JPH07206425A - Hexagonal platy zeolite particle material and its production - Google Patents

Hexagonal platy zeolite particle material and its production

Info

Publication number
JPH07206425A
JPH07206425A JP24624993A JP24624993A JPH07206425A JP H07206425 A JPH07206425 A JP H07206425A JP 24624993 A JP24624993 A JP 24624993A JP 24624993 A JP24624993 A JP 24624993A JP H07206425 A JPH07206425 A JP H07206425A
Authority
JP
Japan
Prior art keywords
weight
parts
particle material
sio
zeolite
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
JP24624993A
Other languages
Japanese (ja)
Inventor
Kanemasa Takadou
銀優 高堂
Tatsuo Murakami
達夫 村上
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.)
Fuji Chemical Industries Co Ltd
Original Assignee
Fuji Chemical Industries 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 Fuji Chemical Industries Co Ltd filed Critical Fuji Chemical Industries Co Ltd
Priority to JP24624993A priority Critical patent/JPH07206425A/en
Publication of JPH07206425A publication Critical patent/JPH07206425A/en
Pending legal-status Critical Current

Links

Landscapes

  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)

Abstract

PURPOSE:To efficiently produce a hexagonal platy zeolite particle material with high purity in a short time. CONSTITUTION:An alkali source, an alumina source and a silica source are prepd. as reactive starting materials so as to regulate the amt. of K2O to 7-12 pts.wt., the total amt. of Al2O3 and SiO2 to 5-15 pts.wt. and the molar ratio of SiO2:(Al2O3+SiO2) to 1:2 (expressed in terms of oxides) and the starting materials are mixed by stirring in an aq. soln. while causing gelling. The resulting suspension is heated to produce the objective novel hexagonal platy zeolite having a high aspect ratio of 10-30.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、樹脂補強剤などとして
有用な六角板状ゼオライト粒子物質及び該粒子物質を純
度良く、かつ、効率良く製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hexagonal plate-shaped zeolite particle material useful as a resin reinforcing agent and a method for producing the particle material with high purity and efficiency.

【0002】[0002]

【従来の技術】従来、結晶性アルミノケイ酸塩からなる
天然ゼオライトや、たとえば、水熱結晶化法により得ら
れる合成ゼオライトなどが、イオン交換機能、吸着・分
子ふるい機能、触媒機能などの多機能を有する素材とし
て広く利用されている。たとえば、最近、合成ゼオライ
トの樹脂添加剤としての利用方法、たとえば、ポリ塩化
ビニル樹脂の熱安定性向上、ポリオレフィン系樹脂フィ
ルムの抗ブロッキング性向上させるための添加剤として
利用され、新しい機能性をもつ素材として注目されてい
る。ところが、上記の天然及び/または合成ゼオライト
結晶を、プラスチックなどの補強剤として使用しようと
すると、たとえば、天然品の場合には純度などの品質が
不均一であること、また合成ゼオライト粒子物質は、立
方体あるいは球状の粒子形態をもつものがほとんどであ
るなど、プラスチックなどの補強剤として用いるには、
強度、純度または粒形などの点で満足し得るものではな
かった。
2. Description of the Related Art Conventionally, natural zeolites made of crystalline aluminosilicates and synthetic zeolites obtained by, for example, hydrothermal crystallization have a multi-function such as an ion exchange function, an adsorption / molecular sieving function, and a catalytic function. Widely used as a raw material. For example, recently, synthetic zeolite has been used as a resin additive, for example, as an additive for improving the thermal stability of polyvinyl chloride resin and the anti-blocking property of polyolefin resin film, and has a new functionality. Has attracted attention as a material. However, when it is attempted to use the above natural and / or synthetic zeolite crystals as a reinforcing agent for plastics, for example, in the case of natural products, the quality such as purity is not uniform, and the synthetic zeolite particle material is Most of them have cubic or spherical particle morphology.
It was not satisfactory in terms of strength, purity or grain shape.

【0003】[0003]

【発明が解決しようとする課題】本発明は、プラスチッ
クなどの補強剤として用いることができる強度、純度ま
たは粒形などを有する六角板状ゼオライト粒子物質およ
びその新規な製造法を確立することを目的とする。
DISCLOSURE OF THE INVENTION It is an object of the present invention to establish a hexagonal plate-like zeolite particle material having strength, purity or particle shape and the like, which can be used as a reinforcing agent for plastics and the like, and a novel production method thereof. And

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記問題
点を解決するために鋭意検討した結果、本発明の六角板
状ゼオライト粒子物質で、アスペクト比(投影面積径と
厚さとの比)が10〜30のものが、上記問題点を解決
し得ることを見いだし本発明を完成した。すなわち、本
発明は、アルカリ源としての水酸化カリウム、アルミナ
源およびシリカ源を含有した出発原料を十分に攪拌混合
することにより均一にゲル化させ、次いで得られた懸濁
液を加熱することを特徴とする六角板状ゼオライト粒子
物質及びその製造法である。
Means for Solving the Problems As a result of intensive studies for solving the above problems, the present inventors have found that the hexagonal plate-like zeolite particle substance of the present invention has an aspect ratio (ratio between projected area diameter and thickness). The present invention has been completed by finding that the above-mentioned problems can be solved by the method of 10) to 10). That is, according to the present invention, a starting material containing potassium hydroxide as an alkali source, an alumina source and a silica source is sufficiently agitated and mixed to cause uniform gelation, and then the obtained suspension is heated. It is a characteristic hexagonal plate-like zeolite particle material and a method for producing the same.

【0005】本発明の六角板状ゼオライト粒子物質は、
組成式 K2O :20〜30重量部 Al23 :20〜30重量部 SiO2 :Al23とSiO2 のモル比は1:2 H2O :0〜20重量部 で表される白色の六角板状の無機粉体物質である。
The hexagonal plate-like zeolite particle material of the present invention is
Composition formula K 2 O: 20 to 30 parts by weight Al 2 O 3: 20~30 parts by weight SiO 2: molar ratio of Al 2 O 3 and SiO 2 is 1: 2 H 2 O: expressed in 0 to 20 parts by weight It is a white hexagonal inorganic powder substance.

【0006】本発明の六角板状ゼオライト粒子物質は、
反応出発原料中のアルカリ源、アルミナ源、シリカ源を
各々酸化物として表示した組成が K2O :7〜12重量部 Al23+SiO2 :5〜15重量部 SiO2 :Al23 とSiO2 のモル比は
1:2 である出発原料を水溶液中でゲル化させながら攪拌混合
し、得られた懸濁液を加熱することを特徴とする製法に
より製造することができる。
The hexagonal plate-shaped zeolite particle material of the present invention is
The composition in which the alkali source, the alumina source, and the silica source in the reaction starting materials are represented as oxides is K 2 O: 7 to 12 parts by weight Al 2 O 3 + SiO 2 : 5 to 15 parts by weight SiO 2 : Al 2 O 3 The starting material having a molar ratio of SiO 2 and SiO 2 of 1: 2 is mixed in an aqueous solution with stirring while being gelled, and the resulting suspension is heated to produce a production method.

【0007】本発明のアルカリ源としては、水酸化カリ
ウム、炭酸カリウム、炭酸水素カリウムなどをあげるこ
とができる。上記のアルカリ源は単独または二種以上を
併用して用いることもできる。
Examples of the alkali source of the present invention include potassium hydroxide, potassium carbonate, potassium hydrogen carbonate and the like. The above alkali sources can be used alone or in combination of two or more.

【0008】アルミナ源としては、アルミニウムイオン
やアルミン酸イオンが得られるものであれば良く、たと
えば、水酸化アルミニウムまたは、各種無機酸とのアル
ミニウム塩またはアルミン酸塩、たとえば、塩化アルミ
ニウム、硝酸アルミニウム、硫酸アルミニウムなどを用
いることができる。これら塩は単独または併用して用い
ることもできる。
Any alumina source may be used as long as aluminum ions and aluminate ions can be obtained, and examples thereof include aluminum hydroxide and aluminum salts or aluminates with various inorganic acids, such as aluminum chloride and aluminum nitrate. Aluminum sulfate or the like can be used. These salts can be used alone or in combination.

【0009】シリカ源としては種々のケイ酸塩を用いる
ことができるが、本発明においては水ガラスおよびシリ
カゾルなどが好ましい。
Although various silicates can be used as the silica source, water glass and silica sol are preferred in the present invention.

【0010】本発明の出発原料をゲル化させながら攪拌
混合する場合の反応の温度範囲は60℃を越えない温度
範囲、好ましくは室温から40℃の温度範囲で行う。反
応時間は、使用する原料の組成などにより異なるが、通
常2〜24時間、好ましくは6〜12時間である。
When the starting material of the present invention is stirred and mixed while gelling, the temperature range of the reaction does not exceed 60 ° C., preferably room temperature to 40 ° C. The reaction time varies depending on the composition of the raw materials used and the like, but is usually 2 to 24 hours, preferably 6 to 12 hours.

【0011】次工程での懸濁液の加熱は、還流冷却器と
攪拌機を組み込んだ反応容器に上記の反応で得られた懸
濁液を入れて行うことができる。上記懸濁液の加熱は、
使用する原料の組成などにより異なるが、通常は60〜
120℃の間の適宜な温度範囲で行うが、特に80〜1
10℃の温度範囲が好ましい。上記懸濁液を加熱する時
間は、温度、容量などの反応条件により異なるが、6〜
240時間、好ましくは24〜72時間である。
The heating of the suspension in the next step can be carried out by putting the suspension obtained in the above reaction in a reaction vessel equipped with a reflux condenser and a stirrer. Heating the suspension is
Although it depends on the composition of the raw materials used, etc., usually 60 to
It is carried out in a suitable temperature range between 120 ° C., but especially 80-1
A temperature range of 10 ° C. is preferred. The time for heating the suspension varies depending on the reaction conditions such as temperature and volume, but is 6 to
It is 240 hours, preferably 24-72 hours.

【0012】本発明の目的物は、上記反応生成物を、次
いで、常法に従って濾別し、水洗し、乾燥することによ
り得ることができる。上記反応生成物を濾別する際の水
洗は、洗浄液のpHが10以下になるまで行う。
The object of the present invention can be obtained by subjecting the above reaction product to filtration, washing with water and drying according to a conventional method. Washing with water at the time of separating the reaction product by filtration is carried out until the pH of the washing liquid becomes 10 or less.

【0013】濾過して得られた固体物質の平衡水分は、
10〜20重量部の範囲にあるが、乾燥条件によって、
水分を0〜20重量部にすることが可能であり、この条
件においても六角板状の形態を保持する。乾燥温度は、
乾燥物の水分により異なるが、通常50〜200℃の間
の温度範囲で行うことができ、好ましくは60〜120
℃である。乾燥時間は、乾燥温度などにより異なるが、
通常、1〜24時間である。
The equilibrium water content of the solid substance obtained by filtration is
It is in the range of 10 to 20 parts by weight, but depending on the drying conditions,
It is possible to set the water content to 0 to 20 parts by weight, and the hexagonal plate-like shape is maintained even under these conditions. The drying temperature is
Although it depends on the water content of the dried product, it can be carried out in a temperature range of usually 50 to 200 ° C., preferably 60 to 120.
℃. The drying time depends on the drying temperature, etc.
Usually, it is 1 to 24 hours.

【0014】本発明の製造法で得られた無機粉体物質の
物理化学的性質は、常法に従って、たとえば、化学的組
成は原子吸光法により、水分は強熱減量を測定すること
により求めこの強熱減量(igloss)は試料1gを
取り500℃で恒量となったときの減量を測定すること
により、粉末X線回折スペクトルは粉末X線回折(XR
D;理学電機社製)を用いて求めた。
The physicochemical properties of the inorganic powder substance obtained by the production method of the present invention are determined according to a conventional method, for example, the chemical composition is determined by an atomic absorption method, and the water content is measured by an ignition loss. The ignition loss (igloss) was obtained by taking 1 g of the sample and measuring the weight loss when the sample reached a constant weight at 500 ° C. The powder X-ray diffraction spectrum was measured by powder X-ray diffraction (XR).
D; manufactured by Rigaku Denki Co., Ltd.).

【0015】アスペクト比(投影面積径と厚さとの比)
は、走査型電子顕微鏡にて電子顕微鏡写真を撮影し、写
真の中の六角板状粒子像をスケ−ルを用いて測定するこ
とにより求めた。
Aspect ratio (ratio between projected area diameter and thickness)
Was determined by taking an electron microscope photograph with a scanning electron microscope and measuring the hexagonal plate-shaped particle image in the photograph using a scale.

【0016】比表面積は、B.E.T多点法により測定
し、密度は、JIS K 6220・6・8に準じて測
定した。
The specific surface area is E. The density was measured by the T multipoint method, and the density was measured according to JIS K 6220.6.8.

【0017】本発明の粒子物質は、六角板状結晶という
特異な形状と従来のゼオライト粒子物質に比較してアス
ペクト比が10〜30と大きいためプラスチックなどの
補強剤として使用した場合には極めて有利である。ま
た、該粒子物質は純度良く、かつ、効率よく製造するこ
とができるので工業的にも有利である。
Since the particulate material of the present invention has a unique shape of hexagonal plate-like crystals and a large aspect ratio of 10 to 30 as compared with the conventional zeolite particulate material, it is extremely advantageous when used as a reinforcing agent for plastics and the like. Is. Further, since the particulate matter can be produced with high purity and efficiency, it is industrially advantageous.

【0018】また、本発明の粒子物質は、従来から知ら
れているゼオライトの特徴的な性質、すなわちイオン交
換機能、吸着・分子ふるい機能および触媒機能をもつこ
とにより、石油精製、酸素製造、水素精製、乾燥プロセ
ス、放射性廃棄物処理、洗剤ビルダ−、土壌改質材、飼
料添加物、太陽熱冷凍システムなどに、また樹脂添加剤
としてポリ塩化ビニル樹脂の熱安定性向上、ポリオレフ
ィン系樹脂フィルムの抗ブロッキング性向上剤などにも
利用することができる。
Further, the particulate matter of the present invention has the characteristic properties of conventionally known zeolites, namely, the ion exchange function, the adsorption / molecular sieving function and the catalytic function, so that petroleum refining, oxygen production, hydrogen For refining, drying process, radioactive waste treatment, detergent builder, soil modifier, feed additive, solar heat refrigeration system, etc., and improving the thermal stability of polyvinyl chloride resin as a resin additive, resistance of polyolefin resin film. It can also be used as a blocking property improver.

【0019】また、化粧料基剤、研磨剤、医薬、農薬、
香料、芳香剤などを担持させるための担体または各種ク
ロマトグラフィ−用担体としても利用することができる
など極めて有用である。以下の実施例において本発明を
より詳細に説明する。
Further, cosmetic bases, abrasives, pharmaceuticals, agricultural chemicals,
It is extremely useful because it can be used as a carrier for supporting a fragrance, a fragrance or the like, or as a carrier for various chromatographies. The invention is explained in more detail in the following examples.

【0020】[0020]

【実施例】【Example】

実施例1 蒸留水240mlに水酸化カリウム(KOH:95%)
48.84gを溶解し、水酸化アルミニウム(Al
23:65%)18.83gを加え懸濁液とする。さら
に攪拌しながらコロイダルシリカ(SiO2:20%、
触媒化成工業(株):商品名カタロイド)72.13g
を徐々に滴下する。得られた懸濁液を30℃で6時間、
十分に攪拌し、均一な懸濁液を得た。この反応開始時の
混合物の組成を酸化物で表示すると K2O=10.28重量部、Al23=3.22重量
部、SiO2=3.80重量部であった。次いでこの懸
濁液を還流冷却器と攪拌機を組み込んだ反応容器に移
し、100℃で24時間加熱し、結晶化させた。
Example 1 Potassium hydroxide (KOH: 95%) in 240 ml of distilled water
Dissolve 48.84 g and add aluminum hydroxide (Al
2 O 3 : 65%) (18.83 g) is added to make a suspension. With further stirring, colloidal silica (SiO 2 : 20%,
Catalyst Kasei Kogyo Co., Ltd .: trade name Cataloid) 72.13 g
Is gradually added dropwise. The resulting suspension at 30 ° C. for 6 hours,
After thorough stirring, a uniform suspension was obtained. When the composition of the mixture at the start of this reaction was expressed as an oxide, K 2 O was 10.28 parts by weight, Al 2 O 3 was 3.22 parts by weight, and SiO 2 was 3.80 parts by weight. Then, this suspension was transferred to a reaction vessel equipped with a reflux condenser and a stirrer, and heated at 100 ° C. for 24 hours to be crystallized.

【0021】反応終了後、反応液を冷却し、濾過して得
られた固体物質を洗液のpHが10になるまで洗浄し、
次いで、60℃で24時間乾燥し、白色の無機粉体物質
を得た。この時の収率は99%以上であり、出発物質の
アルミナ源、シリカ源は全て生成物として回収できた。
上記合成方法で得られた無機粉体物質の機器分析の結果
は、下記の表1に示す通りであった。
After completion of the reaction, the reaction solution is cooled and the solid substance obtained by filtration is washed until the pH of the washing solution becomes 10.
Then, it was dried at 60 ° C. for 24 hours to obtain a white inorganic powder substance. The yield at this time was 99% or more, and the alumina source and silica source as starting materials could all be recovered as products.
The results of instrumental analysis of the inorganic powder substance obtained by the above synthesis method are shown in Table 1 below.

【0022】また、当該無機粉体物質の粉末X線回折ス
ペクトルの結果は、図1に示す通りであった。この粉末
X線回折スペクトルのパタ−ンから、上記生成物は高純
度のK型ゼオライトであることが確認できた。また、上
記無機粉体物質が六角板状粒子物質であることは、電子
顕微鏡写真(倍率10000倍)により確認することが
できた。
The result of the powder X-ray diffraction spectrum of the inorganic powder substance was as shown in FIG. From the pattern of this powder X-ray diffraction spectrum, it was confirmed that the above product was a high-purity K-type zeolite. Moreover, it was possible to confirm that the above-mentioned inorganic powder substance was a hexagonal plate-like substance by an electron micrograph (magnification: 10000 times).

【0023】実施例2 実施例1において使用したものと同一の懸濁液を、還流
冷却器と攪拌機を組み込んだ反応容器に移し、80℃で
72時間加熱し、結晶化させた。以下、実施例1と同様
に後処理することにより白色の無機粉体物質を得た。当
該無機粉体物質は、粉末X線回折スペクトルのパタ−ン
から、高純度のK型ゼオライトであり、電子顕微鏡写真
より、六角板状結晶であることが確認できた。
Example 2 The same suspension as that used in Example 1 was transferred to a reaction vessel equipped with a reflux condenser and a stirrer, and heated at 80 ° C. for 72 hours to be crystallized. Then, a post-treatment was carried out in the same manner as in Example 1 to obtain a white inorganic powder substance. From the pattern of the powder X-ray diffraction spectrum, it was confirmed that the inorganic powder substance was high-purity K-type zeolite, and it was confirmed from the electron micrograph that it was a hexagonal plate crystal.

【0024】実施例3 実施例1記載の製法で、出発原料の組成を、 K2O=12.0重量部、Al23=6.05重量部、
SiO2=7.15重量部となるように変更した以外は
実施例1と同様にして反応を行ない白色の無機粉体物質
を得た。該無機粉体物質は、粉末X線回折スペクトルの
パタ−ンから高純度のK型ゼオライトであり、電子顕微
鏡写真より、六角板状結晶であることが確認できた。
Example 3 According to the production method described in Example 1, the composition of the starting materials was as follows: K 2 O = 12.0 parts by weight, Al 2 O 3 = 6.05 parts by weight,
A reaction was performed in the same manner as in Example 1 except that the amount of SiO 2 was changed to 7.15 parts by weight to obtain a white inorganic powder substance. From the pattern of the powder X-ray diffraction spectrum, it was confirmed that the inorganic powder substance was high-purity K-type zeolite, and it was confirmed from the electron micrograph that it was a hexagonal plate crystal.

【0025】[0025]

【表1】 [Table 1]

【0026】[0026]

【発明の効果】本発明により、六角板状結晶という特異
な形状と従来のゼオライト粒子物質に比較してアスペク
ト比が10〜30と大きい、新規な六角板状ゼオライト
粒子物質およびその当該粒子物質を効率よく、かつ、純
度良く、短時間で製造し得る製造法を提供することがで
きた。本発明の粒子物質は、上記の様な優れた性質を有
するためプラスチックなどの補強剤として使用した場合
には極めて有利である。
According to the present invention, a novel hexagonal plate-like zeolite particle material and a specific hexagonal plate-like crystal having a large aspect ratio of 10 to 30 as compared with the conventional zeolite particle material and the particle material thereof are provided. It has been possible to provide a manufacturing method that can be manufactured efficiently and with good purity in a short time. Since the particulate material of the present invention has the above-mentioned excellent properties, it is extremely advantageous when used as a reinforcing agent for plastics and the like.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例1で得られた六角板状K型ゼオ
ライト粒子物質の粉末X線回折スペクトルである。
FIG. 1 is a powder X-ray diffraction spectrum of a hexagonal plate K-type zeolite particle material obtained in Example 1 of the present invention.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 反応出発原料中のアルカリ源、アルミナ
源、シリカ源を各々酸化物として表示した組成が K2O :7〜12重量部 Al23+SiO2 :5〜15重量部 SiO2 :Al23 とSiO2 のモル比は
1:2 である出発原料を水溶液中でゲル化させながら攪拌混合
し、得られた懸濁液を加熱することを特徴とする六角板
状ゼオライト粒子物質の製造法。
1. A composition in which an alkali source, an alumina source, and a silica source in a reaction starting material are expressed as oxides K 2 O: 7 to 12 parts by weight Al 2 O 3 + SiO 2 : 5 to 15 parts by weight SiO 2 : Al 2 O 3 and SiO 2 molar ratio is 1: 2 Hexagonal plate-like zeolite particles characterized in that the starting material is stirred and mixed in an aqueous solution while being gelled, and the resulting suspension is heated The method of manufacturing a substance.
【請求項2】 加熱温度が60〜120℃の範囲である
請求項1記載の六角板状ゼオライト粒子物質の製造法。
2. The method for producing a hexagonal plate-like zeolite particle material according to claim 1, wherein the heating temperature is in the range of 60 to 120 ° C.
【請求項3】 組成式 K2O :20〜30重量部 Al23 :20〜30重量部 SiO2 :Al23とSiO2 のモル比は1:2 H2O :0〜20重量部 で表される六角板状ゼオライト粒子物質。3. A composition formula K 2 O: 20 to 30 parts by weight Al 2 O 3 : 20 to 30 parts by weight SiO 2 : Al 2 O 3 and SiO 2 have a molar ratio of 1: 2 H 2 O: 0 to 20. Hexagonal tabular zeolite particle material expressed in parts by weight. 【請求項4】 アスペクト比が10〜30の範囲である
請求項3記載の六角板状ゼオライト粒子物質。
4. The hexagonal plate-like zeolite particle material according to claim 3, wherein the aspect ratio is in the range of 10 to 30.
JP24624993A 1992-09-10 1993-09-07 Hexagonal platy zeolite particle material and its production Pending JPH07206425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24624993A JPH07206425A (en) 1992-09-10 1993-09-07 Hexagonal platy zeolite particle material and its production

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP4-269750 1992-09-10
JP26975092 1992-09-10
JP24624993A JPH07206425A (en) 1992-09-10 1993-09-07 Hexagonal platy zeolite particle material and its production

Publications (1)

Publication Number Publication Date
JPH07206425A true JPH07206425A (en) 1995-08-08

Family

ID=26537640

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24624993A Pending JPH07206425A (en) 1992-09-10 1993-09-07 Hexagonal platy zeolite particle material and its production

Country Status (1)

Country Link
JP (1) JPH07206425A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999023033A1 (en) * 1997-10-31 1999-05-14 Kao Corporation Aluminosilicate
JP2015199652A (en) * 2014-03-31 2015-11-12 日揮触媒化成株式会社 Tabular particle, and composition for polishing containing the tabular particle

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999023033A1 (en) * 1997-10-31 1999-05-14 Kao Corporation Aluminosilicate
JP2015199652A (en) * 2014-03-31 2015-11-12 日揮触媒化成株式会社 Tabular particle, and composition for polishing containing the tabular particle

Similar Documents

Publication Publication Date Title
JPS58176123A (en) Superpure boehmite and pseudoboehmite and manufacture thereof
EP0196043A2 (en) Massive bodies of maximum aluminum x-type zeolite
US4661332A (en) Zeolite (ECR-18) isostructural with paulingite and a method for its preparation
CN111392745B (en) High-silica-alumina ratio ferrierite, and preparation method and application thereof
US3594121A (en) Dry gel process for preparing zeolite y
JPS62275015A (en) Thermostable zeolite omega, manufacture and use
EP0142349B1 (en) Stoichiometric process for preparing a zeolite of the l type
JPS63500238A (en) Crystalline zeolite LZ-202 and its manufacturing method
US4007253A (en) Production of synthetic zeolite of faujasite structure
JP3547791B2 (en) High heat water resistant high silica zeolite and method for producing the same
JP3322308B2 (en) Synthetic method of zeolite
US5919427A (en) Amorphous aluminosilicate and process for producing the same
JPH07206425A (en) Hexagonal platy zeolite particle material and its production
US5474753A (en) Preparation of crystalline 4A zeolites
US4395388A (en) Synthetic cristobalite
Kuanchertchoo et al. Preparation of uniform and nano‐sized NaA zeolite using silatrane and alumatrane precursors
JP4488691B2 (en) Method for producing faujasite type zeolite
JPS63162520A (en) Production of synthetic mazzite
JP5116326B2 (en) Synthesis method of micro faujasite type zeolite
JP3677807B2 (en) Clinotylolite and synthesis method thereof
JPH06100314A (en) Production of a type zeolite
CN111186846B (en) ITH structure silicon-aluminum molecular sieve and preparation method thereof
JPS6168322A (en) Manufacture of crystalline silicon material
US5549881A (en) Process for preparing a seeded high-silica zeolite having the faujasite topology
JP2793376B2 (en) Method for producing type A zeolite