JPS63258642A - Hollow inorganic powder and grain materials and preparation of same - Google Patents

Hollow inorganic powder and grain materials and preparation of same

Info

Publication number
JPS63258642A
JPS63258642A JP9358587A JP9358587A JPS63258642A JP S63258642 A JPS63258642 A JP S63258642A JP 9358587 A JP9358587 A JP 9358587A JP 9358587 A JP9358587 A JP 9358587A JP S63258642 A JPS63258642 A JP S63258642A
Authority
JP
Japan
Prior art keywords
emulsion
added
aqueous solution
organic solvent
inorganic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP9358587A
Other languages
Japanese (ja)
Other versions
JPH059133B2 (en
Inventor
Yoshiko Nakahara
佳子 中原
Masaaki Mizuguchi
正昭 水口
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.)
National Institute of Advanced Industrial Science and Technology AIST
Suzukiyushi Industrial Corp
Original Assignee
Agency of Industrial Science and Technology
Suzukiyushi Industrial Corp
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 Agency of Industrial Science and Technology, Suzukiyushi Industrial Corp filed Critical Agency of Industrial Science and Technology
Priority to JP9358587A priority Critical patent/JPS63258642A/en
Publication of JPS63258642A publication Critical patent/JPS63258642A/en
Publication of JPH059133B2 publication Critical patent/JPH059133B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Silicon Compounds (AREA)

Abstract

PURPOSE:To increase the void content by adding and mixing an organic solvent to an organic solvent containing lipophilic surface active agent after being added and mixed with the water solution of inorganic compound to form O/W type emulsion. CONSTITUTION:O/W type emulsion is prepared by adding and mixing an organic solvent to water solution containing 0.5mol./l or more of silicate or the like of alkali metal. The O/W ratio is preferably O:W=1:10-3:1. Then, said O/W type emulsion is added and mixed into an inorganic solvent containing lipophilic surface active agent to prepare O/W/O type emulsion. Preferably the ratio should be 1:10-2:1. Then, the water solution of a compound to be able to form water-insoluble sediments is added to the O/W/O type emulsion mixed and reacted with to form a wall substance. The reaction time is approximately one hour or less, and water solution concentration is preferably 0.05mol./l - saturation concentration. By said process, particles of uniform film thickness can be prepared.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は中空無機質粉粒体及びその製造法に関し更に詳
しくはそのIIIIJ厚が粒子径の約5〜45%である
中空無機質粉粒体及びその製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a hollow inorganic powder and a method for producing the same, and more particularly to a hollow inorganic powder having a IIIJ thickness of about 5 to 45% of the particle diameter and its production. Regarding the law.

従来の技術 無機質多孔性粉粒状物の従来の製造方法の一つとして、
次の様な方法が知られている。即ちアルカリ金属の珪酸
塩、炭酸塩、リン酸塩、ならびに硝酸塩、及びアルカリ
類金属またはその他の金属のハロゲン化物から選ばれた
無機化合物の少くとも1種を含む水溶液に、有機溶剤を
添加混合して乳化液となし、次いでアルカリ土類金属の
ハロゲン化物、無機酸、有機酸、無機酸のアンモニウム
塩、有n酸のアンモニウム塩並びにアルカリ金属の炭酸
、硝酸塩の少くとも1種であって、且つ上記無機化合物
との水溶液反応によって水不溶性沈澱を形成しつる化合
物の水溶液を、上記乳化液に混合して、多孔質無機質粉
体を製造する方法がある。
Conventional technology One of the conventional manufacturing methods for inorganic porous powder and granular materials.
The following methods are known. That is, an organic solvent is added to and mixed with an aqueous solution containing at least one inorganic compound selected from silicates, carbonates, phosphates, and nitrates of alkali metals, and halides of alkali metals or other metals. to form an emulsion, and then at least one of alkaline earth metal halides, inorganic acids, organic acids, ammonium salts of inorganic acids, ammonium salts of n-acids, and carbonates and nitrates of alkali metals, and There is a method of producing porous inorganic powder by mixing an aqueous solution of a compound that forms a water-insoluble precipitate through an aqueous reaction with the above-mentioned inorganic compound into the above-mentioned emulsion.

この方法は、無11質多孔性微粒子を製造する方法とし
ては極めて優れた方法であるが、この方法に於いては、
積極的に中空の無機質多孔性微粒子を製造することにつ
いては、考慮が払われていなかった。
This method is an extremely excellent method for producing 11-free porous particles, but in this method,
No consideration has been given to actively producing hollow inorganic porous particles.

発明が解決しようとする問題点 従って本発明が解決しようとする問題点は、この種従来
方法の技術を応用して、中空の無機質多孔性微粒子、惹
いては中空で空隙率の極めて大きい無機質微粒子を積極
的に製造しうる方法を開発することである。
Problems to be Solved by the Invention Accordingly, the problems to be solved by the present invention are to apply the technology of this type of conventional method to produce hollow inorganic porous fine particles, and by extension hollow inorganic fine particles with an extremely large porosity. The objective is to develop a method that can actively produce .

問題点を解決するための手段 この問題点は、アルカリ金属の珪酸塩、炭酸塩、リンM
塩、ならびに硝酸塩、及びアルカリ類金属またはその他
の金属のハロゲン化物から選ばれた無機化合物の少くと
も1種を含む水溶液に、有機溶剤を添加混合して乳化液
となし、次いでアルカリ土類金属のハロゲン化物、無機
酸、有機酸、無機酸のアンモニウム塩、有機酸のアンモ
ニウム塩並びにアルカリ金属の炭酸、硝酸塩の少くとも
1種であって、且つ上記無機化合物との水溶液反応によ
って水不溶性沈澱を形成しうる化合物の水溶液を、上記
乳化液に混合して、多孔質無機質粉体を製造する方法に
於いて、 (イ) 上記無機化合物の水溶液に有機溶剤を添加混合
してO/W型乳化液となし、 (ロ) ここに得た0/W型乳化液を、親油性界面活性
剤を含む有機溶剤中に添加混合して0/W/O型乳化液
となし、次いで (ハ) 上記水溶性反応によって水不溶性沈澱を形成し
うる化合物の水溶液中に上記(ロ)のO/W/O型乳化
液を添加混合する ことによって解決される。
Means for solving the problem This problem is solved by the use of alkali metal silicates, carbonates, phosphorus M
An organic solvent is added to an aqueous solution containing at least one inorganic compound selected from salts, nitrates, and halides of alkali metals or other metals to form an emulsion, and then an emulsion of alkaline earth metals is prepared. At least one of halides, inorganic acids, organic acids, ammonium salts of inorganic acids, ammonium salts of organic acids, and carbonates and nitrates of alkali metals, and forms a water-insoluble precipitate by an aqueous reaction with the above-mentioned inorganic compounds. In the method for producing a porous inorganic powder by mixing an aqueous solution of a compound capable of forming a compound with the above emulsion, (a) an organic solvent is added to and mixed with the aqueous solution of the inorganic compound to form an O/W emulsion. (b) The 0/W type emulsion obtained here is added and mixed into an organic solvent containing a lipophilic surfactant to form a 0/W/O type emulsion, and then (c) the above water soluble This problem can be solved by adding and mixing the O/W/O emulsion described in (b) above into an aqueous solution of a compound capable of forming a water-insoluble precipitate through a chemical reaction.

発明の構成並びに作用 水元用法の大きな特徴は、上記でのべた通り、(イ) 
上記無機化合物の水溶液に有機溶剤を添加混合してO/
W型乳化液となし、 (ロ) ここに得たO/W型乳化液を、親油性界面活性
剤を含む有機溶剤中に添加混合して0/W/O型乳化液
となし、次いで (ハ) 上記水溶性反応によって水不溶性沈澱を形成し
うる化合物の水溶液中に上記(ロ)のO/W/O型乳化
液を添加混合する ことである。
As stated above, the main features of the structure and action of the invention are as follows: (a)
Add and mix an organic solvent to the aqueous solution of the above inorganic compound and O/
(b) The O/W emulsion obtained here is added and mixed into an organic solvent containing a lipophilic surfactant to form an O/W/O emulsion, and then ( c) Adding and mixing the O/W/O type emulsion of (b) above into an aqueous solution of a compound capable of forming a water-insoluble precipitate by the water-soluble reaction.

更に詳しくは、上記無機質化合物の少くとも1種の水溶
液に有機溶剤を添加混合して乳化液を調製するに際し、
従来方法ではW/O型乳化液となすが、上記(イ)の如
く本発明に於いてはこれを0/W型乳化液となす。次い
で、このO/W型乳化液を、上記(0)の如く親油性界
面活性剤を含む有機溶剤中に添加混合してO/W/O型
乳化液とする。即ち、(イ)の工程では第1図に示す通
り無機化合物の水溶液(1)中に有機溶剤(2)が液滴
となって分散しており、これを上記(ロ)の様に処理す
ることにより、第2図に示す様に、有機溶剤(3)中に
その内部に有機溶剤(2)がつつみ込まれた無機化合物
の水溶液(1)の液滴が生成し、O/W/O型乳化液と
なる。
More specifically, when preparing an emulsion by adding and mixing an organic solvent to at least one aqueous solution of the above inorganic compound,
In the conventional method, a W/O type emulsion is made, but in the present invention, as described in (a) above, this is made into an 0/W type emulsion. Next, this O/W type emulsion is added and mixed into an organic solvent containing a lipophilic surfactant as described in (0) above to obtain an O/W/O type emulsion. That is, in the step (a), as shown in Figure 1, the organic solvent (2) is dispersed in the form of droplets in the aqueous solution (1) of the inorganic compound, and this is treated as in (b) above. As a result, as shown in Fig. 2, droplets of an aqueous solution (1) of an inorganic compound in which the organic solvent (2) is embedded in the organic solvent (3) are generated, and the O/W/O It becomes a type emulsion.

このようなO/W/O型乳化液は、次いで上記(ハ)の
工程に従って水溶性反応によって水不溶性沈澱を形成し
うる化合物の水溶液中に添加され、上記液滴と該水溶液
との界面に於いて反応が生じて水不溶性の沈澱物質所謂
壁物質を形成する。この状態を示したのが第3図であり
、第3図中(4)は壁?5賀であり、壁物質(4)内に
有機溶剤(1)が内包された微粒子が生成する。尚この
際上記水溶液反応により、生成する壁物質自体は多孔質
となっており、従って、本発明の微粒子は、壁物質自体
が多孔質であると共に内部の有機溶剤を適宜な手段で揮
散せしめることにより、内部も中空となり、その多孔度
は穫めて大きなものとなる特徴を発揮する。
Such an O/W/O type emulsion is then added to an aqueous solution of a compound capable of forming a water-insoluble precipitate by a water-soluble reaction according to the step (c) above, and is added to the interface between the droplets and the aqueous solution. A reaction takes place to form a water-insoluble precipitate material, the so-called wall material. Figure 3 shows this state, and (4) in Figure 3 is a wall? 5, and fine particles in which the organic solvent (1) is encapsulated in the wall material (4) are generated. At this time, the wall material itself produced by the aqueous reaction is porous, and therefore, in the fine particles of the present invention, the wall material itself is porous, and the organic solvent inside must be volatilized by an appropriate means. As a result, the inside becomes hollow, and its porosity becomes extremely large.

これに対し従来方法では、反応しつる無機化合物の水溶
液と41機溶剤とからW/O型乳化液を調製し、これを
上記壁物質形成用化合物の水溶液と混合しているために
、内部に有機溶剤が包含された形状とはならず、中空状
の微粒子が生成し難い。
On the other hand, in the conventional method, a W/O emulsion is prepared from an aqueous solution of a reactive inorganic compound and a 41-organic solvent, and this is mixed with the aqueous solution of the wall material forming compound. The shape does not include the organic solvent, and hollow particles are difficult to form.

ただし、従来方法に於いても、液滴と水溶液との界面で
反応が生じることは本発明法と同じであり、液滴中の無
機化合物が壁形成用物質と反応して壁を形成するために
、液滴中の無機化合物がこの反応に消費されて内部に時
として空隙が生じることもあるが、この従来方法と本発
明法とは、その中空形成過程が上記で説明した通り根本
的に異なるものである。
However, even in the conventional method, the reaction occurs at the interface between the droplet and the aqueous solution, which is the same as in the method of the present invention, and the inorganic compound in the droplet reacts with the wall-forming substance to form the wall. Inorganic compounds in the droplet are consumed in this reaction, sometimes creating voids inside the droplet, but the difference between this conventional method and the method of the present invention is that the hollow formation process is fundamentally the same as explained above. They are different.

以下に本発明法をその製造工程順に説明する。The method of the present invention will be explained below in the order of its manufacturing steps.

先ずアルカリ金属の珪酸塩、炭酸塩、リン酸塩ならびに
硝酸塩、アルカリ土類金属またはその他のハロゲン化物
から選ばれた無機化合物の少くとも1種を含む水溶液好
ましくはその濃度0.5モル/交以上、特に好ましくは
3.0モル/文〜飽和濃度の水溶液に、有機溶剤を添加
混合してO/W型乳化液をtJA製する(上記(イ)の
工程)。この際の有機溶剤としては従来からこの種方法
に於いて使用されて来たものがいずれも使用出来、好ま
しいものとして常温で液状で水に対する溶解度が8%以
下で実質上反応に関しないものを挙げることが出来る。
First, an aqueous solution containing at least one inorganic compound selected from silicates, carbonates, phosphates of alkali metals, nitrates, alkaline earth metals, or other halides, preferably at a concentration of 0.5 mol/min or more. Particularly preferably, an organic solvent is added to and mixed with an aqueous solution having a concentration of 3.0 mol/liter to saturation to prepare an O/W emulsion (step (a) above). As the organic solvent in this case, any organic solvent that has been conventionally used in this type of method can be used, and preferred ones are those that are liquid at room temperature, have a solubility in water of 8% or less, and are not substantially involved in the reaction. I can do it.

これ等の好ましい具体例を挙げると以下の通りである。Preferred specific examples of these are as follows.

脂肪族炭化水素類: n−ヘキサン、イソヘキサン、n−へブタン、イソへブ
タン、n−オクタン、イソオクタン、ガソリン、石油エ
ーテル、灯油、ベンジン、ミネラルスピリットなど、 脂環式炭化水素類ニ ジクロペンタン、シクロヘキサン、シクロヘキセン、シ
クロノナンなど 芳香族炭化水素類: ベンゼン、トリエン、キシレン、エチルベンゼン、プロ
ピルベンゼン、クメン、メシチレン、テトラリン、スチ
レンなど エーテル類: プロビルエーテル、イソプロピルエーテルなど、ハロゲ
ン化炭化水素: 塩化メチレン、りOoフォルム、塩化エチレン、トリク
ロロエタン、トリクロロエチレンなど、エステル類: 酢酸エチル、酢酸−〇−プロピル、酢酸イソプロピル、
酢酸−n−ブチル、酢酸イソブチル、酢酸−〇−アミル
、酢酸イソアミル、乳酸ブチル、プロピオン酸メチル、
プロピオン酸エチル、プロピオン酸ブチル、酪酸メチル
、酪酸エチル、酪酸ブチルなど、 これらの有機溶媒は、1種または2種以上を混合して使
用できる。
Aliphatic hydrocarbons: n-hexane, isohexane, n-hebutane, isohbutane, n-octane, isooctane, gasoline, petroleum ether, kerosene, benzine, mineral spirits, etc. Alicyclic hydrocarbons dichloropentane, Aromatic hydrocarbons such as cyclohexane, cyclohexene, and cyclononane: Benzene, triene, xylene, ethylbenzene, propylbenzene, cumene, mesitylene, tetralin, styrene, etc. Ethers: Probyl ether, isopropyl ether, etc. Halogenated hydrocarbons: Methylene chloride, Oo form, ethylene chloride, trichloroethane, trichloroethylene, etc., esters: ethyl acetate, -propyl acetate, isopropyl acetate,
n-butyl acetate, isobutyl acetate, amyl acetate, isoamyl acetate, butyl lactate, methyl propionate,
These organic solvents, such as ethyl propionate, butyl propionate, methyl butyrate, ethyl butyrate, and butyl butyrate, can be used alone or in combination of two or more.

このO/W型乳化液をlI製する際には、通常界面活性
剤を用いる。またこの際のO/W比は、得られる乳化液
がO/W型となる限り、特に限定されないが、O:W−
1:/O〜3:1程°度が好ましい。界面活性剤の使用
量は有機溶剤の/O重憬%程度以下が好ましく、特にo
、oi〜3重量%程度が好ましい。
When producing this O/W type emulsion, a surfactant is usually used. Further, the O/W ratio at this time is not particularly limited as long as the obtained emulsion is O/W type, but O:W-
The ratio is preferably about 1:/O to 3:1. The amount of surfactant to be used is preferably about /O% or less of the organic solvent, especially
, oi to about 3% by weight is preferred.

使用する界面活性剤としても従来から使用されて来たも
のが広い範囲でいずれも使用出来るが、好ましい具体例
を挙げると次の通りである。
Although a wide range of conventional surfactants can be used as the surfactant, preferred specific examples are as follows.

ソルビタン脂肪酸エステル系: ソルビタンモノラウレート、ソルビタンモノパルミテー
ト、ソルビタンモノステアレート、ソルビタントリステ
アレート、ソルビタンモノオレエート、ソルビタンセキ
スオレエートなど。
Sorbitan fatty acid esters: sorbitan monolaurate, sorbitan monopalmitate, sorbitan monostearate, sorbitan tristearate, sorbitan monooleate, sorbitan sekisoleate, etc.

ポリオキシエチレンンルビタン脂肪酸エステル系:ポリ
オキシエチレンソルビタンモノラウレート、ポリオキシ
エチレンソルビタンモノパルミテート、ポリオキシエチ
レンソルビタンモノステアレート、ポリオキシエチレン
ソルビタントリステアレート、ポリオキシエチレンソル
ビタンモノオレエート、ポリオキシエチレンソルビタン
ステアレートなど、 ポリオキシエチレン高級アルコールエーテル系:ポリオ
キシエチレンラウリルエーテル、ポリオキシエヂレンセ
ヂルエーテル、ポリオキシエチレンステアリルエーテル
、ポリオキシエチレンオレイルエーテル、ポリオキシエ
チレンオクチルフェノールエーテル、ポリオキシエチレ
ンノニルフェノールエーテルなど、 ポリオキシエチレン脂肪酸エステル系:ポリオキシエチ
レングリコールモノラウレート、ポリオキシエチレング
リコールモノラウレート、ポリオキシエチレングリコー
ルステアレート、ポリオキシエチレングリコールモノオ
レエートなど、 グリセリン脂肪酸エステル系ニ ステアリン酸モノグリセライド、オレイン酸モノグリセ
ライドなど、 ポリオキシエチレンソルビトール脂肪酸エステル系: テトラオレイン酸ポリオキシエチレンソルビットなど、 これらの界面活性剤は、単独または混合して使用される
Polyoxyethylene rubitan fatty acid esters: polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monopalmitate, polyoxyethylene sorbitan monostearate, polyoxyethylene sorbitan tristearate, polyoxyethylene sorbitan monooleate, poly Polyoxyethylene higher alcohol ethers such as oxyethylene sorbitan stearate: polyoxyethylene lauryl ether, polyoxyethylene cedyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, polyoxyethylene octylphenol ether, polyoxyethylene Nonylphenol ether, etc., polyoxyethylene fatty acid esters: polyoxyethylene glycol monolaurate, polyoxyethylene glycol monolaurate, polyoxyethylene glycol stearate, polyoxyethylene glycol monooleate, etc., glycerin fatty acid esters, nistearic acid Monoglyceride, oleic acid monoglyceride, etc. Polyoxyethylene sorbitol fatty acid ester type: Tetraoleic acid polyoxyethylene sorbitol, etc. These surfactants are used alone or in combination.

次いで本発明に於いては、このO/W型乳化液を親油性
界面活性剤を含む有機溶剤中に添加混合して0/W/O
型乳化液を調製する((ロ)の工程)。この際の有8!
溶剤としても上記と同様の範囲から適宜なものが使用さ
れ、(イ)の工程と同じものでも、或いは異なった種類
の有機溶剤でも良い。また界面活性剤としては親油性の
ものが使用され、その好ましい具体例は上記(イ)の工
程のものとほぼ同じであり、その使用量も(イ)の工程
と同じ範囲である。O/W/O比は、O/W:0−1:
/O〜2:1程度が好ましい。
Next, in the present invention, this O/W emulsion is added and mixed into an organic solvent containing a lipophilic surfactant to form an O/W/O emulsion.
Prepare a mold emulsion (step (b)). At this time, there are 8!
An appropriate solvent may be used within the same range as above, and may be the same as in step (a) or a different type of organic solvent. Further, as the surfactant, a lipophilic one is used, and its preferred specific example is almost the same as that in the above step (a), and the amount used is also within the same range as in the step (a). The O/W/O ratio is O/W:0-1:
/O to about 2:1 is preferred.

次いで本発明に於いては、上記0/W/○型乳化液に、
水不溶性沈澱を形成しろる化合物の水溶液を添加混合し
、反応せしめて壁物質を形成せしめる。この反応は、常
温、常圧で良好に進行するが、加熱下に反応を促進させ
ても良い。反応時間は濃度、配合割合により異なるが、
通常1時間程度以下である。上記水溶液の濃度は0.0
5モル/9t〜飽和濃度が好ましく、特に0.1〜2モ
ル/J2程度が好ましい。
Next, in the present invention, in the above 0/W/○ type emulsion,
An aqueous solution of a compound that forms a water-insoluble precipitate is added and mixed and allowed to react to form a wall material. Although this reaction proceeds well at normal temperature and normal pressure, the reaction may be accelerated under heating. The reaction time varies depending on the concentration and blending ratio, but
Usually it takes about 1 hour or less. The concentration of the above aqueous solution is 0.0
The concentration is preferably 5 mol/9t to saturation, particularly preferably about 0.1 to 2 mol/J2.

反応生成物を濾過、水洗し、乾燥することにより中空多
孔性無機質粉粒体が1qられる。
The reaction product is filtered, washed with water, and dried to yield 1 q of hollow porous inorganic powder.

本発明法により得られる粉粒体は中空であってその壁物
質の膜厚は通常粒子径の5〜45%程度であり、また壁
物質自体も多孔性であり、全体として極めて多孔質のも
のである。
The powder and granules obtained by the method of the present invention are hollow, and the film thickness of the wall material is usually about 5 to 45% of the particle diameter, and the wall material itself is also porous, making it extremely porous as a whole. It is.

発明の効果 上記の如き本発明法により、確実に壁模厚が粒子径の5
〜45%である球形中空多孔質粉体が+Fiられる。こ
のものは最高96%の空隙率を有する中空球体で芳香剤
、消臭剤、顔料、殺虫殺菌剤、防錆剤などの内包にきわ
めて有用である。
Effects of the Invention The method of the present invention as described above ensures that the wall thickness is 50% of the particle diameter.
-45% spherical hollow porous powder +Fi. This product is a hollow sphere with a porosity of up to 96% and is extremely useful for encapsulating fragrances, deodorants, pigments, insecticides, disinfectants, rust preventives, etc.

実  施  例 以下に実施例を挙げて本発明を更に詳しく説明する。Example The present invention will be explained in more detail with reference to Examples below.

実施例1 (中空多孔質球形シリカの製法) 水ガラス1号(Si O□として4モル/l2)500
dに、ポリオキシエチレン(n−/O)ラウリルエーテ
ル2%酢酸エチル溶液を/OC)d加え、高速攪拌して
O/W型エマルジョンをXl1j製した。
Example 1 (Production method of hollow porous spherical silica) Water glass No. 1 (4 mol/l2 as SiO□) 500
A 2% ethyl acetate solution of polyoxyethylene (n-/O) lauryl ether was added to d and stirred at high speed to prepare an O/W emulsion.

これをポリオキシエチレンラウリルエーテル3%酢酸エ
チル溶液200Od中に加え、高速攪拌して、O/W/
O型エマルジョンを作成した。
This was added to 200 Od of polyoxyethylene lauryl ether 3% ethyl acetate solution, stirred at high speed, and O/W/
An O-type emulsion was prepared.

このようにして得られたO/W/O型エマルシコンを1
モル/父の硫酸アンモニウム3000teに加えて攪拌
して反応させ、2時間放置し濾過分離し、水洗乾燥して
多孔質粒子内の酢酸エチルを蒸発させた。斯くして粒子
径が1〜/Oμmで膜厚が粒子径に対して約8%である
中空多孔質球形シリカ微粒子1/Ogを得た。このもの
の/O000倍走査型電子顕微鏡写真を第4図に示す。
The O/W/O type emulsion obtained in this way was 1
The mixture was added to 3,000 mol/mol of ammonium sulfate and reacted with stirring, left for 2 hours, filtered and separated, washed with water and dried to evaporate ethyl acetate within the porous particles. In this way, hollow porous spherical silica fine particles 1/Og having a particle diameter of 1 to 0 μm and a film thickness of about 8% based on the particle diameter were obtained. A scanning electron micrograph of this product at a magnification of /O000 is shown in FIG.

実施例2 (中空多孔質球形珪酸マグネシウムの製法)水ガラス3
号(SiO15Tニル/A)500dにポリオキンエチ
レン(n−/O)ノニルフェニールエーテル2.5%ト
ルエン溶液を200m加え、高速攪拌して、O/W型エ
マルジョンをI製した。これをポリオキシエチレン(n
−3)ノニルフェニールエーテル3%トルエン溶液15
00d中に加え高速攪拌して、O/W/O型エマルジ」
ンを製造した。
Example 2 (Production method of hollow porous spherical magnesium silicate) Water glass 3
200 m of a 2.5% toluene solution of polyethylene ethylene (n-/O) nonyl phenyl ether was added to 500 d of No. (SiO15T Nil/A) and stirred at high speed to prepare an O/W emulsion I. This is polyoxyethylene (n
-3) Nonylphenyl ether 3% toluene solution 15
00d and stirred at high speed to form an O/W/O type emulsion.
manufactured.

このようにして得られたものを0.5モル/父塩化マグ
ネシウム水溶液6000威中に加えて攪拌し、反応させ
、3時間放置後濾別し、水洗により反応副生物である塩
化ナトリウムなどをとりのぞき、さらに乾燥して中空内
部のトルエンを蒸発させた。斯くして粒径が1〜15μ
曙で膜厚が粒子径に対して約5%である中空多孔質球形
珪酸マグネシウム250Qを得た。
The product obtained in this way was added to 0.5 mol/6000 g of parent magnesium chloride aqueous solution, stirred, and reacted. After being allowed to stand for 3 hours, it was filtered and washed with water to remove reaction by-products such as sodium chloride. It was removed and further dried to evaporate the toluene inside the hollow. Thus the particle size is 1-15μ
Hollow porous spherical magnesium silicate 250Q having a film thickness of about 5% of the particle diameter was obtained at dawn.

実施例3 (中空多孔質炭酸カルシウムの製法) 4モル/fJ、の炭酸カリウム水溶液300−にポリオ
キシエチレン(n−/O)ノニルフェニールエーテルを
1g加えたものに、ベンゼン50−を加え高速攪拌して
、O/W型エマルシコンをvA製した。
Example 3 (Production method of hollow porous calcium carbonate) 1 g of polyoxyethylene (n-/O) nonyl phenyl ether was added to a 4 mol/fJ potassium carbonate aqueous solution 300-, and 50-benzene was added and stirred at high speed. Then, an O/W type emulsion was manufactured by vA.

このものを、ポリオキシエチレン(n−3)ノニルフェ
ニールエーテル3%キシレン溶液800dに加えて高速
攪拌して、O/W/O型エマルジョンを製造した。
This product was added to 800 d of a 3% xylene solution of polyoxyethylene (n-3) nonylphenyl ether and stirred at high speed to produce an O/W/O type emulsion.

この工ンルジ]ンを0.2モル/Rの塩化カルシウム水
溶液12000dに加え攪拌し、反応さL’30分間放
置した。
The mixture was added to 12,000 d of a 0.2 mol/R calcium chloride aqueous solution, stirred, and left to react for 30 minutes.

これを濾過分離し、水洗によって反応副生物である塩化
カリウムを取り除き、乾燥して、内部のキシレンを蒸発
させた。斯くして粒子径が1〜/Oμmで膜厚が粒子径
に対して約18%である中空多孔質炭酸カルシウム11
5gを得た。
This was separated by filtration, washed with water to remove potassium chloride as a reaction by-product, and dried to evaporate the xylene inside. Thus, the hollow porous calcium carbonate 11 has a particle size of 1 to 0 μm and a film thickness of about 18% of the particle size.
5g was obtained.

実施例4 (中空多孔質塩基性炭酸マグネシウムの製法)3モル/
桑の炭酸カリウム水溶液200ai!に、ポリオキシエ
チレン(n−30>ソルビタントリオレエート1.5%
シクロヘキサン溶液50dを加え高速攪拌して、O/W
型エマルジョンを調製した。これをソルビタンモノラウ
レート3%シクロヘキサン溶液600rR1に加え、高
速攪拌して、0/W/O型エマルジヨンを製造した。
Example 4 (Production method of hollow porous basic magnesium carbonate) 3 mol/
Mulberry potassium carbonate aqueous solution 200ai! , polyoxyethylene (n-30>sorbitan trioleate 1.5%
Add 50 d of cyclohexane solution and stir at high speed, O/W
A mold emulsion was prepared. This was added to 600 rR1 of a 3% sorbitan monolaurate solution in cyclohexane and stirred at high speed to produce a 0/W/O type emulsion.

このようにして得られたエマルジョンを0.3モル/父
の塩化マグネシウム水溶液6000−に加え、攪拌、反
応せしめ、1時間放置した。
The emulsion thus obtained was added to 0.3 mol/6000 ml of aqueous solution of magnesium chloride, stirred, reacted, and left for 1 hour.

これを濾別し、更に水洗、乾燥して0.5〜15μm粒
子径で、その膜厚が粒子径に対して約12%である中空
多孔質球形の塩基性炭酸マグネシウム70gを得た。
This was filtered, further washed with water, and dried to obtain 70 g of hollow porous spherical basic magnesium carbonate having a particle size of 0.5 to 15 μm and a film thickness of about 12% of the particle size.

実施例5 (中空多孔質硫酸バリウムの製法) 3モル/文の硫酸アンモニウム水溶液300#If!に
、ポリオキシエチレン(二しチレンオキザイド基−9)
 t?カンダリーアルコールエーテル2%ヘキセン溶液
50Idを加え高速攪拌してO/W型エマルジョンを調
製した。
Example 5 (Production method of hollow porous barium sulfate) 3 mol/liter ammonium sulfate aqueous solution 300 #If! , polyoxyethylene (diethylene oxide group-9)
T? 50 Id of a 2% hexene solution of candary alcohol ether was added and stirred at high speed to prepare an O/W emulsion.

これをソルビタンモノステアレート3%ヘキセン溶液/
O00d中に加え、高速攪拌してO/W/O型でマルジ
ョンを製造した。
This was mixed with sorbitan monostearate 3% hexene solution/
The mixture was added to O00d and stirred at high speed to produce an O/W/O type emulsion.

このようにして得られたものを0.5モル/文の塩化バ
リウム水溶液5000d中に加えて攪拌し、反応させて
1時間放置した。
The product thus obtained was added to 5,000 d of a 0.5 mol/liter aqueous barium chloride solution, stirred, reacted, and left for 1 hour.

これを繍過分離し、さらに水洗、乾燥して、粒子径1〜
20μ−でその膜厚が約14%である中空多孔質球形の
硫酸バリウム205fllを得た。
This is separated by embroidery, further washed with water, dried, and the particle size is 1 to 1.
205 ml of hollow porous spherical barium sulfate having a thickness of 20 μm and a film thickness of about 14% was obtained.

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

第1〜3図はいずれも本発明法実施の際に生ずる乳化液
の分散状態を模擬的に表わした図面である。また第4図
は実施例1の粉粒体の/O000倍走査型電子顕微鏡写
真である。 1・・・無機化合物の水溶液、 2・・・有機溶剤 3・・・有機溶剤 4・・・壁物質 (以 上)
FIGS. 1 to 3 are drawings simulating the dispersion state of the emulsion produced when carrying out the method of the present invention. Further, FIG. 4 is a scanning electron micrograph of the granular material of Example 1 at a magnification of /O000. 1...Aqueous solution of inorganic compound, 2...Organic solvent 3...Organic solvent 4...Wall material (and above)

Claims (2)

【特許請求の範囲】[Claims] (1)原膜が粒子径の5〜45%であって壁を形成する
物質が無機質多孔性である中空無機質粉粒体。
(1) A hollow inorganic powder or granule in which the original film is 5 to 45% of the particle diameter and the material forming the wall is porous.
(2)アルカリ金属の珪酸塩、炭酸塩、リン酸塩、なら
びに硝酸塩、及びアルカリ類金属またはその他の金属の
ハロゲン化物から選ばれた無機化合物の少くとも1種を
含む水溶液に、有機溶剤を添加混合して乳化液となし、
次いでアルカリ土類金属のハロゲン化物、無機酸、有機
酸、無機酸のアンモニウム塩、有機酸のアンモニウム塩
並びにアルカリ金属の炭酸、硝酸塩の少くとも1種であ
つて、且つ上記無機化合物との水溶液反応によつて水不
溶性沈澱を形成しうる化合物の水溶液を、上記乳化液に
混合して、多孔質無機質粉体を製造する方法に於いて (イ)上記無機化合物の水溶液に有機溶剤を添加混合し
てO/W型乳化液となし、 (ロ)ここに得たO/W型乳化液を、親油性界面活性剤
を含む有機溶剤中に添加混合してO/W/O型乳化液と
なし、次いで (ハ)上記水溶性反応によつて水不溶性沈澱を形成しう
る化合物の水溶液中に上記(ロ)のO/W/O型乳化液
を添加混合する ことを特徴とする中空無機質粉粒体の製造法。
(2) Adding an organic solvent to an aqueous solution containing at least one inorganic compound selected from silicates, carbonates, phosphates, and nitrates of alkali metals, and halides of alkali metals or other metals. Mix to make an emulsion,
Next, an aqueous solution reaction with at least one of alkaline earth metal halides, inorganic acids, organic acids, ammonium salts of inorganic acids, ammonium salts of organic acids, and carbonates and nitrates of alkali metals, and the above-mentioned inorganic compound. In a method for producing a porous inorganic powder by mixing an aqueous solution of a compound capable of forming a water-insoluble precipitate with the emulsion, (a) an organic solvent is added to and mixed with the aqueous solution of the inorganic compound; (b) The O/W emulsion obtained here is added and mixed into an organic solvent containing a lipophilic surfactant to make an O/W/O emulsion. , and then (c) hollow inorganic powder particles characterized in that the O/W/O type emulsion of (b) above is added and mixed into an aqueous solution of a compound capable of forming a water-insoluble precipitate by the water-soluble reaction. How the body is manufactured.
JP9358587A 1987-04-15 1987-04-15 Hollow inorganic powder and grain materials and preparation of same Granted JPS63258642A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9358587A JPS63258642A (en) 1987-04-15 1987-04-15 Hollow inorganic powder and grain materials and preparation of same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9358587A JPS63258642A (en) 1987-04-15 1987-04-15 Hollow inorganic powder and grain materials and preparation of same

Publications (2)

Publication Number Publication Date
JPS63258642A true JPS63258642A (en) 1988-10-26
JPH059133B2 JPH059133B2 (en) 1993-02-04

Family

ID=14086359

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
JP (1) JPS63258642A (en)

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