JPS59169923A - Xonotlite-type calcium silicate and its preparation - Google Patents

Xonotlite-type calcium silicate and its preparation

Info

Publication number
JPS59169923A
JPS59169923A JP4357783A JP4357783A JPS59169923A JP S59169923 A JPS59169923 A JP S59169923A JP 4357783 A JP4357783 A JP 4357783A JP 4357783 A JP4357783 A JP 4357783A JP S59169923 A JPS59169923 A JP S59169923A
Authority
JP
Japan
Prior art keywords
raw material
reaction
calcium silicate
powdered
xonotlite
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
Application number
JP4357783A
Other languages
Japanese (ja)
Inventor
Tsurayuki Yamaya
山家 貫之
Tatsuo Iguchi
井口 辰雄
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP4357783A priority Critical patent/JPS59169923A/en
Publication of JPS59169923A publication Critical patent/JPS59169923A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prepare a xonotlite-type calcium silicate having high crystallinity, by adding powdery lime material stepwise to a powder silicate material to effect the multi-stage batch-wise hydrothermal reaction, while specifying the ratio of CaO/SiO2 in the first-stage reaction. CONSTITUTION:A powdery silicate material is subjected to the hydrothermal reaction with a powdery lime material at a CaO/SiO2 molar ratio of 0.9-1.5. The above reaction is carried out batchwise in multistages by dividing the powdery lime material into two or more parts, and adding the material stepwise to the system. The molar ratio of CaO/SiO2 in the first-stage reaction is selected to be <=0.6, and the reaction is carried out usually at 40-200 deg.C for 3-10hr. The process yields a xonotlite-type calcium silicate having collected acicular crystal form, high crystallinity, improved physical properties such as chemical resistance as formed article, and high specific surface area in powdery state.

Description

【発明の詳細な説明】 本発明は、粉状−ケイ酸質原料と粉状石灰質原料とを水
熱反応させて得られる結晶性のゾノトライト系ケイ酸カ
ルシウム及びその製造方法に関する。ゾノトライト系ケ
イ酸カルシウムは(以下「ゾノトライト」という)は、
トパモライ系に比して耐熱性が優れ、工業用として高温
用膜熱材、建築用として耐火被覆材等の用途がある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a crystalline xonotrite-based calcium silicate obtained by hydrothermally reacting a powdery silicic acid raw material and a powdery calcareous raw material, and a method for producing the same. Zonotlite-based calcium silicate (hereinafter referred to as "Zonotlite") is
It has superior heat resistance compared to the topamolye type, and is used as a high-temperature membrane heating material for industrial purposes and as a fire-resistant coating material for construction.

」二記ンノトライトの製造方法としては、例えば粉状ケ
イ酸質原料と粉状石灰質原料とをCan/5iOzモル
比−0,9〜1.5で当初から混合したものをオートク
レーブ内で水熱反応させていた。しかし、この方法で得
られたゾノトライトは、結晶形態が電子顕微鏡写真で観
察したとき第1図に示すように剣状散在型であり、結晶
化度が低く成形状態においては耐薬品等の点で、また粉
粒体状態においては比表面積の大きなものが得られない
等の問題があった。
The method for producing Nnotrite is, for example, a mixture of a powdered siliceous raw material and a powdered calcareous raw material at a Can/5iOz molar ratio of -0.9 to 1.5, which is then subjected to a hydrothermal reaction in an autoclave. I was letting it happen. However, when the xonotlite obtained by this method is observed in an electron micrograph, it has a sword-like scattered crystal morphology, as shown in Figure 1, and its crystallinity is low, and in the molded state, it has poor chemical resistance. In addition, there was a problem that a product with a large specific surface area could not be obtained in a powder or granule state.

本発明は、上記にかんがみて、結晶化度が高く成形状態
において耐薬品性等の物性向上か図れ、かつ粉粒体状態
において比表面積の小さなものが得られる新規な結晶形
態のゾノトライト及びその製造方法を提供することを目
的とする。
In view of the above, the present invention provides a novel crystal form of xonotlite that has a high degree of crystallinity, improves physical properties such as chemical resistance in a molded state, and has a small specific surface area in a granular state, and the production thereof. The purpose is to provide a method.

第1発明の要旨は、結晶形態が針状集束型であることに
特徴を有するゾノトライトにあり、第2発明の要旨は、
粉状ケイ酸質原料に対して二分割以」−とした前記粉状
石灰質原料の各単位を段階的に加えて多段パッチ式に前
記水熱反応をさせるとともに、水熱反応の第1段反応に
おけるCaO/5i02゜モル比=0.6以下であるこ
とに特徴を有するゾノトライトの製造方法にある。
The gist of the first invention resides in xonotlite, which is characterized in that the crystal form is an acicular focused type, and the gist of the second invention is as follows:
Each unit of the powdered calcareous raw material divided into two parts or more is added stepwise to the powdered siliceous raw material to carry out the hydrothermal reaction in a multi-stage patch manner, and the first stage reaction of the hydrothermal reaction is carried out in a multi-stage patch manner. The method for producing xonotlite is characterized in that the molar ratio of CaO/5i02 is 0.6 or less.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明のゾノトライトに使用する粉状ケイ酸質原料とし
ては、各種ケイ石粉末、ケイソウ上、ホワイトカーボン
、フェロシリコンダスト、ケイ華等を例示でき、また、
粉状石灰質原料としては消石灰、生石灰、焼成Fロマイ
ト等を例示できる。
Examples of the powdered silicic acid raw material used for the xonotlite of the present invention include various silica powders, diatomite powder, white carbon, ferrosilicon dust, silica, etc.
Examples of powdery calcareous raw materials include slaked lime, quicklime, and calcined F lomite.

ここで各原料の粒径は粉末相77−の混合性及び反応性
等の見地からケイ酸質が250メツシユ(63用m)以
下、石灰質原料100メツシユ(49ルm)以下とする
ことが望ましい。また、これらの原料の粉末化に際して
は、鉱物等の粉砕に通常使用されるローラミル、振動ボ
ールミル等の粉砕機を用いる。
Here, the particle size of each raw material is preferably 250 mesh (63 m) or less for the silicic acid material and 100 mesh (49 m) or less for the calcareous material from the viewpoint of the mixability and reactivity of the powder phase 77-. . Further, when powdering these raw materials, a pulverizer such as a roller mill or a vibrating ball mill, which is commonly used for pulverizing minerals, etc., is used.

L記粉状ケイ酸質原料と粉状石灰質原料とCab/Si
02モル比=0.9〜1.5で水熱反応をさせるのであ
るが、本発明の方法では粉状ケイ酸質原料に対して二分
割以上とした粉状石灰質原料の各単位を段□階的に加え
て多段/ヘツチ式で行なう。このとき、第1段反応にお
けるCaO/5i02 モル比=0.6以下(通常0.
5〜0.01)とし、反応条件は通常140〜200℃
X3−10hとする。CaO/5i02モル比が0.6
を越えると第1段の反応系全体における反応が緩慢とな
り、後述の第2段以降の水熱反応をさせても従来より知
られている4状散在型の単調な結晶形態になりやすく、
本発明の針状集束型のゾノトライトが得られない。ここ
で針状集束型結晶とは電子顕微鏡写真で観察したとき第
2図に示すような結晶形態のものをいう。続く二段以降
の水熱反応は、各前段の反応生成物に(粉状でない場合
は前述の公知粉砕機を用いて250メツシユ以Fとして
)、残余の粉状石灰質原料の各学位を加えて行ない、反
応条件は前段より高温長時間(特に最終段反応において
)とし、通常180〜230°OX5〜15hとする。
L: Powdered silicic acid raw material, powdered calcareous raw material, and Cab/Si
The hydrothermal reaction is carried out at a molar ratio of 0.9 to 1.5. In the method of the present invention, each unit of the powdery calcareous raw material, which is divided into two or more parts, is divided into stages □ In addition to the steps, it is also done in a multi-stage/Hetsch style. At this time, the CaO/5i02 molar ratio in the first stage reaction is 0.6 or less (usually 0.6 or less).
5 to 0.01), and the reaction conditions are usually 140 to 200°C.
Let it be X3-10h. CaO/5i02 molar ratio is 0.6
If this value is exceeded, the reaction in the entire reaction system in the first stage becomes slow, and even if the hydrothermal reaction in the second stage and subsequent stages described below is carried out, it tends to result in the monotonous crystal form of the conventionally known four-shaped interspersed type.
The acicular focusing type xonotlite of the present invention cannot be obtained. Here, the term "acicular focused crystal" refers to a crystal in the form shown in FIG. 2 when observed by electron micrograph. For the subsequent hydrothermal reactions in the second and subsequent stages, each grade of the remaining powdery calcareous raw material is added to the reaction product of each previous stage (if it is not in powder form, use the above-mentioned known pulverizer to make it 250 mesh or less). The reaction conditions are higher temperature and longer time than the previous stage (especially in the final stage reaction), usually 180 to 230° OX for 5 to 15 hours.

また、前段反応生成物と石灰質原料の各単位との混合は
、均一とするため、V形ミキサー1.ナウタミキサー、
リボンミキサー等の公知ブレンダーを用いて行なうこと
が望ましい。なお、上記各水熱反応の段数は特に限定さ
れないが、通常2〜3段とし、水熱反応は通常オートク
レーブに高温高圧の飽和水蒸気を刺入して行なう。
In addition, in order to uniformly mix the first-stage reaction product and each unit of the calcareous raw material, the V-type mixer 1. nauta mixer,
It is preferable to use a known blender such as a ribbon mixer. The number of stages for each of the above hydrothermal reactions is not particularly limited, but is usually 2 to 3 stages, and the hydrothermal reactions are usually carried out by introducing high temperature and high pressure saturated steam into an autoclave.

こうして得られた本発明のゾノトライトは電子顕微鏡写
真で観察したとき、結晶形態が針状集束型(第2図)で
あり、結晶化度が従来の針状散在型(第1図)に比して
格段に高くて、成形状態における耐薬品性等の物性が大
幅に向上するとともに、粉粒状IFにおいて比較的比表
面積の大きなものが得られる。従って、成形状態で断熱
材、耐火被覆材等の用途の他に、粉粒体状態で骨材、さ
らには塗料、プラスチック、紙などの充填材、各種吸着
剤等広範な用途を期待できるものである。
When the xonotlite of the present invention thus obtained is observed by electron micrograph, the crystal morphology is needle-like focused type (Fig. 2), and the crystallinity is higher than that of the conventional needle-like scattered type (Fig. 1). The chemical resistance and other physical properties in the molded state are significantly improved, and a powdery IF with a relatively large specific surface area can be obtained. Therefore, in addition to being used as heat insulating materials and fireproof coating materials in the molded state, it is expected to be used in a wide range of applications, including as aggregate in the powdered form, fillers for paints, plastics, paper, etc., and as various adsorbents. be.

なお、第1表に示す条件でツノドライドを反応生成させ
たか、電子顕微鏡写真で観察した結晶形y魚において、
実施例1及び2はいずれも針状集束型であったのに対し
、比較例1及び2はいずれも針状集束型であった。また
、得られた各ゾノトライトの・Ii均粒径30 gmの
ものについて、BET吸清法により測定した結果を、第
1表に示す。実施例の比表面積は、比較例のそれよりい
ずれも大きいことがわかる。
In addition, in the crystal form y fish that was reacted and produced under the conditions shown in Table 1 or observed in electron micrographs,
Both Examples 1 and 2 were of the needle-like focusing type, whereas Comparative Examples 1 and 2 were both of the needle-like focusing type. Furthermore, Table 1 shows the results of measurements by the BET absorption method for each of the obtained xonotlites having an average particle diameter of 30 gm. It can be seen that the specific surface areas of the Examples are all larger than those of the Comparative Examples.

第  1  表 XオーI・クレープ生餌11水蒸気Table 1 X-O I Crepe Live Bait 11 Steam

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

第1図は実施例1のソノドライド 真(X2000倍)、第2図は比較例1のゾノトライト
の電子顕微鏡写真(X2000倍)である特  許  
出  願  人 「Ij   木  政  義
Fig. 1 is an electron micrograph (x2000x) of the sonodrite of Example 1, and Fig. 2 is an electron micrograph (x2000x) of the xonotlite of Comparative Example 1.
Applicant: “Ij Masayoshi Ki”

Claims (1)

【特許請求の範囲】 】、粉状ケイ酸質原料と粉状石灰質原料とを水熱反応さ
せて得られる結晶性のゾノトライト系ケイ酸カルシウム
において、結晶形態が針状集束型であることを特徴とす
るゾノトライト系ケイ酸カルシウム。 2、粉状ケイ酸質原料と粉状石灰質原料とをCaO/S
iO2モル比=0.8〜1.5で水熱反応させてfjJ
、られる結晶性のツノドライド系ケイ酸カルシウムを製
造する方法において、前記粉状ケイ酸質原料に対して二
分割以」−とした前記粉状石灰質原料の各中位を段階的
に加えて多段パッチ式に前記水熱反応をさせるとともに
、該水熱反応の第1段反応におけるCan/5iOzモ
ル比−〇、6以下であることを特徴とするツノドライド
系ケイ酩カルシウムの製造方法。
[Scope of Claims] ] A crystalline xonotrite calcium silicate obtained by hydrothermally reacting a powdered silicic acid raw material and a powdered calcareous raw material, characterized in that the crystalline form is an acicular focused type. Xonotrite type calcium silicate. 2. Powdered silicic acid raw material and powdered calcareous raw material are mixed with CaO/S
fjJ by hydrothermal reaction at iO2 molar ratio = 0.8 to 1.5
In the method for producing crystalline tunodried calcium silicate, each middle part of the powdered calcareous raw material divided into two parts or more is added stepwise to the powdered silicic raw material to form a multistage patch. 1. A method for producing a tunodolide calcium silica, characterized in that the hydrothermal reaction is carried out according to the above formula, and the Can/5iOz molar ratio in the first stage reaction of the hydrothermal reaction is -0, 6 or less.
JP4357783A 1983-03-16 1983-03-16 Xonotlite-type calcium silicate and its preparation Pending JPS59169923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4357783A JPS59169923A (en) 1983-03-16 1983-03-16 Xonotlite-type calcium silicate and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4357783A JPS59169923A (en) 1983-03-16 1983-03-16 Xonotlite-type calcium silicate and its preparation

Publications (1)

Publication Number Publication Date
JPS59169923A true JPS59169923A (en) 1984-09-26

Family

ID=12667609

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4357783A Pending JPS59169923A (en) 1983-03-16 1983-03-16 Xonotlite-type calcium silicate and its preparation

Country Status (1)

Country Link
JP (1) JPS59169923A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6169868A (en) * 1984-09-14 1986-04-10 Agency Of Ind Science & Technol Molding thermoplastic resin blend
JPH01122917A (en) * 1987-11-04 1989-05-16 Onoda Cement Co Ltd Calcium silicate and production thereof
JPH0744814U (en) * 1995-03-14 1995-11-28 株式会社日立ホームテック Hot air heater vaporizer
JP2010037149A (en) * 2008-08-05 2010-02-18 Japan Insulation Co Ltd Calcium silicate reduced in crystalline silica content and method for producing the same
CN103539138A (en) * 2013-11-11 2014-01-29 内蒙古大唐国际再生资源开发有限公司 Method for preparing xonotlite by utilizing desiliconized alkali liquor

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6169868A (en) * 1984-09-14 1986-04-10 Agency Of Ind Science & Technol Molding thermoplastic resin blend
JPH01122917A (en) * 1987-11-04 1989-05-16 Onoda Cement Co Ltd Calcium silicate and production thereof
JPH0744814U (en) * 1995-03-14 1995-11-28 株式会社日立ホームテック Hot air heater vaporizer
JP2010037149A (en) * 2008-08-05 2010-02-18 Japan Insulation Co Ltd Calcium silicate reduced in crystalline silica content and method for producing the same
CN103539138A (en) * 2013-11-11 2014-01-29 内蒙古大唐国际再生资源开发有限公司 Method for preparing xonotlite by utilizing desiliconized alkali liquor
CN103539138B (en) * 2013-11-11 2015-11-25 内蒙古大唐国际再生资源开发有限公司 A kind of method utilizing desiliconization alkali lye to prepare xonotlite

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