CN1266019A - Process for synthesizing hydrophobic medium porous molecular sieve - Google Patents
Process for synthesizing hydrophobic medium porous molecular sieve Download PDFInfo
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- CN1266019A CN1266019A CN 99103705 CN99103705A CN1266019A CN 1266019 A CN1266019 A CN 1266019A CN 99103705 CN99103705 CN 99103705 CN 99103705 A CN99103705 A CN 99103705A CN 1266019 A CN1266019 A CN 1266019A
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Abstract
A method for synthsizing hydrophobic mesopore molecular sieve is characterized by that in the presence of long-chain organic template agent and by using different catalysts, alkyl organo-siloxane and metasilicic ethyl ester are synthesized through hydrolysis and condensation respectively under the condition of water system or alcohol-water cosolvent into the hydrophobic mesopore molecular sieve in one-step and at room temp.. Said invention is simple in operatiion, convenient for preparation, moderate in reaction condition, its mesopore range can be controlled and regulated, and the specific surface area of the obtained molecular sieve is 896-1500 sq.m/g, and its pore size is 1.4-3.0 nm.
Description
The invention belongs to a kind of preparation method of mesoporous molecular sieve, relate in particular to the method for mesopore molecular sieve in a kind of synthesizing hydrophobic.
The MCM-41 mesoporous molecular sieve has wide practical use at catalytic applications, isolation technique and bioengineering field etc. because of it has the dimension pore passage structure that hexagonal is symmetrical, uniform pore size distributes.In recent years, make it structurally-modified and surface-functionalized, paid close attention to by people always to satisfy the demand of each side by cutting to chemical constitution.On the one hand, introduce inorganic heteroatoms or make the metallocenes derivative and MCM-41 surface silanol group effect (forming the Si-O metal), the material that preparation has catalytic activity.(Naturc such as LMaschmeyer, 1995,378,159).On the other hand, by special mesopore material aftertreatment or directly introduce organic group and improve the textural property in duct and the hydrophobic environment of surface properties, enlarge its range of application.(Fudan Journal, 37 (3), 36,1998) such as researchist Xu Taiming carry out modification with trimethylchlorosilane and dimethyldichlorosilane(DMCS) to the silicon hydroxyl of MCM-41 surface hydrophilicity, form the Si-O-Si-(CH on surface
3)
3The surface methylates, and has increased wall thickness, has strengthened hydrophobicity.But silanization grafting Si-(CH
3) group, on the one hand, the synthetic sieve sample is when the high-temperature roasting removed template method in advance, and it is not too large that the surface hydroxyl reduced number will be led the amount that the aftertreatment organic group enters framework of molecular sieve, and surperficial aftertreatment needs excessive methyl chlorosilane.Methylated on the other hand mesopore material will cause the decline of original MCM-41 effective pore radius, specific surface area, makes the performance perameter size wayward.People (Studies in Surface Science ﹠amp such as foreign study personnel DanielBrunel; Catalysis.Vol 97:(1) 173-180), utilizes the MCM-41 mesopore material to be raw material, finishing is carried out in its duct, improve the physical and chemical performance in duct.Promptly utilize different organo-siloxanes under certain condition, with the effect of the synthetic MCM-41 of institute surface silanol group, organic group is grafted on the skeleton of mesoporous silicon, its process comprises: the first step, prepare new MCM-41 mesopore material, and then it is activated.Second step, feeding under the exsiccant nitrogen atmosphere, with the MCM-41 of corresponding organo-siloxane and the above-mentioned new system certain hour that in toluene solvant, refluxes altogether, distill out toluene subsequently, remaining mixture is heated to the refluxing toluene temperature, successively repetitive operation for several times, then through cooling, solid sample spends the night with ether, dichloromethane extraction through the Soxhlet withdrawal device, and last 200 ℃ vacuumized 6 hours.This shows, these preparation method's condition harshnesses, step is various, and process parameter should not be controlled, and is unfavorable for enlarging producing.
Goal of the invention of the present invention provides the method for mesopore molecular sieve in a kind of synthesizing hydrophobic simple to operate, easy to make.
The object of the present invention is achieved like this, in the presence of the long-chain organic formwork agent, uses different catalyzer, alkyl organic siloxane and positive silicon ethyl ester respectively under aqueous systems or pure water cosolvent condition hydrolytic condensation room temperature one-step synthesis hydrophobic in mesopore molecular sieve.
Its synthetic method is as follows:
(1) be the mineral alkali pH of being mixed with soluble in water the basic solution of 12-13;
(2) tetraethoxy (TEOS) is connect certain proportion with alkyl organic siloxane and mix, and under agitation be dissolved in by a certain percentage in the alkaline solution of above-mentioned new preparation, continue stirring and got solution (I) in 30-45 minute;
(3) solution that is mixed with 5-14% (weight percent) in the molten sub-water of cetyl trimethylammonium bromide (CTAB) is got solution (II);
(4) under agitation solution (II) is added in the solution (I) by a certain percentage, continued stirring reaction 5-10 minute;
(5) further add a certain amount of water (surplus water of Total Water), under the room temperature ageing 3-7 days;
(6) then after filtration washing,, drying;
(7) roasting or remove cetyl trimethylammonium bromide (CTAB) organic formwork agent under vacuum through the solvent extraction method; Wherein the mol ratio of each component is:
Tetraethoxy: alkyl organic siloxane: cetyl trimethylammonium bromide: mineral alkali: water=1: (0.11-1.5): (0.13-1.25): (0.33-0.38): (220-550).
Aforesaid alkyl organic siloxane is Union carbide A-162 (MTES), dimethyldiethoxysilane (DDS), phenyl triethoxysilane (PHTES), fluorine-based triethoxyl silane (FTES).
Aforesaid mineral alkali is NaOH, KOH.
The present invention can regulate the hydrophobicity of gained molecular sieve by the addition of control alkyl organic siloxane, in preparation process, also can pass through modulation solution ratio or processing parameter simultaneously, to the aperture of molecular sieve in carry out appropriate regulation in the mesoporous scope.
The present invention compared with prior art has following advantage:
1. simple to operate, easy to make, reaction conditions is gentle.
By regulate material proportion or processing parameter to the aperture of molecular sieve in carry out appropriate regulation in the mesoporous scope.
3. the specific surface area of the molecular sieve of gained is 896-1500m
2/ g, the aperture is 1.4-3.0nm.
Embodiment 1
3.1ml TEOS and 0.3ml MTES are mixed, and the 30ml pH that joins new preparation is in the NaOH aqueous solution of 12-13, and stirring reaction 30 minutes forms solution I; 2.769g CTAB is dissolved in 20mlH
2Among the O, form solution II; Under agitation solution II is added in the solution I then, continue reaction after 10 minutes, further add the water of 10ml; Room temperature ageing seven days after filtration, fully washing, drying, reflux with the alcoholic acid acidic solution at last and remove the CTAB template, obtain hydrophobic mesoporous molecular sieve after the drying.
Embodiment 2
3.1ml TEOS and 0.3ml DDS (10%) being mixed and under agitation add 30ml pH is that stirring reaction 35 minutes forms solution I in 12.5 the NaOH aqueous solution; 2.4570g CTAB is dissolved in the 20ml ethanol, forms solution II; Under agitation solution II is added in the solution I, continue the reaction certain hour after, further add the ethanol of 10ml, room temperature reaction 5 days after filtration, fully washing, drying, vacuumize at 300 ℃ at last and remove the CTAB template, obtain hydrophobic middle mesopore molecular sieve.
Embodiment 3
1.36ml TEOS and 1.82ml MTES are mixed, and the 30ml pH that joins new preparation is in the NaOH aqueous solution of 12-13, and stirring reaction 45 minutes forms solution I; 0.9965gCTAB is dissolved in 20ml H
2Among the O, form solution II; Under agitation solution II is added in the solution I then, continue reaction after 45 minutes, further add remainder water, room temperature ageing three days after filtration, fully washing, drying, reflux with the alcoholic acid acidic solution at last and remove the OTAB template, obtain hydrophobic middle mesopore molecular sieve after the drying.
Embodiment 4
Adopt the preparation process of the foregoing description 1, under the same conditions, the amount of TEOS and DDS can be 1.21ml and 1.08ml.
Embodiment 5
Adopt the preparation process of the foregoing description 1,0.6647g CTAB is dissolved in the 36ml water, wherein DDS can be FTES, and its addition is 0.62ml.
Embodiment 6
Adopt the preparation process of the foregoing description 2, under the same conditions, MTES can be the diethylamino phenyl TMOS, and its addition is 0.37ml.
Embodiment 7
Adopt the preparation process of the foregoing description 3, under the same conditions, the amount of OTAB can be 0.9556g, and the amount of TEOS and MTES can be 2.72ml and 0.91ml.
Claims (3)
1. the method for mesopore molecular sieve in the synthesizing hydrophobic, its synthetic method is as follows:
(1) be the mineral alkali pH of being mixed with soluble in water the basic solution of 12-13;
(2) tetraethoxy and alkyl organic siloxane are connect certain proportion and mix, and under agitation be dissolved in the alkaline solution of above-mentioned new preparation, continue stirring and got solution (I) in 30-45 minute;
(3) solution with the cetyl trimethylammonium bromide 5-14% of being mixed with soluble in water (weight percent) gets solution (II);
(4) under agitation solution (II) is added in the solution (I), continued stirring reaction 5-10 minute;
(5) further add a certain amount of water (surplus water of Total Water), under the room temperature ageing 3-7 days;
(6) then after filtration washing,, drying;
(7) roasting or remove the cetyl trimethylammonium bromide organic formwork agent under vacuum through the solvent extraction method; Wherein the mol ratio of each component is:
Tetraethoxy: alkyl organic siloxane: cetyl trimethylammonium bromide: mineral alkali: water=1: 10.11-1.5): (0.13-1.25): (0.33-0.38): (220-550).
2. the method for mesopore molecular sieve in a kind of synthesizing hydrophobic according to claim 1 is characterized in that described alkyl organic siloxane is Union carbide A-162, dimethyldiethoxysilane, phenyl triethoxysilane, fluorine-based triethoxyl silane.
3. the method for mesopore molecular sieve in a kind of synthesizing hydrophobic according to claim 1 is characterized in that described mineral alkali is NaOH, KOH.
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| CN99103705A CN1092143C (en) | 1999-03-03 | 1999-03-03 | Process for synthesizing hydrophobic medium porous molecular sieve |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1113811C (en) * | 2001-08-14 | 2003-07-09 | 复旦大学 | Preparation method of mesonic pore molecular sieve carrier material |
| WO2008019570A1 (en) * | 2006-08-11 | 2008-02-21 | China Petroleum & Chemical Corporation | A porous zeolite of organosilicon, a method for preparing the same and the use of the same |
| CN101239726B (en) * | 2007-02-07 | 2010-05-19 | 中国石油化工股份有限公司 | Organic silicon micro-pore zeolite and its synthetic method and application |
| CN102050464B (en) * | 2009-10-30 | 2012-07-25 | 中国石油化工股份有限公司 | Synthesizing method of silicon molecular sieve |
| CN101124160B (en) * | 2004-11-26 | 2012-12-12 | 道达尔炼油与销售部 | Zeolite material and preparation and use thereof |
| CN108264057A (en) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | Method for solid-phase synthesis of wettability-controllable ZSM-5 zeolite |
| CN109590010A (en) * | 2018-11-22 | 2019-04-09 | 东北石油大学 | For adjusting the mesoporous hydrophobic surface modification method of core-shell catalyst shell |
| CN109626392A (en) * | 2019-02-02 | 2019-04-16 | 北京工业大学 | A kind of preparation method of nanometer of clinoptilolite molecular sieve |
| CN110184120A (en) * | 2019-05-20 | 2019-08-30 | 李科成 | A kind of preparation method of edible oil depickling processing particle |
| CN113134383A (en) * | 2021-01-08 | 2021-07-20 | 北京科技大学 | Preparation method of metal oxide catalyst |
| CN113304786A (en) * | 2020-02-27 | 2021-08-27 | 中国石油化工股份有限公司 | Catalytic cracking auxiliary agent containing dichlorodimethylsilane modified all-silicon mesoporous material and preparation method and application thereof |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5300277A (en) * | 1990-01-25 | 1994-04-05 | Mobil Oil Corporation | Synthesis of mesoporous crystalline material |
| US5246689A (en) * | 1990-01-25 | 1993-09-21 | Mobil Oil Corporation | Synthetic porous crystalline material its synthesis and use |
| CN1062836C (en) * | 1997-09-18 | 2001-03-07 | 复旦大学 | Method for preparing MCM-48 mesonore molecular sieve using anionic-cationic surfactant as template agent |
-
1999
- 1999-03-03 CN CN99103705A patent/CN1092143C/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1113811C (en) * | 2001-08-14 | 2003-07-09 | 复旦大学 | Preparation method of mesonic pore molecular sieve carrier material |
| CN101124160B (en) * | 2004-11-26 | 2012-12-12 | 道达尔炼油与销售部 | Zeolite material and preparation and use thereof |
| WO2008019570A1 (en) * | 2006-08-11 | 2008-02-21 | China Petroleum & Chemical Corporation | A porous zeolite of organosilicon, a method for preparing the same and the use of the same |
| US8030508B2 (en) | 2006-08-11 | 2011-10-04 | China Petroleum & Chemical Corporation | Porous zeolite of organosilicon, a method for preparing the same and the use of the same |
| CN101239726B (en) * | 2007-02-07 | 2010-05-19 | 中国石油化工股份有限公司 | Organic silicon micro-pore zeolite and its synthetic method and application |
| CN102050464B (en) * | 2009-10-30 | 2012-07-25 | 中国石油化工股份有限公司 | Synthesizing method of silicon molecular sieve |
| CN108264057A (en) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | Method for solid-phase synthesis of wettability-controllable ZSM-5 zeolite |
| CN109590010A (en) * | 2018-11-22 | 2019-04-09 | 东北石油大学 | For adjusting the mesoporous hydrophobic surface modification method of core-shell catalyst shell |
| CN109590010B (en) * | 2018-11-22 | 2021-06-18 | 东北石油大学 | Surface modification method for adjusting shell hydrophobicity of mesoporous core-shell catalyst |
| CN109626392A (en) * | 2019-02-02 | 2019-04-16 | 北京工业大学 | A kind of preparation method of nanometer of clinoptilolite molecular sieve |
| CN109626392B (en) * | 2019-02-02 | 2022-06-07 | 北京工业大学 | Preparation method of nano clinoptilolite molecular sieve |
| CN110184120A (en) * | 2019-05-20 | 2019-08-30 | 李科成 | A kind of preparation method of edible oil depickling processing particle |
| CN113304786A (en) * | 2020-02-27 | 2021-08-27 | 中国石油化工股份有限公司 | Catalytic cracking auxiliary agent containing dichlorodimethylsilane modified all-silicon mesoporous material and preparation method and application thereof |
| CN113304786B (en) * | 2020-02-27 | 2023-05-30 | 中国石油化工股份有限公司 | Catalytic cracking auxiliary agent containing dichloro dimethyl silane modified all-silicon mesoporous material and preparation method and application thereof |
| CN113134383A (en) * | 2021-01-08 | 2021-07-20 | 北京科技大学 | Preparation method of metal oxide catalyst |
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| CN1092143C (en) | 2002-10-09 |
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