸カルシウム
と無定形2酸化珪酸とを機械的に混合しても前記
したような花弁状のものとはなり得ない。この珪
酸カルシウムの形状については電子顕微鏡写真を
とることにより確認出来る。一般には3000〜
10000倍の電子顕微鏡写真で花弁状の形状及び厚
みが鮮明に確認される。花弁の大きさ、形状等は
使用する原料の種類、原料混合比、製造条件等に
よつて異なり一概に限定出来ないが、一般には長
手方向の平均直径が0.1〜30μ、厚みが0.005〜0.1
μ程度の円状、楕円状等をなしたものが多く、就
中バラの花の花弁に類似するものが多い。
しかして、特願昭52−160031号(特公昭60−
29643号公報)で得られる化合物は花弁状即ち、
薄片が一定の方向ではなく多方向に成長した集合
体からなつている。
特願昭52−160031号(特公昭60−29643号公
報)においては、水溶性のカルシウム化合物を原
料として使用することが特徴であつたが、このた
び石膏という水溶性であるが比較的難溶性のカル
シウム化合物を用いても添加順序および添加条件
を選択することによつて、上記(A)式で示されると
同様の花弁状珪酸カルシウム―石膏複合体が得ら
れることを見い出し本発明を完成するに至つた。
本発明は、石膏懸濁液中に珪酸アルカリ
(SiO2/R2O(但しRはNaまたはKである)モル
比1.55〜6.5)(以下単に珪酸アルカリともいう)
溶液を徐々に加え、加圧下で150〜250℃の温度に
加熱処理することを特徴とする花弁状集合体構造
の珪酸カルシウムまたは花弁状集合体構造の珪酸
カルシウム―石膏複合体の製造方法である。
本発明において重要なことは、、石膏懸濁液中
に珪酸アルカリ溶液を添加すること、および該添
加を出来るだけ徐々に行なうことである。このよ
うな配慮のもとに石膏/珪酸アルカリのモル比が
1付近では主として花弁状珪酸カルシウムが、ま
た該モル比が1.1〜1.5においては花弁状の珪酸カ
ルシウム―石膏複合体が得られる。
本発明に使用される原料の珪酸アルカリは、前
記した如く一般式(A)から明らかなように理論的に
SiO2/CaOモル比が1.55〜6.5の範囲である。こ
こでいうSiO2/CaOモル比は過剰の石膏のCaO
は含まない。SiO2/CaOのモル比の制御は、前
記した如く、原料の種類、反応温度、反応時間、
水比等によつて多少異なるので予め生成物中の
SiO2/CaOモル比と原料仕込に於けるSiO2/
CaOモル比との関係を確認して用いるのが好まし
い。一般式には前記一般式で示される珪酸カルシ
ウム中のSiO2/CaOモル比が大きくなると生成
条件によつては花弁状集合体の花弁間に無定形2
酸化珪素が球状にまぶされた形状になる場合があ
るので、種々の条件に応じて予め好適なSiO2/
CaOモル比を定めておくのが好ましい。
上記において原料として使用される珪酸アルカ
リとしては下記示性式R2O・lSiO2(RはNaまた
はK、lは1.5〜6.5)で示されるものを用いるこ
とが好ましく、また石膏および該珪酸アルカリの
使用割合は、石膏/珪酸アルカリのモル比が1.0
〜1.5の範囲が有利である。
本発明においては、まず、石膏は先ず水中に入
れ良く撹拌してスラリーとする。この時のスラリ
ー濃度は、後でも説明するが、低い方が好まし
い。しかし余りに低くしすぎて、最終的に得られ
る珪酸カルシウムに対して、水を100倍重量以上
も加えると得られる珪酸カルシウムは、花弁状と
なり得ず好ましくない。このスラリーに珪酸ナト
リウム、珪酸カリウム等の珪酸アリカリまたはそ
の水溶液を、徐々に一般に大気圧下に添加してス
ラリーとする。ここで重要なのは、添加時間であ
つて、出来るだけゆつくりと加えた方が好まし
い。どの程度の時間が必要かは、石膏の粒度、結
晶形等で一概に限定されるものではないが、一般
には10分以上出来るだけ時間をかけて添加するの
がよい。
珪酸アルカリの添加時間があまりにも短かすぎ
ると花弁状構造をもつ高嵩比容積の珪酸カルシウ
ムあるいは珪酸カルシウム―石膏複合体が生成し
がたく、塊状のものとなりやすいので好ましくな
い。
このように、珪酸アルカリの添加時間が重要と
なる理由については、現在明白ではないが、石膏
は、溶解度が低いものの、溶解速度は比較的大き
く、わずかに溶解した石膏と珪酸アルカリが反応
するとすぐに新たな石膏が溶解してくるため、添
加時間が充分に長いと結果的には水溶性の高いカ
ルシウム化合物と珪酸アルカリとを反応させたこ
とと同一になるのではないかと考えている。逆に
添加時間が短かすぎると、珪酸アルカリと石膏の
反応が、石膏固体上で起り、非常に不均一となつ
て花弁状とはなり得ないと考えている。
又、上記原料成分の添加順序も重要で逆にした
場合、即ち珪酸アルカリまたはその水溶液に石膏
の水性スラリーを添加する場合は、生成する珪酸
カルシウムは花弁状とはなり難い。即ち、珪酸ア
ルカリに石膏スラリーを添加した場合は、添加速
度を十分に遅くした場合でも出来る珪酸カルシウ
ムは大部分花弁状とならず、塊状となる傾向があ
る。
次いで石膏スラリーと珪酸アルカリとの混合物
を150〜250℃で加圧下に、例えばオークレーブを
用いて反応させれば、目的の珪酸カルシウムある
いは珪酸カルシウム−石膏複合体が得られる。
本発明において、花弁状珪酸カルシウムあるい
は珪酸カルシウム一石膏複合体は溶媒と分離する
ことにより得ることが出来るが必要に応じて水洗
し精製することも出来る。このようにして得られ
た花弁状珪酸カルシウムは通常の方法で乾燥しそ
のまま或いは必要に応じて粉砕して製品とすれば
よい。
本発明において、珪酸カルシウムを得る場合に
は、石膏/珪酸アルカリのモル比が1付近になる
ように選べばよく、また、珪酸カルシウム―石膏
複合体を得る場合には該モル比が1.1〜1.5の範囲
になるように選べばよい。常識的には、モル比が
1.0以上の場合、過剰の石膏は全く反応に関与し
ないであろうと、化学反応方程式から考えられる
が、驚くべきことに、過剰に存在する石膏は、得
られた珪酸カルシウム中の単なる不純物としてで
はなく、珪酸カルシウム中にミクロブレンドさ
れ、珪酸カルシウム―石膏複合体となり、10000
倍の電子顕微鏡によつても、珪酸カルシウムと石
膏を区別することは出来ないようになり、しかも
極めて嵩比容積および吸油量の大きいものとなる
ことが判明した。このような現象がなぜ起るの
か、作用機構は明らかではないが、最切に珪酸カ
ルシウムを合成しておき、その後石膏を添加して
オートクレーブ中で水熱処理しても、このような
複合体は得られないことからしても、珪酸カルシ
ウムの結晶成長時に石膏が何らかの関与をしてい
るものではないかと推察している。しかし、モル
比が1.6以上になると、顕微鏡でも明らかに石膏
と珪酸カルシウムが識別できるようになる。
上記した如くして得られる珪酸カルシウム―石
膏複合体は、前記した花弁状高嵩比容積の珪酸カ
ルシウムと同様に吸着担体、ツヤ消し剤および濾
過助剤等の用途に供して優れた性能を発揮する。
本発明を更に詳細に説明するため以下実施例及
び比較例を挙げて説明するが本発明はこれらの実
施例に限定されるものではない。尚以下の実施例
及び比較例に於ける種々の測定値は次のようにし
て求めたものである。
(イ) 嵩比容積
珪酸カルシウムを乳鉢で200メツシユ篩80%通
過粒度まで粉砕した。この粉砕した珪酸カルシウ
ムを用いてJISK6220の6.8項の嵩比重測定方法に
よつて測定した。
(ロ) 吸油量
珪酸カルシウムを乳鉢で200メツシユ篩80%通
過粒度まで粉砕した。この粉砕した珪酸カルシウ
ムを用いてJISK6220の19項の吸油量測定法によ
つて測定した。
実施例 1
4.56gのB型半水石膏(100メツシユ全通)を98
c.c.の水に投じ20分間撹拌する。このスラリーを撹
拌しながら大気圧下25℃で、0.3144モル/lの珪
酸ナトリウム(SiO2/Na2Oモル比2.6)100c.c.を
5c.c./分の速度で20分間かけて加えた。この場合
の仕込CaSO4/Na2O・nSiO2モル比は1.00であつ
た。得られたスラリーをオートクレーブに入れ密
閉し200℃で5時間反応させた。反応物は濾過
し、イオン交換水100c.c.で2回くりかえして水洗
した後、100℃で8時間乾燥した。この乾燥物の
収量は、7.35gであつた。
嵩比容積は21c.c./g、吸油量は、6.3c.c./gで
あつた。尚X線回折の結果、ジヤイロライト型珪
酸カルシウムのパターンを示した。化学分析の結
果は、CaO24.4%、SiO266.2%灼熱減量9.4%であ
つた。
この結果より、前記操作で得られた珪酸カルシ
ウムは2CaO・3SiO2・2.06SiO2・2.39H2Oである
ことがわかつた。電子顕微鏡の10000倍の写真を
第1図に示すが、これより長手方向の平均直径が
約2uで厚みが0.1μ以下の花弁の集合体で構成さ
れていることが確認された。
実施例 2
6.5gの2水石膏(100メツシユ全通)を98c.c.の
水に投じ20分間撹拌する。このスラリーを撹拌し
ながら大気圧下25℃で0.3144モル/lの珪酸ナト
リウム(SiO2/Na2Oモル比2.6)100c.c.を6c.c./
分の速度で16分40秒間かけて加えた。この場合の
仕込CaSO4/Na2O・nSiO2は1.34であつた。その
後の操作は実施例1と同様に実施して8.2gの粉体
を得た。この粉体のX線回折の結果は、型無水
石膏とジヤイロライト型珪酸カルシウムのピーク
が混在していた。化学分析の結果から、(2CaO・
3SiO2・2.05SiO2・2.37H2O)(0.20CaSO4)である
ことが確認された。電子顕微鏡の1万倍の写真を
第2図に示すが、長手方向の直径2μ厚さ0.1u以
下の花弁で構成されていることが確認された。
尚、型無水石膏と思われる結晶は外見上識別出
来なかつた。嵩比容積は、19.5c.c./g吸油量は
63.2c.c./gであつた。
実施例 3
実施例1のB型半水石膏の量、珪酸ナトリウム
のSiO2/CaOモル比、濃度、オートクレーブ反
応温度・反応時間を第1表に示す如く変化させた
以外は、実施例1と同様に処理した。仕込
CaSO4/Na2O・nSiO2はいずれも100であつた。
いずれの場合も花弁状珪酸カルシウムであること
を、X線回折・電子顕微鏡・化学分析によつて確
認した。
結果もあわせて第1表に示す。
The present invention relates to a method for producing calcium silicate or a calcium silicate-gypsum composite having a petal-like aggregate structure and having a very large bulk volume and oil absorption amount from gypsum and an alkali silicate. Research on production methods for calcium silicate has been conducted for a long time, and in particular, there has been much research on tobermorite and zonotrite for use as building materials. The present inventors first developed an alkali silicate (sio 2 /R 2 O (where R is
Na or K) in a molar ratio of 1.55 to 6.5) and a water-soluble calcium compound at a temperature of 150 to 250°C, and the solvent ratio to calcium silicate is 5 to 5.
The reaction was carried out in a range of 100 parts by weight to form a petal-like aggregate represented by the general formula 2CaO・3siO 2・nSiO 2・mH 2 O (A) (where n and m are positive numbers and n=0.1 to 10). It was discovered that calcium silicate having a petal-like structure (hereinafter simply referred to as petal-like) could be obtained, and this was proposed as Na patent application No. 160031/1983. Calcium silicate represented by the above general formula (A) is diairolite type calcium silicate, that is, 2CaO.
3SiO 2 2H 2 O and amorphous silicon dioxide, nSiO 2 .
Amorphous silicon dioxide, which is composed of mH 2 O, is not simply a blended form, but is formed by containing amorphous silicon dioxide when diailolite type calcium silicate is produced. Even if gyrolite-type calcium silicate and amorphous silicic acid are mechanically mixed, the petal-like structure described above cannot be obtained. The shape of this calcium silicate can be confirmed by taking an electron micrograph. Generally 3000~
The petal-like shape and thickness can be clearly seen in the 10,000x electron micrograph. The size, shape, etc. of petals vary depending on the type of raw materials used, raw material mixing ratio, manufacturing conditions, etc., and cannot be absolutely limited, but generally the average diameter in the longitudinal direction is 0.1 to 30μ, and the thickness is 0.005 to 0.1
Many of them are circular or elliptical in shape, with many of them resembling the petals of a rose flower. However, Japanese Patent Application No. 160031 (Sho 52-160031)
29643) is a petal-like compound, that is,
It is made up of aggregates in which flakes grow not in a fixed direction but in multiple directions. Patent Application No. 52-160031 (Japanese Patent Publication No. 60-29643) was characterized by the use of a water-soluble calcium compound as a raw material, but this time, gypsum, which is water-soluble but relatively sparingly soluble, was used as a raw material. It was discovered that a petal-shaped calcium silicate-gypsum complex similar to that shown by the above formula (A) can be obtained by selecting the addition order and addition conditions even when using a calcium compound of It came to this. The present invention uses an alkali silicate (SiO 2 /R 2 O (where R is Na or K) molar ratio 1.55 to 6.5) (hereinafter also simply referred to as an alkali silicate) in a gypsum suspension.
A method for producing calcium silicate with a petal-like aggregate structure or a calcium silicate-gypsum composite with a petal-like aggregate structure, which comprises gradually adding a solution and heat-treating the mixture under pressure at a temperature of 150 to 250°C. . What is important in the present invention is to add the alkaline silicate solution to the gypsum suspension and to do this addition as gradually as possible. Under these considerations, when the molar ratio of gypsum/alkali silicate is around 1, a petal-shaped calcium silicate is mainly obtained, and when the molar ratio is 1.1 to 1.5, a petal-shaped calcium silicate-gypsum composite is obtained. The alkali silicate used as the raw material for the present invention is theoretically
The SiO 2 /CaO molar ratio is in the range of 1.55 to 6.5. The SiO 2 /CaO molar ratio here refers to excess gypsum CaO.
is not included. As mentioned above, the molar ratio of SiO 2 /CaO can be controlled by controlling the type of raw materials, reaction temperature, reaction time,
This will vary slightly depending on the water ratio, etc., so please prepare the amount in the product in advance.
SiO 2 /CaO molar ratio and SiO 2 / in raw material preparation
It is preferable to confirm the relationship with the CaO molar ratio before use. The general formula shows that as the molar ratio of SiO 2 /CaO in calcium silicate increases, depending on the formation conditions, amorphous 2
Since silicon oxide may form a spherical shape, it is necessary to prepare a suitable SiO 2 /
It is preferable to predetermine the CaO molar ratio. As the alkali silicate used as a raw material in the above, it is preferable to use one represented by the following formula R 2 O·lSiO 2 (R is Na or K, l is 1.5 to 6.5), and gypsum and the alkali silicate The usage ratio of gypsum/alkali silicate is 1.0.
A range of ~1.5 is advantageous. In the present invention, first, gypsum is placed in water and stirred thoroughly to form a slurry. As will be explained later, the slurry concentration at this time is preferably lower. However, if the concentration is set too low and water is added at least 100 times the weight of the finally obtained calcium silicate, the obtained calcium silicate cannot become petal-shaped, which is not preferable. An alkali silicate such as sodium silicate or potassium silicate or an aqueous solution thereof is gradually added to this slurry, generally under atmospheric pressure, to form a slurry. What is important here is the addition time, and it is preferable to add as slowly as possible. The amount of time required is not absolutely limited depending on the particle size, crystal shape, etc. of the gypsum, but it is generally best to add as much time as possible, at least 10 minutes. If the addition time of the alkali silicate is too short, it is difficult to form a calcium silicate or a calcium silicate-gypsum complex having a petal-like structure and a high bulk specific volume, which is undesirable because it tends to become lumpy. It is currently not clear why the addition time of alkali silicate is important, but although gypsum has a low solubility, its dissolution rate is relatively high, and as soon as slightly dissolved gypsum and alkali silicate react, Since new gypsum is dissolved in the process, we believe that if the addition time is long enough, the result will be the same as reacting a highly water-soluble calcium compound with an alkali silicate. On the other hand, if the addition time is too short, the reaction between the alkali silicate and the gypsum will occur on the gypsum solid, and the resulting gypsum will become very non-uniform and cannot form a petal shape. Furthermore, the order of addition of the above-mentioned raw material components is also important, and if the order is reversed, that is, when an aqueous slurry of gypsum is added to an alkali silicate or its aqueous solution, the resulting calcium silicate is unlikely to be petal-shaped. That is, when a gypsum slurry is added to an alkali silicate, most of the resulting calcium silicate tends to be lump-like rather than petal-shaped even if the addition rate is sufficiently slow. Next, by reacting the mixture of the gypsum slurry and the alkali silicate under pressure at 150 to 250°C using, for example, an oaklave, the desired calcium silicate or calcium silicate-gypsum composite can be obtained. In the present invention, the petal-shaped calcium silicate or calcium silicate monogypsum complex can be obtained by separating it from the solvent, but it can also be purified by washing with water if necessary. The petal-shaped calcium silicate thus obtained may be dried in a conventional manner and used as it is or, if necessary, pulverized to form a product. In the present invention, when obtaining calcium silicate, the molar ratio of gypsum/alkali silicate may be selected to be around 1, and when obtaining a calcium silicate-gypsum composite, the molar ratio is 1.1 to 1.5. Just choose it so that it falls within the range of . Common sense says that the molar ratio is
If the value is greater than 1.0, the chemical reaction equation suggests that the excess gypsum will not participate in the reaction at all, but surprisingly, the excess gypsum does not act as a mere impurity in the obtained calcium silicate. , microblended in calcium silicate to form a calcium silicate-gypsum complex, 10,000
It became impossible to distinguish between calcium silicate and gypsum even under a magnified electron microscope, and it was found that the bulk specific volume and oil absorption were extremely large. The mechanism of action behind this phenomenon is not clear, but even if calcium silicate is first synthesized and then gypsum is added and hydrothermally treated in an autoclave, such a composite will not work. Considering that it was not obtained, we speculate that gypsum may be involved in some way during the crystal growth of calcium silicate. However, when the molar ratio exceeds 1.6, gypsum and calcium silicate can be clearly distinguished even under a microscope. The calcium silicate-gypsum composite obtained as described above exhibits excellent performance when used as an adsorption carrier, a matting agent, a filter aid, etc., similar to the petal-shaped high bulk specific volume calcium silicate described above. do. EXAMPLES In order to explain the present invention in more detail, Examples and Comparative Examples will be given below, but the present invention is not limited to these Examples. In addition, various measured values in the following Examples and Comparative Examples were determined as follows. (a) Bulk specific volume Calcium silicate was ground in a mortar to a particle size that could pass 80% through a 200 mesh sieve. The pulverized calcium silicate was used to measure bulk specific gravity according to JIS K6220 Section 6.8. (b) Oil absorption amount Calcium silicate was ground in a mortar to a particle size that could pass 80% through a 200 mesh sieve. The pulverized calcium silicate was used to measure oil absorption according to JIS K6220, item 19. Example 1 4.56g of B type hemihydrate gypsum (100 meshes) was 98
Pour into cc water and stir for 20 minutes. While stirring the slurry, 100 c.c. of 0.3144 mol/l sodium silicate (SiO 2 /Na 2 O molar ratio 2.6) was added at a rate of 5 c.c./min over 20 minutes at 25° C. under atmospheric pressure. Ta. In this case, the charged CaSO 4 /Na 2 O·nSiO 2 molar ratio was 1.00. The resulting slurry was placed in an autoclave, sealed and reacted at 200°C for 5 hours. The reaction product was filtered, washed twice with 100 c.c. of ion-exchanged water, and then dried at 100°C for 8 hours. The yield of this dry product was 7.35g. The bulk specific volume was 21 cc/g, and the oil absorption was 6.3 cc/g. Furthermore, the result of X-ray diffraction showed a pattern of diairolite type calcium silicate. The results of chemical analysis were: CaO2 4.4%, SiO 2 66.2%, loss on ignition 9.4%. From this result, it was found that the calcium silicate obtained in the above operation was 2CaO.3SiO 2 .2.06SiO 2 .2.39H 2 O. Figure 1 shows an electron microscope photo taken at 10,000 times magnification, and it was confirmed that the petal was composed of an aggregate of petals with an average longitudinal diameter of about 2u and a thickness of less than 0.1μ. Example 2 6.5 g of dihydrate gypsum (100 meshes) is poured into 98 c.c. of water and stirred for 20 minutes. While stirring this slurry, 100 c.c. of 0.3144 mol/l sodium silicate (SiO 2 /Na 2 O molar ratio 2.6) was added to 6 c.c./l at 25°C under atmospheric pressure.
The mixture was added over a period of 16 minutes and 40 seconds at a rate of 1 minute. In this case, the charged CaSO 4 /Na 2 O·nSiO 2 was 1.34. The subsequent operations were carried out in the same manner as in Example 1 to obtain 8.2 g of powder. The results of X-ray diffraction of this powder showed a mixture of peaks of anhydrite-type anhydrite and gyrolite-type calcium silicate. From the results of chemical analysis, (2CaO・
3SiO 2 .2.05SiO 2 .2.37H 2 O) (0.20CaSO 4 ). Figure 2 shows a photograph taken with an electron microscope at 10,000 times magnification, and it was confirmed that the flower was composed of petals with a diameter of 2μ in the longitudinal direction and a thickness of 0.1μ or less.
It should be noted that crystals that appeared to be type anhydrite could not be visually identified. Bulk specific volume is 19.5cc/g oil absorption
It was 63.2cc/g. Example 3 Same as Example 1 except that the amount of B-type gypsum hemihydrate, SiO 2 /CaO molar ratio of sodium silicate, concentration, autoclave reaction temperature and reaction time were changed as shown in Table 1. Treated in the same way. Preparation
Both CaSO 4 /Na 2 O and nSiO 2 were 100.
In each case, it was confirmed by X-ray diffraction, electron microscopy, and chemical analysis that it was petal-shaped calcium silicate. The results are also shown in Table 1.
【表】
実施例 4
実施例2の2水石膏の量を第2表に示す如くに
変化させた以外は実施例2と同様に実施して第2
表の通りの結果を得た。1万倍の電子顕微鏡の観
察によればNo.3、No.4、No.5は花弁状物と板状の
型無水石膏が混在していることが確認されたが
No.1、No.2は花弁状物のみで、石膏と思われる物
質は、識別出来なかつた。[Table] Example 4 The second test was conducted in the same manner as in Example 2, except that the amount of dihydrate gypsum in Example 2 was changed as shown in Table 2.
The results shown in the table were obtained. According to observation using an electron microscope at a magnification of 10,000 times, it was confirmed that No. 3, No. 4, and No. 5 contained a mixture of petal-like materials and plate-like anhydrite.
In No. 1 and No. 2, there were only petal-like objects, and the substance that appeared to be plaster could not be identified.
【表】
実施例 5
実施例1及び実施例2の珪酸ナトリウムに変え
て珪酸カリウムを用いた以外は、実施例1及び実
施例2と同様に実施した。化学分析X線回折・電
子顕微鏡の結果は、実施例1及び実施例2の結果
とほゞ同様で、実施例1と同様に実施したもの
は、2CaO・3SiO2・2.05SiO2・2.33H2Oで示され
る長手方向2μの花弁状物であり、実施例2と同
様に実施したものは、(2CaO・3SiO2・
2.05SiO2・2.34H2O)(0.20CaSO4)で示される珪
酸カルシウム―石膏複合体からなる花弁状物であ
ることが確認された。
比較例 1
a型半水石膏(CaSO4・1/2H2O)1.45gを0.2モ
ル/lの珪酸ナトリウム(珪酸ナトリウム比
2.6)水溶液50c.c.に添加し、オートクレーブ中200
℃で20時間反応させた。得られたものを実施例1
と同様の操作で乾燥した。このものを電子顕微鏡
写真(1万倍)をとつた結果第3図に示す如く粒
子状物の塊であつた。即ち第1〜2図に示した本
発明の珪酸カルシウムとは全く異なることが明ら
かである。[Table] Example 5 The same procedure as in Examples 1 and 2 was carried out except that potassium silicate was used instead of sodium silicate in Examples 1 and 2. The results of chemical analysis X-ray diffraction and electron microscopy were almost the same as those of Examples 1 and 2, and the results obtained in the same manner as in Example 1 were 2CaO・3SiO 2・2.05SiO 2・2.33H 2 A petal-like object with a length of 2μ in the longitudinal direction, denoted by O, was prepared in the same manner as in Example 2 .
It was confirmed that it was a petal-like substance made of a calcium silicate-gypsum complex represented by 2.05SiO 2 .2.34H 2 O) (0.20CaSO 4 ). Comparative Example 1 1.45 g of a-type gypsum hemihydrate (CaSO 4 1/2 H 2 O) was mixed with 0.2 mol/l of sodium silicate (sodium silicate ratio
2.6) Add to aqueous solution 50c.c. and autoclave 200
The reaction was carried out at ℃ for 20 hours. The obtained result is shown in Example 1.
It was dried in the same manner. An electron micrograph (10,000 times magnification) of this material revealed that it was a mass of particulate matter as shown in FIG. That is, it is clear that it is completely different from the calcium silicate of the present invention shown in FIGS. 1 and 2.
第1図は本発明の珪酸カルシウムの電子顕微鏡
写真(1万倍)、第2図は本発明の珪酸カルシウ
ム―石膏複合体の電子顕微鏡写真(1万倍)、第
3図は、比較例で示した珪酸カルシウムの電子顕
微鏡写真(1万倍)である。
Figure 1 is an electron micrograph (10,000 times) of the calcium silicate of the present invention, Figure 2 is an electron microscope photograph (10,000 times) of the calcium silicate-gypsum composite of the present invention, and Figure 3 is a comparative example. This is an electron micrograph (10,000 times magnification) of the calcium silicate shown.
Claims (1)
徐々に加え、加圧下に150〜250℃の温度に水熱処
理することを特徴とする花弁状集合体構造の珪酸
カルシウムまたは花弁状集合体構造の珪酸カルシ
ウム―石膏複合体の製造方法。 2 珪酸アルカリが珪酸ナトリウムである特許請
求の範囲第1項記載の方法。 3 石膏/珪酸アルカリのモル比が1.0〜1.5の範
囲で反応させる特許請求の範囲第1項記載の方
法。[Claims] 1. Calcium silicate or calcium silicate with a petal-like aggregate structure characterized by gradually adding an alkaline silicate solution to an aqueous suspension of gypsum and hydrothermally treating the mixture under pressure at a temperature of 150 to 250°C. A method for producing a calcium silicate-gypsum composite with a petal-like aggregate structure. 2. The method according to claim 1, wherein the alkali silicate is sodium silicate. 3. The method according to claim 1, wherein the reaction is carried out at a molar ratio of gypsum/alkali silicate in the range of 1.0 to 1.5.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15488978A JPS5585445A (en) | 1978-12-18 | 1978-12-18 | Manufacture of calcium silicate or calcium silicateegypsum compounded body |
| US05/974,523 US4226636A (en) | 1977-12-30 | 1978-12-29 | Production of calcium silicate having high specific bulk volume and calcium silicate-gypsum composite |
| DE2856800A DE2856800C2 (en) | 1977-12-30 | 1978-12-29 | Process for the production of calcium silicate |
| DE2857424A DE2857424C2 (en) | 1977-12-30 | 1978-12-29 | |
| GB7850207A GB2013639B (en) | 1977-12-30 | 1978-12-29 | Production of calcium cilicate having high specific bulk volume and calcium silicategypsum composite |
| FR7900006A FR2422591A1 (en) | 1977-12-30 | 1979-01-02 | CALCIUM SILICATE PREPARATION |
| FR7916239A FR2422592A1 (en) | 1977-12-30 | 1979-06-25 | PROCESS FOR PREPARING A SILICATE / CALCIUM SULPHATE COMPOSITE |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15488978A JPS5585445A (en) | 1978-12-18 | 1978-12-18 | Manufacture of calcium silicate or calcium silicateegypsum compounded body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5585445A JPS5585445A (en) | 1980-06-27 |
| JPS62867B2 true JPS62867B2 (en) | 1987-01-09 |
Family
ID=15594165
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15488978A Granted JPS5585445A (en) | 1977-12-30 | 1978-12-18 | Manufacture of calcium silicate or calcium silicateegypsum compounded body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5585445A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6051651A (en) * | 1983-08-31 | 1985-03-23 | 株式会社トクヤマ | Manufacture of formed body |
| US8679547B2 (en) | 2011-10-20 | 2014-03-25 | Tomita Pharmaceutical Co., Ltd. | Method for manufacturing calcium silicate based composition |
| JP7704568B2 (en) * | 2021-05-19 | 2025-07-08 | 太平洋マテリアル株式会社 | Inorganic coating material |
-
1978
- 1978-12-18 JP JP15488978A patent/JPS5585445A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5585445A (en) | 1980-06-27 |
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