CN1312038C - Large aperture capacity silicon oxide vesicle, foamed material and process for preparing the same - Google Patents

Large aperture capacity silicon oxide vesicle, foamed material and process for preparing the same Download PDF

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Publication number
CN1312038C
CN1312038C CNB2005100268374A CN200510026837A CN1312038C CN 1312038 C CN1312038 C CN 1312038C CN B2005100268374 A CNB2005100268374 A CN B2005100268374A CN 200510026837 A CN200510026837 A CN 200510026837A CN 1312038 C CN1312038 C CN 1312038C
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active agent
silicon oxide
buffered soln
tensio
pore volume
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CN1730392A (en
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余承忠
王红宁
王韵华
赵东元
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Fudan University
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Fudan University
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Abstract

The present invention belongs to the technical field of mesoporous molecular sieve material, particularly to a novel nanometer porous material with large pore volume (as large as 3cm<3>/g), controllable patterns (vesicles, foam, etc.) and adjustable pore size (10 to 200 nm), which is synthesized under mild condition in the method of sol-gel. The preparation method comprises the steps of the preparation of the vesicles and the foam, hydrothermal reaction, drying, the removal of a template agent, etc. The invention has the advantages that the reaction condition is mild, the operation is simple, cosurfactant and cosolvent do not need to be added, and the final material has low cost and is easy to obtain. By changing conditions, such as the ratio of raw materials, the reaction temperature, the pH value of solution and the ion concentration of buffer solution, etc., the physicochemical properties of the porous material, such as the pattern, the pore size and the pore volume, etc., can be changed. The nanometer porous material with large pore volume has wide application foreground in the fields of adsorption, catalyst carriers, drug delivery, separation, chromatography, paint, microreactors, etc.

Description

Large aperture capacity silicon oxide vesicle or foam materials and preparation method thereof
Technical field
The invention belongs to the meso-porous molecular sieve material technical field, be specifically related to a kind of vesica or foam and synthetic method thereof of large aperture capacity silicon oxide.
Background technology
Novel mesopore molecular sieve MCM-41 from 1992 by U.S. Mobil oil company synthetic first since, caused the very big concern of zeolite and catalysis circle, but its pore volume, aperture are less relatively.Stucky[Patrick Schmidt-Winkel, Galen D.Stucky *, et al.Chem.Mater.2000,12,686-696] and the mesoporous vesica (MCF) for preparing of co-workers, have than large pore volume and aperture, make organic expander but must add trimethylbenzene (TMB), TMB has destroyed the order of material when enlarging the material pore volume.In addition, TMB is toxic, and is unfriendly to environment; Volatile, be unsuitable for industrial mass production.Eisenberg[Kui Yu, Adi Eisenberg *, Macromolecules, 1996,29,6359-6361] and co-workers by changing the composition of high-molecular block copolymer, the concentration of segmented copolymer, use different solvents, change the composition of solvent, add additive (salt, acid, alkali, homopolymer), change the temperature of synthetic system, pH value of solution value etc. obtains organic vesica.Pinnavaia[S.S.Kim; T.J.Pinnavaia, Science 1998,282,1302-1305] and co-workers utilize the gemini tensio-active agent to obtain the vesica of the silicon-dioxide of pore size distribution broad (20-1400nm), but its pore volume<1cm 3/ g, and to add organic solvent.Chen Yongming [Jianzhong Du and Yongming Chen, Macromolecules 2004,37,5710-5716] etc. utilize the material of the organic and inorganic compounding of the hydrophilic and hydrophobic segment of special synthetic different lengths, the content that changes water is realized by ball and bar-shaped, arrives stratiform, rod and vesica (on a small quantity), to vesica and stratiform, the transformation of arriving vesica again, its raw material (making silicon source and template simultaneously) is so expensive can't the preparation in a large number.The present invention adopts P123 (EO 20PO 70EO 20) (EO oxyethylene; The PO propylene oxide) etc. as template, silicon oxide vesicle, the foam of preparation large pore volume under the low temperature in buffered soln, its aperture is at 10-200nm, and pore volume is at 1.0-3.0cm 3In/g the scope, adjustable.
Summary of the invention
The purpose of this invention is to provide a kind of silicon oxide vesicle of large pore volume or foam and preparation method thereof.
The vesica or the foam of the large aperture capacity silicon oxide that the present invention proposes are a kind of employing sol-gel method synthetic under mild conditions, have large pore volume, controllable appearance (vesica, foam etc.), and the adjustable novel nano porous material in aperture.The mol ratio in tensio-active agent that it is used and silicon source is 0.01~0.05: 1, and the aperture is at 10-200nm, and pore volume is at 1.0-3.0cm 3In/g the scope, adjustable.
Large aperture capacity silicon oxide vesicle of the present invention or foamy preparation method are as follows:
(1) vesica, foamy preparation
Certain amount of surfactant is dissolved in the buffered soln, under agitation add the silicon source by a certain percentage: methyl silicate (TMOS) or tetraethoxy (TEOS), continue to stir 3-10 minute, and left standstill or continued to stir 20-48 hour, its each mol ratio of forming is:
Tensio-active agent: silicon source=0.01~0.05: 1 buffered soln: silicon source=100~350: 1;
Temperature of reaction system is 15-70 ℃.
(2) hydro-thermal, the mother liquor that step (1) is made under 80-130 ℃ of temperature hydro-thermal 20-36 hour.
(3) drying, with the product suction filtration after step (2) hydro-thermal, washing, flush away inorganic salt, drying at room temperature.
(4) removal of tensio-active agent at 400-900 ℃ of following roasting 4-8 hour, is removed tensio-active agent with dried product, makes product of the present invention.
Aforesaid tensio-active agent is poly-oxyethylene (PEO) as hydrophilic block, the long chain alkane nonionic surface active agent as hydrophobic group, and carbon atom number is 8-20, and the polymerization degree of oxyethylene is 4-100; Perhaps poly-oxyethylene (PEO) is as hydrophilic block, poly-propylene oxide (PPO) or poly-epoxy butylene (PBO) the block macromolecular tensio-active agent as hydrophobic block, and its molecular formula is EO nPO mEO n, n=10-140, m=5-100, or EO nBO mEO n, n=10-200, m=10-100, or EO nBO m, n=10-100, m=5-60.
Aforesaid buffered soln is the NaAc-HAc of pH value between 3-8, or NaOH-NaH 2PO 4Buffered soln uses inorganic salt to regulate and control the total ion concentration of buffered soln, and ionic concn is between 0.05-1.00M.
The present invention compared with prior art has following advantage:
(1) raw material is cheap and easy to get, and the reaction conditions gentleness is easy to operation.
(2) by change raw material ratio, temperature of reaction, pH value of solution value and and condition such as buffered soln total ion concentration can the modulation vesica, physicochemical property such as foamy pattern, aperture and pore volume.
(3) silicon oxide vesicle of gained, foam have bigger pore volume, illustrate as accompanying drawing, and prove to have good adsorption, sustained release performance by experiment.Material of the present invention is with a wide range of applications in fields such as absorption, support of the catalyst, medicament slow release, separation, chromatogram, pigment, microreactors.
Description of drawings
Fig. 1 is the transmission electron microscope picture of silicon oxide vesicle.
Fig. 2 is silicon oxide vesicle nitrogen adsorption-desorption isotherm.
Fig. 3 is a silicon-dioxide foamy transmission electron microscope picture.
Fig. 4 is silicon-dioxide foam nitrogen adsorption-desorption isotherm.
Embodiment
Embodiment 1
1g P123 is added 30g pH=5, Ac -Total ion concentration is a 0.2mol/L NaAC-HAc buffered soln, stirs P123 is dissolved fully under 40 ℃ of temperature, adds 1.52g TMOS in system, continues to stir 5 minutes, left standstill 24 hours, in 100 ℃ of hydro-thermals 24 hours, suction filtration, washing, drying was 550 ℃ of roastings 5 hours.Obtain foam materials.Aperture 40nm, pore volume 2.50cm 3/ g.
Embodiment 2
1g P123 is added 30g pH=5, Ac -Total ion concentration is the NaAC-HAc buffered soln of 0.2mol/L, stirring under 50 ℃ of temperature dissolves P123 fully, in system, add 1.52g TMOS, continue to stir 5 minutes, left standstill 24 hours, in 100 ℃ of hydro-thermals 24 hours, suction filtration, washing, drying was 550 ℃ of roastings 5 hours. obtain foam materials.Aperture 50nm, pore volume 2.20cm 3/ g.
Embodiment 3
1g P123 is added 30g pH=5, Ac -Total ion concentration is the NaAC-HAc buffered soln of 0.2mol/L, stirs P123 is dissolved fully under 60 ℃ of temperature, adds 1.52g TMOS in system, continues to stir 5 minutes, left standstill 24 hours, in 100 ℃ of hydro-thermals 24 hours, suction filtration, washing, drying was 550 ℃ of roastings 5 hours.Obtain foam materials.Aperture 40nm, pore volume 2.10cm 3/ g.
Embodiment 4
1g P123 is added 30g pH=6, Na +Total ion concentration is the NaOH-NaH of 0.2mol/L 2PO 4Buffered soln stirs under 40 ℃ of temperature P123 is dissolved fully, adds 1.52g TMOS in system, continues to stir 5 minutes, left standstill 24 hours, and in 100 ℃ of hydro-thermals 24 hours, suction filtration, washing, drying was 550 ℃ of roastings 5 hours.Obtain foam materials.Aperture 30nm, pore volume 2.80cm 3/ g.
Embodiment 5
1g P123 is added 30g pH=5, Ac -Total ion concentration is the NaAC-HAc buffered soln of 0.05mol/L, stirs P123 is dissolved fully under 40 ℃ of temperature, adds 1.52g TMOS in system, continues to stir 5 minutes, left standstill 24 hours, in 100 ℃ of hydro-thermals 24 hours, suction filtration, washing, drying is at 550 ℃ of roasting 5h.Be and obtain the vesica material.Aperture 20-130nm, pore volume 1.82cm 3/ g.
Embodiment 6
1g P123 is added 30g pH=5, Ac -Total ion concentration is the NaAC-HAc buffered soln of 0.2mol/L, stirs P123 is dissolved fully under 40 ℃ of temperature, adds 2.08g TEOS in system, continues to stir 5 minutes, left standstill 24 hours, in 100 ℃ of hydro-thermals 24 hours, suction filtration, washing, drying was 550 ℃ of roastings 5 hours.Obtain foam materials.Aperture 100nm, pore volume 2.05cm 3/ g.

Claims (3)

1, the preparation method of a kind of large aperture capacity silicon oxide vesicle or foam materials is characterized in that concrete steps are as follows:
(1) vesica, foamy preparation
Surfactant dissolves is gone into buffered soln, under agitation add the silicon source: methyl silicate or tetraethoxy, continue to stir 3-10 minute, leave standstill or continued to stir 20-48 hour, the mol ratio of its each component is:
Tensio-active agent: silicon source=0.01~0.05: 1 buffered soln: silicon source=100~350: 1
The temperature of reaction of system is 15-70 ℃;
(2) hydro-thermal, the mother liquor that step (1) is made under 80-130 ℃ of temperature hydro-thermal 20-36 hour;
(3) drying, with the product suction filtration after step (2) hydro-thermal, washing, the flush away inorganic salt, dry under the room temperature;
(4) removal of tensio-active agent at 400-900 ℃ of following roasting 4-8 hour, is removed tensio-active agent with dried product, promptly gets required silicon oxide vesicle or foam, and its aperture is at 10-200nm, and pore volume is at 1.0-3.0cm 3/ g.
2, large aperture capacity silicon oxide vesicle as claimed in claim 1 or foamy preparation method, it is characterized in that described tensio-active agent for poly-oxyethylene as hydrophilic block, long chain alkane nonionic surface active agent as hydrophobic group, carbon atom number is 8-20, and the polymerization degree of poly-oxyethylene is 4-100; Perhaps poly-oxyethylene is as hydrophilic block, poly-propylene oxide or the poly-epoxy butylene block macromolecular tensio-active agent as hydrophobic block, and its molecular formula is EO nPO mEO n, n=10-140, m=5-100, or EO nBO mEO n, n=10-200, m=10-100, or EO nBO m, n=10-100, m=5-60.
3, large aperture capacity silicon oxide vesicle as claimed in claim 1 or foamy preparation method is characterized in that described buffered soln is NaAc-HAc or the NaOH-NaH of pH=3-8 2PO 4Buffered soln, and use inorganic salt to regulate and control the ionic concn of buffered soln, ionic concn is between 0.05-1.00M.
CNB2005100268374A 2005-06-16 2005-06-16 Large aperture capacity silicon oxide vesicle, foamed material and process for preparing the same Expired - Fee Related CN1312038C (en)

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CN101289189B (en) * 2008-04-03 2010-12-29 复旦大学 Earth silicon vesicle material with controllable shape, dimension and thickness of wall and method for preparing same
CN102718204A (en) * 2011-03-30 2012-10-10 苏州方昇光电装备技术有限公司 Preparation method for three-dimensional ordered macroporous porous carbon
CN102145897B (en) * 2011-04-19 2012-10-24 冷水江三A化工有限责任公司 Large-pore-volume silicon dioxide with nanoparticle structure and preparation method thereof
CN102502658A (en) * 2011-09-20 2012-06-20 重庆工商大学 Nanometer saccular material constituted by ordered mesoporous pore canals and preparation method thereof
CN102806071A (en) * 2012-06-29 2012-12-05 常州大学 Material for hollow nano organosilicon sphere and preparation method of material
CN103641121B (en) * 2013-11-05 2016-01-27 常州大学 A kind of nano-magnetic macroporous silica matrix material and preparation method thereof
US11033507B2 (en) 2013-12-19 2021-06-15 The University Of Queensland Method of synthesis of silica vesicles and use thereof
KR102592369B1 (en) * 2015-07-02 2023-10-25 사우디 아라비안 오일 컴퍼니 Preparation of propylene using mesoporous silica foam metathesis catalyst
CN110272052B (en) * 2018-03-14 2022-10-04 天津工业大学 Novel preparation method of nano silicon dioxide microcapsule
CN109354026A (en) * 2018-09-17 2019-02-19 佛山皖和新能源科技有限公司 A kind of preparation method of the uniform mesoporous silicon foam material in aperture

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KR20170007262A (en) * 2014-05-21 2017-01-18 필립모리스 프로덕츠 에스.에이. Aerosol-forming article comprising magnetic particles
KR102656343B1 (en) * 2014-05-21 2024-04-12 필립모리스 프로덕츠 에스.에이. Aerosol-forming article comprising magnetic particles

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