JPH0621029B2 - Method for producing raw material for kaolinite synthetic clay - Google Patents
Method for producing raw material for kaolinite synthetic clayInfo
- Publication number
- JPH0621029B2 JPH0621029B2 JP63310540A JP31054088A JPH0621029B2 JP H0621029 B2 JPH0621029 B2 JP H0621029B2 JP 63310540 A JP63310540 A JP 63310540A JP 31054088 A JP31054088 A JP 31054088A JP H0621029 B2 JPH0621029 B2 JP H0621029B2
- Authority
- JP
- Japan
- Prior art keywords
- kaolinite
- raw material
- synthetic clay
- powder
- raw materials
- 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
- 239000002994 raw material Substances 0.000 title claims description 31
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 title claims description 21
- 229910052622 kaolinite Inorganic materials 0.000 title claims description 21
- 239000004927 clay Substances 0.000 title claims description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 235000012239 silicon dioxide Nutrition 0.000 claims description 15
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 11
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 10
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 8
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 8
- 239000004571 lime Substances 0.000 claims description 8
- 230000002378 acidificating effect Effects 0.000 claims description 4
- 239000000843 powder Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 12
- 241000209094 Oryza Species 0.000 description 10
- 235000007164 Oryza sativa Nutrition 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 10
- 235000009566 rice Nutrition 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 8
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 6
- 239000010903 husk Substances 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 238000004380 ashing Methods 0.000 description 5
- 239000010453 quartz Substances 0.000 description 5
- 239000004575 stone Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 229910000323 aluminium silicate Inorganic materials 0.000 description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 4
- 239000000920 calcium hydroxide Substances 0.000 description 4
- 235000011116 calcium hydroxide Nutrition 0.000 description 4
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 4
- 239000000292 calcium oxide Substances 0.000 description 4
- 235000012255 calcium oxide Nutrition 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- 239000004809 Teflon Substances 0.000 description 3
- 229920006362 Teflon® Polymers 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000010335 hydrothermal treatment Methods 0.000 description 3
- 229910052573 porcelain Inorganic materials 0.000 description 3
- 238000000634 powder X-ray diffraction Methods 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241000209504 Poaceae Species 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000010433 feldspar Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000010445 mica Substances 0.000 description 2
- 229910052618 mica group Inorganic materials 0.000 description 2
- 229910052651 microcline Inorganic materials 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- -1 aluminum compound Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000008119 colloidal silica Substances 0.000 description 1
- 210000002808 connective tissue Anatomy 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- MKTRXTLKNXLULX-UHFFFAOYSA-P pentacalcium;dioxido(oxo)silane;hydron;tetrahydrate Chemical compound [H+].[H+].O.O.O.O.[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O MKTRXTLKNXLULX-UHFFFAOYSA-P 0.000 description 1
- 239000000941 radioactive substance Substances 0.000 description 1
- 239000012070 reactive reagent Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910052905 tridymite Inorganic materials 0.000 description 1
Landscapes
- Silicon Compounds (AREA)
- 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、カオリナイト質合成粘土を工業的に量産する
ための原料の製造方法に関する。The present invention relates to a method for producing a raw material for industrially mass-producing a kaolinitic synthetic clay.
従来、カオリナイト質合成粘土を得るための原料として
は、次のようなものが知られている。Conventionally, the following materials have been known as raw materials for obtaining kaolinite synthetic clay.
i.高結晶質の珪酸塩ないしアルミノ珪酸塩など。i. Highly crystalline silicate or aluminosilicate.
ii.非晶質もしくは低結晶質の天然産の珪酸塩、あるい
はアルミノ珪酸塩など。ii. Amorphous or low crystalline naturally occurring silicate or aluminosilicate.
iii.易反応性の高純度人工試薬類(コロイダルシリカ
など)など。iii. Easily reactive high-purity artificial reagents such as colloidal silica.
ところが、かゝる従来公知のカオリナイト質合成粘土を
製する原料には、次のような問題点が指摘されていた。However, the following problems have been pointed out in the raw materials for producing such conventionally known kaolinite synthetic clay.
即ち、上記iの珪酸塩ないしアルミノ珪酸塩を使用する
場合には、遊離の石英、雲母などの不純物がそのままの
形で多量に残留してしまい、この不純物を完全に消失さ
せるには300℃以上の高温で数十日以上も長期間に亙っ
て水熱処理する必要があるので、生産性の面で難点があ
り、また、上記iiの原料を用いる場合には、水簸分級と
いう極めて効率が悪く、手間の要する厄介な選別処理を
施して原料を精選する必要があり、 さらに、上記iiiの原料を用いる方法では、非常に希薄
な液状にして処理しなければならぬため収率が悪く、か
つ、原料が極めて高価で経済的ではなかった。That is, when the silicate or aluminosilicate of the above i is used, a large amount of impurities such as free quartz and mica remain as they are, and 300 ° C or more is required to completely eliminate the impurities. Since it is necessary to carry out hydrothermal treatment at a high temperature for several tens of days or more for a long period of time, there is a problem in terms of productivity, and when the raw material of the above ii is used, elutriation classification is extremely efficient. Bad, it is necessary to perform a troublesome and troublesome selection process to select the raw materials, and further, in the method using the raw material iii, the yield is poor because it has to be processed in a very dilute liquid state, Moreover, the raw materials were extremely expensive and not economical.
本発明は、従来におけるカオリナイト質合成粘土の製造
技術に前述のごとき難点があったことに鑑みて為された
もので、天然粘土に近いカオリナイト質の合成粘土の効
率的生産に適した原料を、工業的に量産することができ
る新方法を提供することを技術的課題とするものであ
る。The present invention has been made in view of the above-mentioned drawbacks in the conventional production technique of kaolinitic synthetic clay, and is a raw material suitable for efficient production of kaolinitic synthetic clay close to natural clay. It is a technical object to provide a new method capable of industrial mass production.
本発明者らは、上記技術的課題を解決すべく簡易かつ安
価に易反応性のカオリナイト質合成粘土を製するに適し
た原料を求めて試行錯誤的試験研究を繰り返してきたと
ころ、偶然にも i.含水珪酸石灰系化合物を酸性雰囲気中に曝らすと、
珪酸と石灰の結合組織が簡単に破壊されて含水珪酸が遊
離する事実、 ii.また、米・麦などの生産工程で派生する籾殻を500
〜900℃で酸化焼成して灰化するとカーボンを殆ど含ま
ず、非晶質珪酸を主成分とする粉末が生成される事実、 を発見した。The present inventors have repeated trial and error test research for raw materials suitable for producing easily and inexpensively easily reactive kaolinite synthetic clay to solve the above technical problems, and by chance, I. When a hydrous silicate-based compound is exposed to an acidic atmosphere,
The fact that the connective tissue of silicic acid and lime is easily destroyed and hydrous silicic acid is liberated, ii. In addition, 500 rice husks derived from the production process of rice, wheat, etc.
It was discovered that when ashing is performed by oxidative firing at ~ 900 ° C, a powder containing almost no carbon and containing amorphous silicic acid as the main component is produced.
そこで、この発見により知得した新事実の産業技術的に
利用するための途を求めて、さらに実用化のための研究
を進め、上記iの処理を施して得た含水珪酸、または上
記iiの非晶質珪酸に易反応性のアルミニウム化合物を加
えて水熱処理を施してみた結果、前述した従来のカオリ
ナイト質合成粘土を製造上の隘路が一挙に解消し、本発
明に到達した次第である。Therefore, in order to find a way to utilize the new facts obtained from this discovery in industrial technology, further research for practical application is carried out, and the hydrous silicic acid obtained by the above treatment i or the above ii As a result of performing a hydrothermal treatment by adding an easily reactive aluminum compound to amorphous silicic acid, the bottleneck in the production of the above-mentioned conventional kaolinite synthetic clay was solved at once and the present invention was reached. .
即ち、本発明が上記技術的課題を解決するため採用した
第1の方法的手段は、各種珪酸質原料粉末に生石灰ある
いは消石灰をCaO/SiO2+Al2O3モル比が0.5〜2.0の範囲
になるように混合し、これに水を加えて150℃以上で水
熱反応させて含水珪酸石灰化合物を生成せしめた後、酸
性雰囲気中に曝すことによって難反応性の石英を易反応
性の珪酸に変化させるというものである。That is, the first method means adopted by the present invention to solve the above technical problems is to use quick lime or slaked lime in various siliceous raw material powders in a CaO / SiO 2 + Al 2 O 3 molar ratio of 0.5 to 2.0. After mixing so that water is added to the mixture and hydrothermal reaction is carried out at 150 ° C or higher to generate hydrous silicate lime compound, by exposing it to an acidic atmosphere, difficult-to-react quartz is converted into easily-reactive silica. It is to change.
しかして、この第1の方法で出発物質として使用する珪
酸質原料は、珪酸分の多いものであれば良く、特に制限
はない。また、石灰質原料としては、粉末生石灰や粉末
消石灰を用いるのが望ましい。The siliceous raw material used as the starting material in the first method is not particularly limited as long as it has a large silicic acid content. Further, it is desirable to use powder quicklime or powder slaked lime as the calcareous raw material.
こうして得られる含水珪酸石灰化合物は、ゾノトライト
(6CaO・6SiO2・H2O)や、11Åトバモライト(5CaO・6SiO2・5H
2O)などの結晶質物や、その他のゲル状物、あるいはAl、
Fe、K、Naなどの各イオンを含んだものなど結晶構造の違
いにより多種類のものが存在するが、何れも本発明の目
的を達成するカオリナイト質合成粘土用原料として有効
である。The hydrous silicate lime compound thus obtained is zonotolite.
(6CaO ・ 6SiO 2・ H 2 O) and 11Åtobermorite (5CaO ・ 6SiO 2・ 5H
2 O) and other crystalline substances, other gel-like substances, or Al,
There are various kinds of materials such as those containing respective ions such as Fe, K and Na depending on the difference in crystal structure, and all of them are effective as raw materials for kaolinite synthetic clay for achieving the object of the present invention.
次に、本発明が上記技術的課題を解決するため採用した
第2の方法的手段は、イネ科植物の籾殻を500〜900℃の
酸化雰囲気中で燃焼させて灰化することにより、易反応
性の非晶質珪酸を主成分とする粉末を生成せしめるとい
うものである。Next, the second method means adopted by the present invention to solve the above technical problems is to easily react by burning rice husks of grasses in an oxidizing atmosphere at 500 to 900 ° C. for ashing. This is to generate a powder containing a crystalline amorphous silicic acid as a main component.
しかして、この第2の方法で出発物質として使用するイ
ネ科植物の籾殻としては、我が国の稲作農業を通じ副産
物として大量に産出され、煙害の原因として廃棄処分に
難渋している籾殻が好適であり、かゝる米の籾殻を灰化
することによって、SiO2 90 %以上の良質の非晶質珪酸
を得ることができる。この場合、灰化条件としては500
℃以上で900 ℃以下が望ましい。これは、500 ℃以下で
はカーボンが残留し易いこと、900 ℃以上ではクリスト
バライトやトリジマイトなどの結晶質珪酸の同質異像が
生成し易い等、といった欠点が生ずるからである。な
お、灰化にあたっては、カーボンを残留させないために
は十分な酸素供給を行うことが必要である。Therefore, as the rice husk of the Gramineae plant used as the starting material in the second method, the rice husk which is produced in large quantities as a by-product through rice cultivation in Japan and is difficult to dispose of due to smoke damage is preferable. By ashing such rice husks, it is possible to obtain high-quality amorphous silicic acid having a SiO 2 content of 90% or more. In this case, the ashing condition is 500
It is desirable that the temperature is above ℃ and below 900 ℃. This is because carbon is likely to remain at 500 ° C or lower, and homomorphism of crystalline silicic acid such as cristobalite or tridymite is easily generated at 900 ° C or higher. In addition, in the ashing, it is necessary to supply sufficient oxygen to prevent carbon from remaining.
また、上記した第1の発明方法および第2の発明方法に
よって得た原料を用いてカオリナイト質合成粘土を製造
する場合には、まずカオリナイトの組成比(Al/Si原子比
で1付近)になるよう前記各原料に易反応性のアルミニ
ウム源(例えば、塩化アルミニウム、硝酸アルミニウ
ム、ゲル状水酸化アルミニウム、アルミナゾルなど)を
適量加え、pH2付近の酸性領域下で150〜250℃で数時間
以上水熱反応させる。このように処理すると、純白でカ
オリナイトを主成分とする良質の合成粘土を容易に得る
ことができる。In the case of producing a kaolinite synthetic clay using the raw materials obtained by the above-mentioned first and second invention methods, first, the kaolinite composition ratio (Al / Si atomic ratio is about 1) To each of the above raw materials, an easily reactive aluminum source (eg, aluminum chloride, aluminum nitrate, gelled aluminum hydroxide, alumina sol, etc.) is added in an appropriate amount, and the pH is adjusted to 150 to 250 ° C. for several hours or more in an acidic region near pH 2. Hydrothermally react. When treated in this manner, a pure white, high-quality synthetic clay containing kaolinite as a main component can be easily obtained.
本発明の具体的内容を、図面を参照しつゝ実施例を上げ
て更に詳しく説明する。The specific contents of the present invention will be described in more detail with reference to the drawings and by way of examples.
実施例 珪酸質原料として、福井県産の低級陶石(試料:A)を44
μ以下に紛砕して用いた。この陶石粉末の化学組成は第
1表に、また鉱物組成は第1図の粉末X線回折図に示す
とおりである。上記陶石粉末に対し消石灰をCaO/SiO2+
Al2O3モル比が1になるように混合して4gとし、更に
原料と水の比が重量比が1対4になるように水を加えて
ステンレス製容器に入れ、オートクレーブ中で180℃で1
2時間水熱反応させた。こうして得られた処理物をブフ
ナーロートで吸引脱水し、100℃で乾燥した(試料B)。
この粉末は第1図の粉末X線回折図に示したとおり、殆
どが含水珪酸石灰化合物(この場合生成物は11Åトバモ
ライト)に変化しており、遊離の石英は全く残留してい
なかった。Example As a siliceous raw material, 44 low-grade porcelain stones (Sample: A) produced in Fukui Prefecture are used.
It was used after being pulverized to μ or less. The chemical composition of this porcelain stone powder is shown in Table 1, and the mineral composition is shown in the powder X-ray diffraction pattern of FIG. Slaked lime is added to the above-mentioned pottery stone powder by CaO / SiO 2 +
The Al 2 O 3 molar ratio was mixed to 1 to 4 g, and water was added so that the weight ratio of the raw material and water was 1: 4, and the mixture was placed in a stainless steel container and placed in an autoclave at 180 ° C. In 1
It was hydrothermally reacted for 2 hours. The treated product thus obtained was suction-dewatered with a Buchner funnel and dried at 100 ° C. (Sample B).
As shown in the powder X-ray diffraction pattern of FIG. 1, most of this powder was changed to a hydrous silicate lime compound (in this case, the product was 11Åtobermorite), and no free quartz remained.
次に、これに塩酸を加えてpH2付近とした後、カオリナ
イト組成比(Al/Si原子比≒1)になるように2モルの塩
化アルミニウム水溶液を適量加えてテフロン製容器に入
れ、230℃で48時間水熱反応させた。そして、この処理
物を遠心分離器で個・液を分離し、40℃で乾燥した(試
料C)。この粉末は純白で第1表と第1図に示すごと
く、Al2O3およびカオリナイト含有率が頗る高く、遊離
の石英や微斜長石、雲母などの不純物を全く含まない良
質のカオリナイト質合成粘土であることが確認された。Next, add hydrochloric acid to this to adjust the pH to around 2, then add an appropriate amount of 2 mol of an aluminum chloride aqueous solution so that the kaolinite composition ratio (Al / Si atomic ratio ≈ 1) and put it in a Teflon container at 230 ° C. It was hydrothermally reacted for 48 hours. Then, the treated product was separated into individual pieces and liquid by a centrifuge and dried at 40 ° C. (Sample C). As shown in Table 1 and Figure 1, this powder is pure white and has a high content of Al 2 O 3 and kaolinite, and it is a high-quality kaolinite that does not contain impurities such as free quartz, microcline, and mica. It was confirmed to be synthetic clay.
実施例 一般に市販されている含水珪酸石灰化合物の廃材(ゾノ
トライト)の粉末を用い、これに塩酸を加えてpH2付近
に調整し、さらに実施例場合と同様に、カオリナイト
組成比になるように塩化アルミニウムを加えてテフロン
製容器に入れ、オートクレーブ中で200℃で48時間水熱
反応させた。得られた粉末は実施例で得られたものと
非常に近似しており、不純物は全く含まれていない純白
のカオリナイト質合成粘土であった。Example A powder of a commercially available waste material (zonotolite) of hydrous silicate lime compound is used, and hydrochloric acid is added to the powder to adjust the pH to around 2. Further, as in the case of the example, chlorination is performed so that the kaolinite composition ratio is obtained. Aluminum was added and the mixture was placed in a Teflon container and hydrothermally reacted at 200 ° C. for 48 hours in an autoclave. The obtained powder was very similar to that obtained in the example, and was pure white kaolinite synthetic clay containing no impurities.
実施例 電気炉で550℃で3時間加熱して灰化した稲の籾殻灰(S
iO2 93%含有)を4g秤量し、これに2モルの塩化アル
ミニウム水溶液を15.2ml加えてpH2付近に調整した後、
水を加えて原料と水の比を1対4となしテフロン製容器
に入れ、オートクレーブ中で230℃96時間水熱処理し
た。こうして得られた処理物はカオリナイトを主成分と
する白色の微粉末であった。Example Rice husk ash (S) which was ashed by heating at 550 ° C. for 3 hours in an electric furnace
iO 2 93% content) was weighed in an amount of 4 g, and 15.2 ml of a 2 mol aqueous solution of aluminum chloride was added to adjust the pH to around 2.
Water was added and the ratio of raw material to water was not set to 1: 4. The mixture was placed in a Teflon container and hydrothermally treated at 230 ° C. for 96 hours in an autoclave. The treated product thus obtained was white fine powder containing kaolinite as a main component.
〔本発明の効果〕 以上実施例を挙げて説明したとおり、本発明によれば、
次のような効果が得られる。 [Effects of the Invention] As described above with reference to the embodiments, according to the present invention,
The following effects can be obtained.
(1)従来周知のカオリナイト質合成粘土の原料を使用す
る場合には、所定の品質の粘土にしようとすると、反応
に高温と長時間が必要であっただけでなく非晶質ないし
は低結晶質部分を精選して用いなければならないのに加
え、易反応性の高純度の試薬類を使用しなければならな
い等、原材料の選別範囲が極度に限定されていたのであ
るが、本発明においては、結晶度の高い難反応性の原材
料、不純物の多い低級な原材料など殆どの珪酸塩、アル
ミノ珪酸塩が利用できるほか、一般市販の含水珪酸石灰
化合物、さらにはその廃材までも使用できるのであり、
原材料の選別範囲は大きく広がり、また原料コストを極
度に低減化することができる。(1) When using a conventionally known raw material of kaolinite synthetic clay, when trying to obtain clay of a predetermined quality, not only high temperature and long time were required for the reaction, but also amorphous or low crystalline In addition to having to select and use the quality part carefully, it is necessary to use highly reactive reagents with high reactivity, and the selection range of raw materials was extremely limited, but in the present invention, It is possible to use most silicates and aluminosilicates such as raw materials with high crystallinity and difficult reactivity, low-grade raw materials with many impurities, and general commercially available hydrous silicate lime compounds, and even waste materials thereof.
The range of selection of raw materials is greatly expanded, and raw material costs can be extremely reduced.
(2)本発明方法にあっては、水熱処理条件が比較的低温
で、しかも短時間処理が可能であるため、従来に比して
飛躍的に生産性が向上し、かつ、生産コストも極度に低
減化される。(2) In the method of the present invention, the hydrothermal treatment conditions are relatively low, and the treatment can be performed for a short time. Therefore, the productivity is dramatically improved as compared with the conventional method, and the production cost is extremely high. Is reduced to.
本発明方法によって製造された原料は、石英、長石な
どの不純物が全く残留していないため、品質的に頗る良
質である。The raw material produced by the method of the present invention is of excellent quality because impurities such as quartz and feldspar do not remain at all.
本発明によれば、従来、稲作農業に副次的に産出して
処理に難渋していたイネの籾殻をカオリナイト質合成粘
土の原料として大量に有効利用することができ、資源の
有効利用に役立つと共に、生産コストの低減化をも齋ら
すなど、一石二鳥の効果が得られる。According to the present invention, it is possible to effectively use rice hulls, which have been difficult to process by secondary production in rice farming, as a raw material for kaolinite synthetic clay, and to effectively use resources. In addition to being useful, it also brings about the effects of two birds with one stone, such as reducing production costs.
このように本発明は、従来この種のカオリナイト質合成
粘土の原料の製造技術上の隘路されていた問題を悉く解
消することができるうえに、良質な原料供給に危惧を抱
く窯業界には新規材料源を提供できると共に、医薬品、
化粧品、食料品の原料として、さらには放射性物質処理
用材など、本発明によって製造される微粉体としての用
途は限り無く広がるのであり、その産業上の利用価値は
頗る大きいものと云えよう。Thus, the present invention, in addition to being able to solve the problems that have been bottlenecked in the manufacturing technology of the raw materials of this type of kaolinite synthetic clay in the past, in addition to the kiln industry which is concerned about the supply of high-quality raw materials. We can provide a new material source,
The use as a fine powder produced by the present invention such as a raw material for cosmetics and foods, a material for treating radioactive substances, and the like is infinitely widespread, and it can be said that its industrial utility value is extremely large.
第1図は出発原料としての低級陶石(試料A)と、それを
実施例のように水熱処理して得られた含水珪酸石灰化
合物(試料B)と、カオリナイト質合成粘土(試料C)と
の生成状態を比較説明するために同一条件で測定した粉
末X線回折図である。 K……カオリナイト、M……微斜長石、 Q……石英、S……絹雲母、 T……11Åトバモライト、P……消石灰。FIG. 1 shows low-grade porcelain stone as a starting material (Sample A), hydrous silicate lime compound (Sample B) obtained by hydrothermally treating it as in Example, and kaolinite synthetic clay (Sample C). FIG. 4 is a powder X-ray diffraction diagram measured under the same conditions for the purpose of comparing and explaining the production states of and. K: Kaolinite, M: Microcline feldspar, Q: Quartz, S: Sericite, T: 11Å Tobermorite, P: Slaked lime.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭53−106400(JP,A) 特開 昭52−6397(JP,A) 特開 昭60−191018(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-53-106400 (JP, A) JP-A-52-6397 (JP, A) JP-A-60-191018 (JP, A)
Claims (1)
ことによって易反応性の珪酸に変化させることを特徴と
するカオリナイト質合成粘土用原料の製造方法。1. A method for producing a raw material for kaolinite synthetic clay, which comprises converting a hydrous silicate lime compound into an easily reactive silicic acid by exposing it to an acidic atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63310540A JPH0621029B2 (en) | 1988-12-07 | 1988-12-07 | Method for producing raw material for kaolinite synthetic clay |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63310540A JPH0621029B2 (en) | 1988-12-07 | 1988-12-07 | Method for producing raw material for kaolinite synthetic clay |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02157116A JPH02157116A (en) | 1990-06-15 |
| JPH0621029B2 true JPH0621029B2 (en) | 1994-03-23 |
Family
ID=18006467
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63310540A Expired - Lifetime JPH0621029B2 (en) | 1988-12-07 | 1988-12-07 | Method for producing raw material for kaolinite synthetic clay |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0621029B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5623919B2 (en) * | 2011-01-13 | 2014-11-12 | 梅夫 祖父江 | Method for producing inorganic curable composition using method for purifying amorphous silica and method for producing inorganic cured body |
| JP6600908B2 (en) * | 2015-09-14 | 2019-11-06 | 国立大学法人 熊本大学 | Method for producing zeolite |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS526397A (en) * | 1975-07-01 | 1977-01-18 | Deii Sutanbuuku Deii Horuhe | Manufacturing process for silica or silicate |
| JPS53106400A (en) * | 1977-02-28 | 1978-09-16 | Matsushita Electric Works Ltd | Preparation of calcium silicate |
| JPS60191018A (en) * | 1984-03-09 | 1985-09-28 | Agency Of Ind Science & Technol | Molecular sieve type zeorite |
-
1988
- 1988-12-07 JP JP63310540A patent/JPH0621029B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02157116A (en) | 1990-06-15 |
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