JPH0629131B2 - Method for producing high-purity kaolinite-like minerals - Google Patents
Method for producing high-purity kaolinite-like mineralsInfo
- Publication number
- JPH0629131B2 JPH0629131B2 JP2230231A JP23023190A JPH0629131B2 JP H0629131 B2 JPH0629131 B2 JP H0629131B2 JP 2230231 A JP2230231 A JP 2230231A JP 23023190 A JP23023190 A JP 23023190A JP H0629131 B2 JPH0629131 B2 JP H0629131B2
- Authority
- JP
- Japan
- Prior art keywords
- kaolinite
- ion exchange
- gel
- product
- minerals
- 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 - Lifetime
Links
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims description 20
- 239000011707 mineral Substances 0.000 title claims description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 238000005342 ion exchange Methods 0.000 claims description 16
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 15
- 238000010335 hydrothermal treatment Methods 0.000 claims description 13
- 239000007864 aqueous solution Substances 0.000 claims description 10
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 6
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 6
- 239000004115 Sodium Silicate Substances 0.000 claims description 5
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 5
- 239000003729 cation exchange resin Substances 0.000 claims description 4
- 229910001415 sodium ion Inorganic materials 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 23
- 239000000047 product Substances 0.000 description 23
- 239000002994 raw material Substances 0.000 description 21
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 19
- 229910052622 kaolinite Inorganic materials 0.000 description 19
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 13
- 238000002441 X-ray diffraction Methods 0.000 description 11
- 239000003456 ion exchange resin Substances 0.000 description 11
- 229920003303 ion-exchange polymer Polymers 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 239000011734 sodium Substances 0.000 description 11
- 239000000203 mixture Substances 0.000 description 8
- 239000004927 clay Substances 0.000 description 7
- 239000000377 silicon dioxide Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 238000002411 thermogravimetry Methods 0.000 description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000005909 Kieselgur Substances 0.000 description 4
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000010453 quartz Substances 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 125000000524 functional group Chemical group 0.000 description 3
- 238000001027 hydrothermal synthesis Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229920001429 chelating resin Polymers 0.000 description 2
- 239000002734 clay mineral Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000001879 gelation Methods 0.000 description 2
- 125000000962 organic group Chemical group 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910001583 allophane Inorganic materials 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- -1 aluminum compound Chemical class 0.000 description 1
- HPTYUNKZVDYXLP-UHFFFAOYSA-N aluminum;trihydroxy(trihydroxysilyloxy)silane;hydrate Chemical compound O.[Al].[Al].O[Si](O)(O)O[Si](O)(O)O HPTYUNKZVDYXLP-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000008119 colloidal silica Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 229910001649 dickite Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 229910052621 halloysite Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 125000000542 sulfonic acid group Chemical group 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、セラミック用原料、セラミックス用バインダ
ー、製紙用フィラー等として多用されており、また新し
い機能材料として注目を集めている高純度カオリナイト
様鉱物の製造法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention is widely used as a raw material for ceramics, a binder for ceramics, a filler for papermaking, and the like, and is a high-purity kaolinite that has been attracting attention as a new functional material. It is related to a method for producing such minerals.
従来からセラミックスの原料として、カオリナイトを主
成分とする天然粘土が用いられている。このカオリナイ
トは粘土鉱物の中のカオリン類の主要な鉱物であって、
白色、灰色又は黄色の高アルミナ鉱物である。一方カオ
リナイトを主成分とする良質の天然粘土、特に愛知県瀬
戸地区で産出する木節粘土、蛙目粘土は、近年の急激な
宅地開発等に起因して産出量が減少しており、これらの
天然粘土に代わる材料として、また層状構造であること
を利用した新規な機能材料として人工粘土の研究開発が
推進されている。Conventionally, natural clay containing kaolinite as a main component has been used as a raw material for ceramics. This kaolinite is the main mineral of kaolins in clay minerals,
It is a white, gray or yellow high alumina mineral. On the other hand, the production of high-quality natural clay mainly composed of kaolinite, especially Kibushi Clay and Frogme Clay, which are produced in the Seto area of Aichi Prefecture, has been decreasing due to rapid housing development in recent years. The research and development of artificial clay is being promoted as a material that replaces the natural clay, and as a new functional material utilizing its layered structure.
カオリナイトの製造法としては、通常水熱合成法が用い
られる。この水熱合成法とは、原材料を水分の存在下で
オートクレーブ内に密閉して一定時間高温高圧状態に保
持することによって所望の鉱物を得る方法であり、各種
人工鉱物の合成手段として広く用いられている。このよ
うな水熱合成法によるカオリナイトの製造法としては、
芝崎,渡村(Clays and Clay Minerals,1983年)らに
よるシリカゾルとアルミナゾルを混合し原料として使用
する方法、アロフェン、珪藻土、モンモリロナイト、
ゼオライト等とアルミニウム化合物を混合し原料として
使用する方法が知られている。A hydrothermal synthesis method is usually used as a method for producing kaolinite. This hydrothermal synthesis method is a method of obtaining a desired mineral by hermetically sealing raw materials in an autoclave in the presence of water and maintaining a high temperature and high pressure for a certain time, and is widely used as a synthetic means for various artificial minerals. ing. As a method for producing kaolinite by such a hydrothermal synthesis method,
Method of mixing silica sol and alumina sol by Clays and Clay Minerals (1983) and using as raw material, allophane, diatomaceous earth, montmorillonite,
A method is known in which zeolite or the like and an aluminum compound are mixed and used as a raw material.
しかしながら上記の方法では、シリカ原料とアルミナ原
料が固体混合又は固体/液体混合であるため非反応性部
分が存在するため反応が100%進行せずカオリナイト含
有率が上がらないという問題点があった。さらに天然原
料を用いた場合は原料中に含まれる金属酸化物、石英等
の不純物がカオリナイト中に残存し粘土特性の低下、着
色といった問題点も有している。例えば、合成品である
シリカゾルとアルミナゾルを混合し原料として使用した
場合、金属酸化物、石英等の不純物の混入はないが水熱
処理温度、水熱処理時間に関係なくカオリナイト含有率
が90%程度で反応は終了し未反応のシリカ、アルミナが
残存する。これはシリカ、アルミナ原料の混合が固体混
合でありそのため均一混合になっていないこと、また方
法上安定剤の除去のために焼成をおこなっていることに
起因し非反応性部分が存在するためと考えられる。残存
する未反応のシリカ、アルミナはカオリナイトの凝集を
を引き起こし粘土特性の低下を招く。さらに珪藻土と塩
化アルミニウムを混合し原料として使用した場合、不純
物として石英、鉄分、その他金属酸化物がカオリナイト
中に混入するうえ原料である珪藻土も残存する。However, the above method has a problem that since the silica raw material and the alumina raw material are solid mixed or solid / liquid mixed, there is a non-reactive portion, so that the reaction does not proceed 100% and the kaolinite content does not increase. . Further, when a natural raw material is used, impurities such as metal oxides and quartz contained in the raw material remain in kaolinite, which causes problems such as deterioration of clay characteristics and coloring. For example, when silica sol and alumina sol, which are synthetic products, are mixed and used as a raw material, there is no mixing of impurities such as metal oxides and quartz, but the kaolinite content is about 90% regardless of the hydrothermal treatment temperature and hydrothermal treatment time. The reaction is completed and unreacted silica and alumina remain. This is because the silica and alumina raw materials were mixed in a solid state and therefore were not homogeneously mixed, and because there was a non-reactive portion due to firing for removing the stabilizer in the method. Conceivable. The remaining unreacted silica and alumina cause agglomeration of kaolinite, resulting in deterioration of clay characteristics. Further, when diatomaceous earth and aluminum chloride are mixed and used as a raw material, quartz, iron, and other metal oxides are mixed as impurities in kaolinite, and the raw material diatomaceous earth also remains.
本発明の目的は、従来の方法よりも不純物及び未反応物
を含まない高純度のカオリナイト様鉱物を製造すること
ができる方法を提供するものである。An object of the present invention is to provide a method capable of producing a high-purity kaolinite-like mineral containing no impurities and unreacted substances as compared with the conventional method.
本発明者らは上記問題を解決するために鋭意検討を行っ
た結果、本発明のカオリナイト様鉱物の製造法を得るに
至った。すなわち本発明は、ケイ酸ソーダ水溶液と硫酸
アルミニウム水溶液をpH=4〜12に維持しながら均一に
混合ゲル化し、ついでイオン交換樹脂を用い含有ナトリ
ウムイオンをプロトンにイオン交換した後、該ゲルを水
熱処理することを特徴とする高純度カオリナイト様鉱物
の製造法である。As a result of intensive studies to solve the above problems, the present inventors have arrived at the method for producing a kaolinite-like mineral of the present invention. That is, according to the present invention, a sodium silicate aqueous solution and an aluminum sulfate aqueous solution are uniformly mixed and gelled while maintaining pH = 4 to 12, and then sodium ions contained therein are ion-exchanged with protons using an ion exchange resin, and then the gel is water-exchanged. It is a method for producing a high-purity kaolinite-like mineral characterized by heat treatment.
以下、本発明を具体的に説明する。Hereinafter, the present invention will be specifically described.
本発明におけるカオリナイト様鉱物とは化学式{Al2
Si2O5(OH)4}で表されるシリカ層とアルミナ
層が1:1で構成された層状アルミノケイ酸塩である。
具体的にはカオリナイト、ディッカイト、ハロイサイト
等を挙げることができる。The kaolinite-like mineral in the present invention has a chemical formula {Al 2
It is a layered aluminosilicate in which a silica layer represented by Si 2 O 5 (OH) 4 } and an alumina layer are constituted by 1: 1.
Specific examples thereof include kaolinite, dickite, halloysite and the like.
本発明においてケイ酸ソーダ水溶液と硫酸アルミニウム
水溶液をpH=4〜12に維持しながら均一に混合ゲル化を
行う。上記のpH範囲以外でのゲル化は、シリカまたはア
ルミナの溶解領域になるため均一なシリカ・アルミナゲ
ルを得ることはできない。よってゲル化はpH4〜12好ま
しくはpH6〜8で行い、必要によりアルカリ,酸を添加
することができる。混合方法には特に制限はないが、シ
リカ、アルミナの分散性を向上させるためには撹拌しな
がら連続混合を行うことが好ましい。また合成ゲル中の
Si/Alは水熱処理における副生成物抑制のためにS
i/Al=1に近いことが好ましい。In the present invention, the sodium silicate aqueous solution and the aluminum sulfate aqueous solution are uniformly mixed and gelled while maintaining pH = 4 to 12. Gelation in a pH range other than the above results in a dissolution region of silica or alumina, so that a uniform silica-alumina gel cannot be obtained. Therefore, gelation is performed at pH 4 to 12, preferably pH 6 to 8, and alkali and acid can be added if necessary. The mixing method is not particularly limited, but continuous mixing is preferably performed with stirring in order to improve the dispersibility of silica and alumina. Further, Si / Al in the synthetic gel is S for suppressing by-products in hydrothermal treatment.
It is preferably close to i / Al = 1.
本発明におけるイオン交換に用いられるイオン交換樹脂
は官能基にスルホン酸基またはカルボン酸基を有するカ
チオン交換性イオン交換樹脂である。イオン交換樹脂が
プロトン型である以外はイオン交換容量等は特に制限は
なく、イオン交換に用いられるゲル中のナトリウム量に
より選択することができる。イオン交換方法としては、
バッチ式,フロー式等特に制限はないが、水熱処理にお
いて残存ナトリウムが結晶化を阻害することより結晶化
促進のためにはNa/Alが0.1以下になるようにイオ
ン交換することが好ましい。イオン交換樹脂量及び反応
温度は、イオン交換樹脂の過剰使用または高温でのイオ
ン交換によりアルミニウムの溶解が促進されSi/Al
の組成変化を引き起こすため、温和な条件で行うことが
好ましい。例えば含有ナトリウム量の2倍等量以下のイ
オン交換樹脂を用い、室温で数回イオン交換を繰り返し
行うことにより組成変化なくプロトン型にイオン交換を
行うことができる。The ion exchange resin used for the ion exchange in the present invention is a cation exchangeable ion exchange resin having a sulfonic acid group or a carboxylic acid group as a functional group. The ion exchange capacity and the like are not particularly limited except that the ion exchange resin is a proton type, and can be selected depending on the amount of sodium in the gel used for ion exchange. As an ion exchange method,
Although there is no particular limitation such as batch type and flow type, it is preferable to perform ion exchange so that Na / Al is 0.1 or less in order to promote crystallization because residual sodium inhibits crystallization in hydrothermal treatment. The amount of ion-exchange resin and the reaction temperature are set so that the dissolution of aluminum is promoted by the excessive use of the ion-exchange resin or the ion-exchange at high temperature.
It is preferable to carry out the treatment under mild conditions because it causes a change in composition. For example, an ion exchange resin having an amount equal to or less than twice the content of sodium is used, and ion exchange can be carried out to a proton type without changing the composition by repeating ion exchange several times at room temperature.
本発明における水熱処理は通常のオートクレーブ又は高
圧カップを用いて行うことができる。水熱処理における
スラリー濃度、反応温度、反応時間は特に制限されない
が、スラリー濃度は1〜30wt%、反応温度は100℃以
上、反応時間は1時間以上行うことが好ましい。また必
要により撹拌の実施及び/又は種晶の添加により反応時
間を短縮することができる。The hydrothermal treatment in the present invention can be carried out using an ordinary autoclave or a high pressure cup. The slurry concentration, reaction temperature, and reaction time in the hydrothermal treatment are not particularly limited, but the slurry concentration is preferably 1 to 30 wt%, the reaction temperature is 100 ° C. or higher, and the reaction time is 1 hour or longer. If necessary, the reaction time can be shortened by performing stirring and / or adding seed crystals.
このような水熱処理により、従来の方法において生成率
が90%程度であったのに比べ100%近い生成率でカオリ
ナイト様鉱物が生成できる。By such a hydrothermal treatment, a kaolinite-like mineral can be produced at a production rate close to 100% as compared with the production rate of about 90% in the conventional method.
以下、実施例により本発明を詳細に述べるが、本発明は
これらに限定されるものではない。Hereinafter, the present invention will be described in detail with reference to Examples, but the present invention is not limited thereto.
実施例1 原料として3号水ガラス(SiO2=29.3wt%,Na2
O=9.35wt%)と硫酸アルミニウム(Al2O3=8.02
wt%)を用い、Si/Al=1となるように撹拌しなが
ら原料を連続的に混合した。同時に反応pHが6〜8とな
るように水酸化ナトリウムを添加し中和することにより
シリカ・アルミナゲルを調製した。このゲルの組成分析
を行ったところ、Si/Al=1,Na/Al=0.25で
あった。Example 1 No. 3 water glass (SiO 2 = 29.3 wt%, Na 2 as a raw material)
O = 9.35 wt%) and aluminum sulfate (Al 2 O 3 = 8.02)
wt%), and the raw materials were continuously mixed while stirring so that Si / Al = 1. At the same time, a silica-alumina gel was prepared by adding sodium hydroxide and neutralizing it so that the reaction pH became 6-8. When the composition of this gel was analyzed, Si / Al = 1 and Na / Al = 0.25.
つぎにイオン交換樹脂を用いゲル中のナトリウムをプロ
トンにイオン交換した。イオン交換樹脂はオルガノ製カ
チオン交換樹脂アンバーライト200C(官能基=スルホ
ン酸,イオン交換容量=1.75mep)をゲル中のナトリウム
に対して2倍等量用い、室温にてイオン交換した。また
再度このゲルの組成分析を行ったところ、Si/Al=
1,Na/Al=0.01であった。Next, sodium in the gel was ion-exchanged for protons using an ion-exchange resin. As the ion exchange resin, cation exchange resin Amberlite 200C (functional group = sulfonic acid, ion exchange capacity = 1.75 mep) manufactured by Organo was used in an amount twice as much as that of sodium in the gel, and ion exchange was performed at room temperature. When the composition of this gel was analyzed again, Si / Al =
1, Na / Al = 0.01.
上記原料ゲルをスラリー濃度5wt%になるようにオート
クレーブに仕込み、220℃、10日間水熱処理を行った。
冷却後、水洗過、乾燥し生成物を得た。得られた生成
物のX線回折結果を第1図に示す。The above raw material gel was charged into an autoclave so that the slurry concentration was 5 wt%, and hydrothermal treatment was performed at 220 ° C. for 10 days.
After cooling, it was washed with water and dried to obtain a product. The X-ray diffraction result of the obtained product is shown in FIG.
生成物はカオリナイト様鉱物のX線パターンのみを示し
ていた。また熱重量分析(TG)によってカオリナイト
の構造水の脱水にともなう重量減少を測定しカオリナイ
トの生成量を定量したところ、生成物中のカオリナイト
含有率は98%であった。The product showed only an X-ray pattern of kaolinite-like minerals. Further, the weight loss of kaolinite due to dehydration of structured water was measured by thermogravimetric analysis (TG) to quantify the amount of kaolinite produced, and the content of kaolinite in the product was 98%.
実施例2 実施例1において、イオン交換樹脂にオルガノ製カチオ
ン交換樹脂アンバーライトIRC−84(官能基=カルボ
ン酸,イオン交換容量3.5mep)を用いた以外は同様の操
作を行い生成物を得た。イオン交換後のゲルの組成分析
を行なったところ、Si/Al=1,Na/Al=0.03
であった。得られた生成物のX線回析結果を第2図に示
す。Example 2 A product was obtained by performing the same operation as in Example 1 except that the cation exchange resin Amberlite IRC-84 (functional group = carboxylic acid, ion exchange capacity 3.5 mep) manufactured by Organo was used as the ion exchange resin. . When the composition of the gel after ion exchange was analyzed, Si / Al = 1, Na / Al = 0.03
Met. The X-ray diffraction result of the obtained product is shown in FIG.
実施例1と同様に生成物は高純度なカオリナイト様鉱物
であることがわかる。また熱重量分析より、生成物中の
カオリナイトの含有率は97%であった。As in Example 1, it can be seen that the product is a high-purity kaolinite-like mineral. The content of kaolinite in the product was 97% by thermogravimetric analysis.
比較例1 実施例1において、イオン交換を行わなかった以外は同
様の操作を行い生成物を得た。得られた生成物のX線回
折結果を第3図に示す。Comparative Example 1 A product was obtained by performing the same operation as in Example 1 except that ion exchange was not performed. The X-ray diffraction result of the obtained product is shown in FIG.
第3図から明らかな様にX線回折図にカオリナイト様鉱
物のピークは現れず、カオリナイト様鉱物は生成してい
ないことがわかる。As is clear from FIG. 3, the peak of the kaolinite-like mineral does not appear in the X-ray diffraction pattern, and it is understood that the kaolinite-like mineral is not formed.
比較例2 実施例1において、イオン交換樹脂の代わりに塩酸を用
いた以外は同様の操作を行い生成物を得た。イオン交換
後のゲルの組成分析を行ったところ、Si/Al=1.
8,Na/Al=0.10でありアルミの溶解が起きている
ことがわかる。得られた生成物のX線回折結果を第4図
に示す。Comparative Example 2 A product was obtained by performing the same operation as in Example 1 except that hydrochloric acid was used instead of the ion exchange resin. When the composition of the gel after ion exchange was analyzed, Si / Al = 1.
8, Na / Al = 0.10, indicating that aluminum is melting. The X-ray diffraction result of the obtained product is shown in FIG.
実施例1と同様に生成物はカオリナイト様鉱物のみであ
ることがわかる。また熱重量分析により、生成物中のカ
オリナイト含有率は45%であった。As in Example 1, it can be seen that the product is only kaolinite-like minerals. Further, the thermogravimetric analysis revealed that the kaolinite content in the product was 45%.
比較例3 原料としてコロイダルシリカ(SiO2=20wt%)とア
ルミナゾル(Al2O3=10wt%)を用い、Si/Al
=1となるように混合、撹拌した。ついで乾燥、さらに
安定剤である酢酸を除去するために600℃、1時間の焼
成処理を施し、水熱処理に用いる原料ゲルとした。Comparative Example 3 Using colloidal silica (SiO 2 = 20 wt%) and alumina sol (Al 2 O 3 = 10 wt%) as raw materials, Si / Al
They were mixed and stirred so that = 1. Then, the raw material gel was dried and calcined at 600 ° C. for 1 hour to remove acetic acid as a stabilizer to obtain a raw material gel used for hydrothermal treatment.
上記原料ゲルをスラリー濃度5wt%になるようにオート
クレーブに仕込み、220℃、10日間水熱処理を行った。
冷却後、水洗過、乾燥し生成物を得た。得られた生成
物のX線回折結果を第5図に示す。The above raw material gel was charged into an autoclave so that the slurry concentration was 5 wt%, and hydrothermal treatment was performed at 220 ° C. for 10 days.
After cooling, it was washed with water and dried to obtain a product. The X-ray diffraction result of the obtained product is shown in FIG.
生成物はカオリナイト様鉱物のX線回折パターンのみを
示していた。また熱重量分析により、生成物中のカオリ
ナイト含有率は90%であった。The product showed only the X-ray diffraction pattern of kaolinite-like minerals. Moreover, the kaolinite content in the product was 90% by thermogravimetric analysis.
比較例4 原料に珪藻土と塩化アルミニウムを用い、Si/Al=
1となるように混合、撹拌した。次いでオートクレーブ
に仕込み、220℃、10日間水熱処理を行なった。冷却
後、水洗過、乾燥し生成物を得た。得られた生成物の
X線回折結果を第6図に示す。Comparative Example 4 Si / Al = using diatomaceous earth and aluminum chloride as raw materials
The mixture was mixed and stirred so as to be 1. Then, it was charged into an autoclave and subjected to hydrothermal treatment at 220 ° C. for 10 days. After cooling, it was washed with water and dried to obtain a product. The X-ray diffraction result of the obtained product is shown in FIG.
生成物はカオリナイト様鉱物と不純物として石英のX線
回折パターンを示していた。また熱重量分析より、生成
物中のカオリナイト含有率は50%であった。The product showed an X-ray diffraction pattern of kaolinite-like mineral and quartz as an impurity. The kaolinite content in the product was 50% by thermogravimetric analysis.
〔発明の効果〕 以上述べた通り、本発明によればケイ酸ソーダ水溶液と
硫酸アルミニウム水溶液を用い混合中和によりケイ酸ソ
ーダ水溶液と硫酸アルミニウム水溶液をpH4〜12に維持
しながら均一に混合ゲル化し、ついでカチオン交換樹脂
を用い含有ナトリウムイオンをプロトンにイオン交換し
た後水熱処理を行うことにより、従来の方法よりも不純
物及び未反応物を含まない高純度のカオリナイト様鉱物
を合成することができる。 [Effects of the Invention] As described above, according to the present invention, a sodium silicate aqueous solution and an aluminum sulfate aqueous solution are mixed and neutralized to uniformly mix and gelate the sodium silicate aqueous solution and the aluminum sulfate aqueous solution while maintaining the pH at 4 to 12. Then, by performing ion exchange of the contained sodium ions into protons using a cation exchange resin and then performing hydrothermal treatment, it is possible to synthesize a high-purity kaolinite-like mineral containing no impurities and unreacted substances as compared with the conventional method. .
第1図ないし第6図は、実施例1〜2及び比較例1〜4
で得られたX線回折測定の夫々の結果を示す図である。1 to 6 show Examples 1-2 and Comparative Examples 1-4.
It is a figure which shows each result of the X-ray-diffraction measurement obtained by.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 大崎 恭 山口県新南陽市大神1丁目26番22号 (72)発明者 鮫島 宗一郎 山口県新南陽市宮の前2丁目6番10号 東 ソー自彊寮 (72)発明者 里川 重夫 愛知県名古屋市北区田幡2丁目14番8号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kyo Osaki 1-226-22 Ogami, Shinnanyo-shi, Yamaguchi Prefecture (72) Inventor Soichiro Samejima 2-6-10 Miyanoma, Shinnanyo-shi Tosoh Jijo Dormitory ( 72) Inventor Shigeo Satokawa 2-14-8 Tabata, Kita-ku, Nagoya, Aichi Prefecture
Claims (1)
溶液をpH=4〜12に維持しながら均一に混合ゲル化し、
次いでカチオン交換樹脂を用い含有ナトリウムイオンを
プロトンにイオン交換した後、該ゲルを水熱処理するこ
とを特徴とする高純度カオリナイト様鉱物の製造法。1. A sodium silicate aqueous solution and an aluminum sulfate aqueous solution are uniformly mixed and gelled while maintaining pH = 4 to 12,
Next, a method for producing a high-purity kaolinite-like mineral, which comprises subjecting the gel to ion exchange of contained sodium ions with a cation exchange resin, and then subjecting the gel to hydrothermal treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2230231A JPH0629131B2 (en) | 1990-08-31 | 1990-08-31 | Method for producing high-purity kaolinite-like minerals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2230231A JPH0629131B2 (en) | 1990-08-31 | 1990-08-31 | Method for producing high-purity kaolinite-like minerals |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04114914A JPH04114914A (en) | 1992-04-15 |
| JPH0629131B2 true JPH0629131B2 (en) | 1994-04-20 |
Family
ID=16904596
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2230231A Expired - Lifetime JPH0629131B2 (en) | 1990-08-31 | 1990-08-31 | Method for producing high-purity kaolinite-like minerals |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0629131B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100308520B1 (en) * | 1999-06-01 | 2001-11-05 | 김충섭 | A Process for Production of Polysilicate microgels as Retention and Drainage Aids in Papermaking |
| JP2017007869A (en) * | 2013-11-11 | 2017-01-12 | コニカミノルタ株式会社 | Method for producing tubular aluminum silicate |
-
1990
- 1990-08-31 JP JP2230231A patent/JPH0629131B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04114914A (en) | 1992-04-15 |
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