JP4814435B2 - Synthetic swellable fluorinated mica containing aluminum - Google Patents
Synthetic swellable fluorinated mica containing aluminum Download PDFInfo
- Publication number
- JP4814435B2 JP4814435B2 JP2001102959A JP2001102959A JP4814435B2 JP 4814435 B2 JP4814435 B2 JP 4814435B2 JP 2001102959 A JP2001102959 A JP 2001102959A JP 2001102959 A JP2001102959 A JP 2001102959A JP 4814435 B2 JP4814435 B2 JP 4814435B2
- Authority
- JP
- Japan
- Prior art keywords
- mica
- swellable
- synthetic
- production rate
- aluminum
- 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 - Fee Related
Links
- 229910052618 mica group Inorganic materials 0.000 title claims description 35
- 239000010445 mica Substances 0.000 title claims description 34
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title description 21
- 229910052782 aluminium Inorganic materials 0.000 title description 21
- 238000004519 manufacturing process Methods 0.000 claims description 29
- 239000002994 raw material Substances 0.000 claims description 21
- WSNJABVSHLCCOX-UHFFFAOYSA-J trilithium;trimagnesium;trisodium;dioxido(oxo)silane;tetrafluoride Chemical compound [Li+].[Li+].[Li+].[F-].[F-].[F-].[F-].[Na+].[Na+].[Na+].[Mg+2].[Mg+2].[Mg+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O WSNJABVSHLCCOX-UHFFFAOYSA-J 0.000 claims description 19
- 239000000126 substance Substances 0.000 claims description 17
- 238000002844 melting Methods 0.000 claims description 9
- 230000008018 melting Effects 0.000 claims description 9
- 239000011734 sodium Substances 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 claims description 6
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical compound [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 0.000 claims description 4
- 229910052708 sodium Inorganic materials 0.000 claims description 4
- ORUIBWPALBXDOA-UHFFFAOYSA-L magnesium fluoride Chemical compound [F-].[F-].[Mg+2] ORUIBWPALBXDOA-UHFFFAOYSA-L 0.000 claims description 3
- 229910001635 magnesium fluoride Inorganic materials 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 3
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 239000011775 sodium fluoride Substances 0.000 claims description 3
- 235000013024 sodium fluoride Nutrition 0.000 claims description 3
- 239000000454 talc Substances 0.000 claims description 3
- 229910052623 talc Inorganic materials 0.000 claims description 3
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 claims description 2
- 229910052808 lithium carbonate Inorganic materials 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 238000002156 mixing Methods 0.000 description 18
- 230000008961 swelling Effects 0.000 description 17
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 13
- 229910052744 lithium Inorganic materials 0.000 description 13
- 230000000052 comparative effect Effects 0.000 description 12
- 230000004927 fusion Effects 0.000 description 11
- 238000001308 synthesis method Methods 0.000 description 11
- 239000013078 crystal Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000010410 layer Substances 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 5
- RJDOZRNNYVAULJ-UHFFFAOYSA-L [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[F-].[F-].[Mg++].[Mg++].[Mg++].[Al+3].[Si+4].[Si+4].[Si+4].[K+] Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[F-].[F-].[Mg++].[Mg++].[Mg++].[Al+3].[Si+4].[Si+4].[Si+4].[K+] RJDOZRNNYVAULJ-UHFFFAOYSA-L 0.000 description 4
- 238000007500 overflow downdraw method Methods 0.000 description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000002562 thickening agent Substances 0.000 description 3
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 2
- WZFUQSJFWNHZHM-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)CC(=O)N1CC2=C(CC1)NN=N2 WZFUQSJFWNHZHM-UHFFFAOYSA-N 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 230000002522 swelling effect Effects 0.000 description 2
- HMUNWXXNJPVALC-UHFFFAOYSA-N 1-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C(CN1CC2=C(CC1)NN=N2)=O HMUNWXXNJPVALC-UHFFFAOYSA-N 0.000 description 1
- WWSJZGAPAVMETJ-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-3-ethoxypyrazol-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C=1C(=NN(C=1)CC(=O)N1CC2=C(CC1)NN=N2)OCC WWSJZGAPAVMETJ-UHFFFAOYSA-N 0.000 description 1
- ZRPAUEVGEGEPFQ-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]pyrazol-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C=1C=NN(C=1)CC(=O)N1CC2=C(CC1)NN=N2 ZRPAUEVGEGEPFQ-UHFFFAOYSA-N 0.000 description 1
- YJLUBHOZZTYQIP-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)NN=N2 YJLUBHOZZTYQIP-UHFFFAOYSA-N 0.000 description 1
- CONKBQPVFMXDOV-QHCPKHFHSA-N 6-[(5S)-5-[[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]methyl]-2-oxo-1,3-oxazolidin-3-yl]-3H-1,3-benzoxazol-2-one Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C[C@H]1CN(C(O1)=O)C1=CC2=C(NC(O2)=O)C=C1 CONKBQPVFMXDOV-QHCPKHFHSA-N 0.000 description 1
- 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 1
- CNLWCVNCHLKFHK-UHFFFAOYSA-N aluminum;lithium;dioxido(oxo)silane Chemical compound [Li+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O CNLWCVNCHLKFHK-UHFFFAOYSA-N 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 238000007796 conventional method 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
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 229910001947 lithium oxide Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 229910052611 pyroxene Inorganic materials 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910052642 spodumene Inorganic materials 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
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- Silicates, Zeolites, And Molecular Sieves (AREA)
- Lubricants (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、固体潤滑剤、増粘剤、フィラー材料等として使用される合成膨潤性フッ素雲母に係り、詳記すれば、結晶構造中にアルミニウム若しくはアルミニウムとリチウムとを含有する新規合成膨潤性フッ素雲母に関するものである。
【0002】
【従来の技術】
合成膨潤性フッ素雲母は、従来から固体潤滑剤、増粘剤、フィラー材料等として使用されている。この従来の合成膨潤性フッ素雲母は、層間にNaを持つ四珪素雲母であった。しかしながら、この層間にNaを持つ四珪素雲母は、合成時の回収物単位重量あたりの生成率が低く、その結果精製して不純物を取り除く必要があるという問題があった。そのため、作業工程が煩雑となる問題があった。
【0003】
このような欠点があるにもかかわらず、合成膨潤性雲母として、層間にNaを持つ四珪素雲母が使用されていたのは、その構造中の四面体位置にアルミニウムを含有させると膨潤能を失うと考えられていたためである。例えば下記先行技術文献には、アルミニウムとリチウムとを同時に配合するとスポデュメーン(リシア輝石)になり膨潤性雲母は形成されない旨記載されている。このような理由から、膨潤性フッ素雲母の合成においては、アルミニウムとリチウムとの配合はもとより、アルミニウムの配合についても検討されていなかった。そればかりか、製造時のアルミニウムの混入は極力避けるように工夫されており、坩堝、熔融炉の材料にはアルミニウムが含まれないものが用いられていた。
【0004】
膨潤性フッ素雲母の先行技術文献としては、著者;Haskiel R. Shell & Kenneth H. IveyのFluorine micas p.123-141、第16章 水膨潤性フッ素雲母及びフッ素モンモリロナイト、発行元;U.S.Dept. of the Interior,Bureau of Mines,発行年;1969年が挙げられる。
【0005】
【発明が解決しようとする課題】
この発明のうち請求項1記載の発明は、合成時の回収物単位重量あたりの生成率が向上し得る新規合成膨潤性フッ素雲母を提供することを目的とする。
【0006】
また、請求項2記載の発明は、上記請求項1記載の目的に加えて、従来よりも膨潤性が高められ得る新規合成膨潤性フッ素雲母を提供することを目的とする。
【0007】
更に、本発明は、不純物の量を減らし、用途によっては精製を不要とできる新規合成膨潤性フッ素雲母を提供することを目的とする。
【0008】
【課題を解決するための手段】
本発明者等は、上記目的を達成するため鋭意研究を重ねた結果、従来使用を避けていたアルミニウムをあえて構造中の四面体位置の珪素に置き換えて導入することによって、膨潤性を有し、しかも従来の四珪素雲母より生成率を著しく向上させ得ることを見出し、請求項1に記載の本発明に到達した。
【0009】
即ち、本発明のうち請求項1記載の発明は、合成雲母の結晶構造中に、アルミニウムを含有することを特徴とする。該アルミニウムは、合成雲母の結晶構造中の四面体位置にある珪素の一部を置き換える形で含有している。
【0010】
具体的には、溶融法で合成された、化学組成が
【化1】
(式中、Xの値は
【数1】
である)で表される合成膨潤性フッ素雲母である。
【0011】
アルミニウムに加えて、更にリチウムを含有させると、合成膨潤性フッ素雲母の生成率が高められるだけでなく、膨潤性もアルミニウムを含有しない従来の雲母よりも高められ得る合成膨潤性フッ素雲母が得られる。これは、従来の予測に全く反する結果である。
【0012】
即ち、請求項2記載の発明は、合成雲母の結晶構造中に、アルミニウムとリチウムとを含有することを特徴とする。該リチウムは、合成雲母の結晶構造中の層間のナトリウムの一部若しくは全部を置き換える形で含有している。
【0013】
具体的には、溶融法で合成された、化学組成が
【化2】
(式中、X'の値は0.5≧X’>0であり、Yの値は0.8≧Y>0である)で表される合成膨潤性フッ素雲母である。
【0014】
【発明の実施の形態】
本発明の合成膨潤性フッ素雲母は、好ましくは、前記[化1]又は[化2]になるように原料を調合し、これを加熱することによる溶融法によって製造することができる。
【0015】
即ち、上記[化1]で表される合成膨潤性フッ素雲母は、原料として二酸化珪素、酸化マグネシウム、フッ化マグネシウム、珪フッ化ナトリウム、フッ化ナトリウム、炭酸ナトリウム、及び天然鉱物であるタルク等と四面体位置に入るアルミニウムの素となる酸化アルミニウムを、目的とする膨潤性フッ素雲母の化学組成になるように調合し、熔融炉で加熱融解し、これを冷却することによって得られる。
【0016】
また、上記[化2]で表される合成膨潤性フッ素雲母は、上記原料に加えて、層間位置に入るリチウムの素となるフッ化リチウムもしくは炭酸リチウム等を添加して、同様に加熱融解、冷却することによって得られる。
【0017】
加熱融解温度は、1200℃〜1600℃好ましくは1400℃〜1500℃である。加熱融解した熔融体は、好ましくは0.01℃/分〜50℃/分、更に好ましくは1℃/分〜10℃/分の冷却速度で冷却し、結晶化させると良い。
【0018】
前記[化1]中の(AlXSi4-X)は、雲母の結晶構造における四面体位置の陽イオンのモル数を表し、好ましくは0.5≧X>0、特に好ましくは0.5≧X≧0.01の値をとるようにすると良い。Xの値が大きすぎると、雲母の膨潤性が低下する。このような組成は、前記したように、合成時に原料配合組成を調整することによって、自由に制御することができる。
【0019】
[化2]中の(AlX ´Si4-X ´)は、好ましくは1≧X´>0、特に好ましくは0.8≧X´≧0.1の値をとるようにすると良い。前記[化1]中のXよりも、値が大きくても差し支えなくなっているのは、Liを導入することによって、膨潤性が向上するためである。
【0020】
[化2]中、1≧X´であるのは、雲母の構造上八面体位置は三つしかなく、単位格子当りのMgは、最大で3であるので、3≧2.5+X´/2となり、1≧X´となるからである。
【0021】
[化2]中の(LiYNa1- Y) は、雲母の結晶構造における層間の陽イオンのモル比を表し、1≧Y>0好ましくは0.8≧Y≧0.1の値をとるようにすると良い。
【0022】
本発明で得られる合成膨潤性フッ素雲母は、膨潤性を保持し、しかも従来の四珪素雲母より高い生成率を示す。
【0023】
また、アルミニウムに加えて更にリチウムを含有させると、アルミニウムとリチウムとの相乗効果により、アルミニウムのみを有する合成膨潤性フッ素雲母に比べて、高い膨潤性が得られると共に、生成率も更に向上する。
【0024】
本発明の合成膨潤性フッ素雲母は、従来の四珪素雲母と同様に固体潤滑剤、増粘剤、フィラー材料等の通常の用途に用いることができる。本発明の合成膨潤性フッ素雲母は、新規物質であり、従来に無い優れた性質の膨潤性雲母も含まれているので、従来にない色々な用途への応用も期待される。
【0025】
【実施例】
次に、実施例、比較例を挙げて本発明を更に説明するが、本発明は、これら実施例に限定されない。例中、生成率は陽イオン交換容量(CEC)の値により測定し、膨潤力については、日本ベントナイト工業会により規定された標準法に基づいて評価した。
【0026】
実施例1
後記表1に示す配合割合で原材料を1kg調合し、熔融合成法によって、膨潤性合成フッ素雲母を合成した。得られた回収物を全量粉砕した試料について、生成率(CEC)を測定した。結果を後記表2に示す。
【0027】
実施例2
後記表1に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例1と同様にして生成率(CEC)を測定した。結果を後記表2に示す。
【0028】
実施例3
後記表1に示す通り、実施例1と同じ配合割合で原材料を500kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例1と同様にして生成率(CEC)を測定した。結果を後記表2に示す。
【0029】
実施例4
後記表1に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例1と同様にして生成率(CEC)を測定した。結果を後記表2に示す。
【0030】
比較例1
後記表1に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例1と同様にして生成率(CEC)を測定した。結果を後記表2に示す。
【0031】
比較例2
後記表1に示す通り、比較例1と同じ配合割合で原材料を500kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例1と同様にして生成率(CEC)を測定した。結果を後記表2に示す。
【0032】
【表1】
【0033】
【表2】
上記表2から明らかなように、比較例1〜2と比べて実施例1〜4では、CECが著しく高い値を示している。これは本発明の回収物単位質量あたりの生成量が、従来の四珪素雲母の生成率よりも著しく多いことを示すものである。尚、膨潤性については、比較例よりも実施例では低下していたが、いずれも膨潤性雲母として十分産業上利用し得る膨潤性(膨潤力:10〜15(cc/2g))を示すことが実験により確認されている。
【0034】
実施例5
後記表3に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成した。得られた回収物を全量粉砕した試料について、生成率の測定と膨潤力評価を行った。結果を後記表4に示す。
【0035】
実施例6
後記表3に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0036】
実施例7
後記表3に示す通り、実施例6と同じ配合割合で原材料を500kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0037】
実施例8
後記表3に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0038】
実施例9
後記表3に示す通り、実施例4と同じ配合割合で原材料を500kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0039】
実施例10
後記表3に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成した。実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0040】
比較例3
後記表3に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0041】
比較例4
後記表3に示す配合割合で原材料を1kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0042】
比較例6
後記表3に示す通り、比較例3と同じ配合割合で原材料を500kg調合し、熔融合成法で膨潤性フッ素雲母を合成し、実施例5と同様にして生成率の測定と膨潤力評価を行った。結果を後記表3に示す。
【0043】
【表3】
【0044】
【表4】
【0045】
上記表4の結果から、アルミニウムに加えてリチウムを添加した実施例5〜10では、従来の四珪素雲母の比較例3〜5と比べて、CEC及び膨潤力のいずれも高い値になっている。このことから、アルミニウムに加えてリチウムを添加した本発明の膨潤性雲母は、回収物単位質量あたりの生成量が高くなるだけでなく、膨潤力も向上すること明らかである。
【0046】
また、実施例5〜10のリチウムの添加量、比較例4及び前記実施例1〜4との比較から、リチウムを添加することにより、膨潤性が向上するだけでなく、生成率も向上することがわかる。
【0047】
【発明の効果】
以上述べた如く、本発明のうち請求項1記載の発明によれば、従来の四珪素雲母と比べて、合成時の回収物単位重量あたりの生成率が著しく向上し得るので、不純物の量が著しく減少し、用途によっては精製を不要とすることができる。その結果、膨潤性雲母を工業的に著しく安価に供することができるという絶大な効果を示す。
【0048】
また、請求項2記載の発明によれば、上記請求項1に記載の効果に加えて、従来よりも膨潤性が高められ得ると共に更に生成率が向上し得る利点が得られる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a synthetic swellable fluorine mica used as a solid lubricant, a thickener, a filler material, and the like, and more specifically, a novel synthetic swellable fluorine containing aluminum or aluminum and lithium in a crystal structure. It is about mica.
[0002]
[Prior art]
Synthetic swellable fluorinated mica has been conventionally used as a solid lubricant, a thickener, a filler material, and the like. This conventional synthetic swellable fluorine mica was tetrasilicon mica having Na between layers. However, the tetrasilicon mica having Na between the layers has a problem that the production rate per unit weight of the recovered product at the time of synthesis is low, and as a result, it is necessary to purify and remove impurities. Therefore, there is a problem that the work process becomes complicated.
[0003]
Despite these drawbacks, tetrasilicon mica with Na between layers was used as a synthetic swelling mica, because when aluminum is contained in the tetrahedral position in the structure, the swelling ability is lost. It was because it was thought. For example, the following prior art documents describe that when aluminum and lithium are blended simultaneously, spodumene (lithia pyroxene) is formed and no swellable mica is formed. For these reasons, in the synthesis of swellable fluoromica, not only the blending of aluminum and lithium but also the blending of aluminum has not been studied. In addition, it has been devised to avoid mixing aluminum as much as possible, and the crucible and melting furnace materials that do not contain aluminum have been used.
[0004]
Prior art literature on swellable fluorinated mica includes the author; Haskiel R. Shell & Kenneth H. Ivey's Fluorine micas p.123-141, Chapter 16 Water-swellable fluorinated mica and fluor montmorillonite, publisher; USDept. Of the Interior, Bureau of Mines, publication year; 1969.
[0005]
[Problems to be solved by the invention]
The object of the present invention is to provide a novel synthetic swellable fluorinated mica capable of improving the production rate per unit weight of the recovered product during synthesis.
[0006]
The invention of claim 2, wherein, in addition to the purpose of the claim 1, and an object thereof is to provide a novel synthetic swellable fluorinated mica that may swellability increased than before.
[0007]
Furthermore, an object of the present invention is to provide a novel synthetic swellable fluoromica capable of reducing the amount of impurities and eliminating the need for purification depending on applications.
[0008]
[Means for Solving the Problems]
As a result of intensive research to achieve the above-mentioned object, the present inventors have swelled by introducing aluminum, which was conventionally avoided, by replacing it with silicon at the tetrahedral position in the structure, In addition, the inventors have found that the production rate can be remarkably improved compared to the conventional tetrasilicon mica, and have reached the present invention according to claim 1.
[0009]
That is, the invention according to claim 1 of the present invention is characterized in that aluminum is contained in the crystal structure of the synthetic mica. The aluminum is contained in a form that replaces a part of silicon at a tetrahedral position in the crystal structure of the synthetic mica .
[0010]
Specifically , the chemical composition synthesized by the melting method is:
(In the formula, the value of X is ## EQU1 ##
It is a synthetic swelling fluorine mica represented by .
[0011]
When lithium is further contained in addition to aluminum, not only the production rate of the synthetic swellable fluorine mica is increased, but also a synthetic swellable fluorine mica that can be enhanced in comparison with the conventional mica not containing aluminum is obtained. . This is a result completely contrary to the conventional prediction.
[0012]
That is, the invention described in claim 2 is characterized in that aluminum and lithium are contained in the crystal structure of the synthetic mica. The lithium is contained in the form of replacing part or all of sodium between layers in the crystal structure of the synthetic mica .
[0013]
Specifically, the chemical composition synthesized by the melting method is
( Wherein the value of X ′ is 0.5 ≧ X ′> 0 and the value of Y is 0.8 ≧ Y> 0 ).
[0014]
DETAILED DESCRIPTION OF THE INVENTION
The synthetic swellable fluorinated mica of the present invention can be preferably produced by a melting method in which raw materials are prepared so as to have the above [Chemical Formula 1] or [Chemical Formula 2] and heated.
[0015]
That is, the synthetic swellable fluorinated mica represented by the above [Chemical Formula 1] includes silicon dioxide, magnesium oxide, magnesium fluoride, sodium silicofluoride, sodium fluoride, sodium carbonate, and natural mineral talc as raw materials. It is obtained by preparing aluminum oxide, which is a base of aluminum entering the tetrahedron position, so as to have the chemical composition of the target swellable fluorine mica, heating and melting it in a melting furnace, and cooling it.
[0016]
Further, the synthetic swellable fluorine mica represented by the above [Chemical Formula 2], in addition to the above raw materials, is added with lithium fluoride or lithium carbonate that becomes a source of lithium entering the interlayer position, and is similarly heated and melted. Obtained by cooling.
[0017]
The heating and melting temperature is 1200 ° C to 1600 ° C, preferably 1400 ° C to 1500 ° C. The heat-melted melt is preferably cooled at a cooling rate of 0.01 ° C./min to 50 ° C./min, more preferably 1 ° C./min to 10 ° C./min, and crystallized.
[0018]
(Al X Si 4-X ) in [Chemical Formula 1] represents the number of moles of cations at the tetrahedral position in the crystal structure of mica, preferably 0.5 ≧ X> 0, particularly preferably 0.5. It is preferable to take a value of ≧ X ≧ 0.01. When the value of X is too large, the swellability of mica is lowered. As described above, such a composition can be freely controlled by adjusting the raw material composition during synthesis.
[0019]
(Al X ' Si 4-X ' ) in [Chemical Formula 2] preferably takes a value of 1 ≧ X ′> 0, particularly preferably 0.8 ≧ X ′ ≧ 0.1. The reason why the value can be larger than X in the above [Chemical Formula 1] is that the introduction of Li improves the swellability.
[0020]
In [Chemical Formula 2], 1 ≧ X ′ is because there are only three octahedral positions in the structure of mica, and the maximum number of Mg per unit cell is 3, 3 ≧ 2.5 + X ′ / 2. This is because 1 ≧ X ′.
[0021]
(Li Y Na 1- Y ) in [Chemical Formula 2] represents the molar ratio of cations between layers in the crystal structure of mica, and 1 ≧ Y> 0, preferably 0.8 ≧ Y ≧ 0.1. It is better to take it.
[0022]
The synthetic swellable fluorinated mica obtained in the present invention retains the swellability and exhibits a higher production rate than the conventional tetrasilicon mica.
[0023]
Further, when lithium is further contained in addition to aluminum, a high swellability is obtained and the production rate is further improved due to the synergistic effect of aluminum and lithium as compared with a synthetic swellable fluorine mica having only aluminum.
[0024]
The synthetic swellable fluorine mica of the present invention can be used for ordinary applications such as solid lubricants, thickeners, filler materials, etc., as in the case of conventional tetrasilicon mica. The synthetic swellable fluorine mica of the present invention is a novel substance and includes a swellable mica having an excellent property that has never been obtained.
[0025]
【Example】
EXAMPLES Next, although an Example and a comparative example are given and this invention is further demonstrated, this invention is not limited to these Examples. In the examples, the production rate was measured by the value of cation exchange capacity (CEC), and the swelling power was evaluated based on the standard method defined by the Japan Bentonite Industry Association.
[0026]
Example 1
1 kg of the raw material was blended at a blending ratio shown in Table 1 below, and a swellable synthetic fluorinated mica was synthesized by a fusion synthesis method. About the sample which grind | pulverized the whole collection | recovery obtained, the production rate (CEC) was measured. The results are shown in Table 2 below.
[0027]
Example 2
1 kg of the raw material was blended at a blending ratio shown in Table 1 below, and swellable fluorine mica was synthesized by a fusion synthesis method, and the production rate (CEC) was measured in the same manner as in Example 1. The results are shown in Table 2 below.
[0028]
Example 3
As shown in Table 1 below, 500 kg of the raw material was blended at the same blending ratio as in Example 1, and swellable fluoromica was synthesized by the fusion method, and the production rate (CEC) was measured in the same manner as in Example 1. The results are shown in Table 2 below.
[0029]
Example 4
1 kg of the raw material was blended at a blending ratio shown in Table 1 below, and swellable fluorine mica was synthesized by a fusion synthesis method, and the production rate (CEC) was measured in the same manner as in Example 1. The results are shown in Table 2 below.
[0030]
Comparative Example 1
1 kg of the raw material was blended at a blending ratio shown in Table 1 below, and swellable fluorine mica was synthesized by a fusion synthesis method, and the production rate (CEC) was measured in the same manner as in Example 1. The results are shown in Table 2 below.
[0031]
Comparative Example 2
As shown in Table 1 below, 500 kg of raw materials were blended at the same blending ratio as in Comparative Example 1, and swellable fluoromica was synthesized by the fusion method, and the production rate (CEC) was measured in the same manner as in Example 1. The results are shown in Table 2 below.
[0032]
[Table 1]
[0033]
[Table 2]
As is apparent from Table 2 above, Examples 1 to 4 show significantly higher CEC values than Comparative Examples 1 and 2. This indicates that the production amount per unit mass of the recovered material of the present invention is significantly higher than the production rate of the conventional tetrasilicon mica. In addition, although the swelling property was lower in the Examples than the Comparative Example, all exhibit swelling properties (swelling power: 10 to 15 (cc / 2g)) that can be used industrially as swelling mica. Has been confirmed by experiments.
[0034]
Example 5
1 kg of the raw material was blended at a blending ratio shown in Table 3 below, and swellable fluoromica was synthesized by a fusion synthesis method. About the sample which grind | pulverized the whole collection | recovery obtained, the production rate measurement and swelling power evaluation were performed. The results are shown in Table 4 below.
[0035]
Example 6
1 kg of the raw material was blended at a blending ratio shown in Table 3 below, and swellable fluorine mica was synthesized by the fusion synthesis method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. The results are shown in Table 3 below.
[0036]
Example 7
As shown in Table 3 below, 500 kg of the raw material was blended at the same blending ratio as in Example 6, and a swellable fluorinated mica was synthesized by the fusion method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. It was. The results are shown in Table 3 below.
[0037]
Example 8
1 kg of the raw material was blended at a blending ratio shown in Table 3 below, and swellable fluorine mica was synthesized by the fusion synthesis method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. The results are shown in Table 3 below.
[0038]
Example 9
As shown in Table 3 below, 500 kg of the raw material was blended at the same blending ratio as in Example 4, and swellable fluorine mica was synthesized by the fusion method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. It was. The results are shown in Table 3 below.
[0039]
Example 10
1 kg of the raw material was blended at a blending ratio shown in Table 3 below, and swellable fluoromica was synthesized by a fusion synthesis method. In the same manner as in Example 5, the production rate was measured and the swelling power was evaluated. The results are shown in Table 3 below.
[0040]
Comparative Example 3
1 kg of the raw material was blended at a blending ratio shown in Table 3 below, and swellable fluorine mica was synthesized by the fusion synthesis method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. The results are shown in Table 3 below.
[0041]
Comparative Example 4
1 kg of the raw material was blended at a blending ratio shown in Table 3 below, and swellable fluorine mica was synthesized by the fusion synthesis method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. The results are shown in Table 3 below.
[0042]
Comparative Example 6
As shown in Table 3 below, 500 kg of the raw material was blended at the same blending ratio as in Comparative Example 3, and the swellable fluoromica was synthesized by the fusion synthesis method, and the production rate was measured and the swelling power was evaluated in the same manner as in Example 5. It was. The results are shown in Table 3 below.
[0043]
[Table 3]
[0044]
[Table 4]
[0045]
From the result of the said Table 4, in Examples 5-10 which added lithium in addition to aluminum, both CEC and swelling power are high values compared with the comparative examples 3-5 of the conventional tetrasilicon mica. . From this, it is clear that the swellable mica of the present invention, in which lithium is added in addition to aluminum, not only increases the yield per unit mass of recovered material but also improves the swelling power.
[0046]
In addition, from the amount of lithium added in Examples 5 to 10, Comparative Example 4 and the comparison with Examples 1 to 4 above, addition of lithium not only improves the swellability but also improves the production rate. I understand.
[0047]
【Effect of the invention】
As described above, according to the invention described in claim 1 of the present invention, the production rate per unit weight of the recovered product at the time of synthesis can be remarkably improved as compared with the conventional tetrasilicon mica. It is significantly reduced and, depending on the application, no purification is required. As a result, it shows a great effect that the swellable mica can be industrially provided at a very low cost.
[0048]
Further, according to the invention described in claim 2 , in addition to the effect described in claim 1, there can be obtained an advantage that the swellability can be enhanced as compared with the conventional technique and the production rate can be further improved.
Claims (4)
NaMg2.5+X/2(AlXSi4−X)O10F2
[0.5≧X>0]
の化学組成になるように調合し、これを1200〜1600℃で融解後、冷却することを特徴とする請求項1記載の合成膨潤性フッ素雲母の製造方法。A raw material selected from silicon dioxide, magnesium oxide, magnesium fluoride, sodium silicofluoride, sodium fluoride, sodium carbonate, talc, and aluminum oxide is represented by the formula (1):
NaMg 2.5 + X / 2 (Al X Si 4-X ) O 10 F 2
[0.5 ≧ X> 0]
The method for producing a synthetic swellable fluorinated mica according to claim 1, wherein the composition is prepared so as to have a chemical composition of 1 mol.
(LiYNa1−Y)Mg2.5+X’/2(AlX’Si4−X’)O10F2
[0.8≧Y>0、0.5≧X'>0]
の化学組成になるように調合し、これを1200〜1600℃で融解後、冷却することを特徴とする請求項2記載の合成膨潤性フッ素雲母の製造方法。A raw material selected from silicon dioxide, magnesium oxide, magnesium fluoride, sodium silicofluoride, sodium fluoride, sodium carbonate, talc, aluminum oxide, lithium fluoride, and lithium carbonate is represented by the formula (2):
(Li Y Na 1-Y) Mg 2.5 + X '/ 2 (Al X' Si 4-X ') O 10 F 2
[ 0.8 ≧ Y> 0, 0.5 ≧ X ′> 0]
3. The method for producing a synthetic swellable fluorinated mica according to claim 2, wherein the composition is prepared so as to have a chemical composition of, melted at 1200 to 1600 ° C., and then cooled.
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