CN101190794A - Method for synthesizing mesoporous titanium-silicon molecular screen material - Google Patents
Method for synthesizing mesoporous titanium-silicon molecular screen material Download PDFInfo
- Publication number
- CN101190794A CN101190794A CNA2006101442156A CN200610144215A CN101190794A CN 101190794 A CN101190794 A CN 101190794A CN A2006101442156 A CNA2006101442156 A CN A2006101442156A CN 200610144215 A CN200610144215 A CN 200610144215A CN 101190794 A CN101190794 A CN 101190794A
- Authority
- CN
- China
- Prior art keywords
- titanium
- alkyl
- active agent
- source
- carbon atom
- 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.)
- Granted
Links
Images
Landscapes
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
The invention provides a synthesis method of mesoporous Ti-HMS material and is characterized in that silica resource, titanium resource, organic alkali compound and surfactant are evenly mixed together by ultrasonic blending technology and that the mixture is used for obtaining product through hydrothermal crystallization. The synthesis method of the invention simplifies the synthesis technique, has easy and convenient operation, easily controllable process, good repeatedly preparation capacity but no special equipment requirement, and is applicable to industrial production; meanwhile the mesoporous Ti-HMS material prepared by the method has good catalytic oxidation function and promotes better effect in particular on the reaction of macromolecule.
Description
Technical field
The invention relates to a kind of synthetic method of titanium-containing materials, furtherly about a kind of synthetic method of mesoporous titanium-silicon molecular screen material.
Background technology
HTS is the novel titaniferous hetero-atom molecular-sieve that last century, early eighties began to develop.The Ti-ZSM-5 that MFI type structure is arranged that has synthesized at present is TS-1, the TS-2 of MEL type structure, and have than the TS-48 of macroporous structure etc.Wherein the TS-1 molecular sieve is that the transition metal titanium is introduced formed a kind of new titanium-silicone molecular sieve with good selective paraffin oxidation catalytic performance in the framework of molecular sieve with ZSM-5 structure.TS-1 not only has the catalysed oxidn of titanium, but also has the shape effect selected and the advantages of excellent stability of ZSM-5 molecular sieve.But Ti-ZSM-5 has micropore (about 0.55 nanometer) structure, big organic molecule is difficult to spread therein and by catalyzed oxidation, make its good catalytic oxidation performance be difficult in more wide field especially biological and bring into play in medicine macromole field, and then impel people to research and develop more wide-aperture titanium-containing molecular sieve material.
The early 1990s in last century, scientist's reported first of the Mobil company of the U.S. mesopore molecular sieve and the synthetic method thereof of M41S series, this series material has homogeneous granules degree and regular meso-hole structure, attracted the very big concern of relevant academia, for having brought hope in aspects such as macromolecular catalysis, separation.Wherein representational is MCM-41, its meso-hole structure feature (Q.Huo etc., NATURE, 1994,368:317) be its X-ray diffraction spectrogram near 2 θ are 2.3 °, near 4.0 °, there is diffraction peak 4.6 ° of vicinity.But MCM-41 is the mesoporous SiO of pure silicon
2, must in its structure, introduce heteroatoms and just have catalytic activity.Corma (Corma etc., Chem.Commun., 1994,147-148) equal titanium to be incorporated in the structure of MCM-41 by synthesizing mean in 1994, success obtained titaniferous MCM-41, i.e. Ti-MCM-41 molecular sieve.
Because the homogeneous meso-hole structure of Ti-MCM-41 molecular sieve rule, people place high hopes at aspects such as macromole fine chemistry industry and medicine macromole are synthetic to it.But, this material is a non-crystalline state, hydrothermal stability and hydrophobic nature all are weaker than crystalline Ti-Si zeolite (TS-1), catalytic activity in the oxidizing reaction that with the aqueous hydrogen peroxide solution is oxygenant is lower, greatly limited its application (Microporous Materials, 1997,9:173 and Stud.Surf.Sci.Catal., 1995).
In order to overcome titaniferous micro porous molecular sieve TS-1 and titanium-containing meso-porous molecular sieve Ti-MCM-41 limitation separately, people try to explore synthetic titanium-containing meso-porous molecular sieve material with high catalytic activity.In recent years, the research of this respect has become one of hot research problem.CN1226187C has reported HTS matrix material and its preparation method with above-mentioned two kinds of structures, the matrix material that obtains has certain catalytic activity, but that the subject matter of its existence is the duct size is single (restriction of diffraction peak position is strict in the X-ray diffraction spectrogram), and in its preparation method preparation process comparatively numerous and diverse, environment and cost burden arranged.This shows that simple and feasible, environment amenable synthetic method with mesoporous titanium-silicon molecular screen material of high catalytic activity is worth further research and explores.
In recent years, ultrasonic technique is as a kind of physical means and instrument, and people are applied in it that chemistry and material synthesize.Under the ultrasonic wave radiation, produce the collapse moment of countless small cavity bubbles in the medium, can emit great energy and huge pressure, promptly in medium, produce a series of extreme conditions that approach, as the high temperature of moment, high pressure etc., these energy have played light, electricity, the by the use of thermal means effect of being beyond one's reach in material is synthetic.Ultransonic cavatition is seen uniform mixing with the synthetic technology that the stirring of machinery is merged mutually with desired Jie of the narrow distribution nano-powder of easier realization particle, eliminates the partial concn inequality.Ultrasonic technology is as a kind of novel synthetic technology; be subjected to people just day by day and pay close attention to, it has demonstrated great potential at chemistry and material aspect synthetic, as is applied in (the big woods of state etc. on the nano material preparation; " SCI " in August, 2002, the 1592-1594 page or leaf is used to prepare nano-TiO
2Ren Zhen etc., " chemical industry journal " in January, 2006, the 210-213 page or leaf is used to prepare nanometer SiO
2Deng).Upward (Wu Jianmei etc., " catalysis journal " in May, 2006, the 375-377 page or leaf was used for aging MCM-49 Si-Al molecular sieve to be applied in the molecular sieve preparation; Intercalation bright great waves etc., " Chinese Journal of Inorganic Chemistry " in February, 2004, the 219-224 page or leaf is used for synthetic pure silicon mesopore molecular sieve etc.).
Summary of the invention
Mesoporous titanium-silicon molecular screen material is different from other pure silicon molecular screen material or Si-Al molecular sieve material, and the titanium source easily generates TiO in the preparation process from reuniting
2, produce extra-framework titanium, therefore becoming the polymerization that prevents titanium in the glue process is that titanium-containing mesoporous material prepares key of success.
The objective of the invention is deficiency, a kind of synthetic method of mesoporous titanium-silicon molecular screen material is provided at the synthetic aspect of existing mesoporous titanium-silicon molecular screen material.This synthetic method makes the titanium of hydrolysis better combine with silicon and organic bases and tensio-active agent etc., eliminates the partial concn inequality, the TiO that makes the titanium source reunite and generate
2Few as far as possible, reduce the generation of extra-framework titanium, and make the titanium-containing mesoporous material of preparing have good catalyzed oxidation function, better to the reaction effect of macromole participation especially.
Therefore, the invention provides the synthetic method of mesoporous titanium-silicon molecular screen material, it is characterized in that silicon source, titanium source, organo-alkali compound and tensio-active agent are mixed, utilize the ultrasonic agitation technology to make it evenly, with the mixture that obtains through hydrothermal crystallizing and reclaim product.
In the synthetic method provided by the invention, preferred reinforced process is earlier the silicon source to be joined in the mixed aqueous solution of being made up of organo-alkali compound and tensio-active agent, utilize the ultrasonic agitation technology to make it mixing, again the titanium source is dripped in wherein, continue ultrasonic agitation and form uniform mixture, through hydrothermal crystallizing and reclaim product.
The mole of said mixture consists of the silicon source: titanium source: organic bases: tensio-active agent: water=1: (0.0005-0.5): (0.05-0.8): (0.01-0.5): (5-220), preferred mole consists of 1: (0.005-0.5): (0.05-0.5): (0.05-0.5): (20-180), wherein the silicon source is with SiO
2Meter, the titanium source is with TiO
2Meter.
The reaction conditions of said hydrothermal crystallizing be with mixture in sealed reactor under 20-190 ℃, preferred 80-180 ℃ and autogenous pressure hydrothermal crystallizing handled 2-360 hour, preferred 24-144 hour; Perhaps earlier 60-120 ℃ pre-crystallization 0.5-10 hour down, preferred 1-8 hour, and then, reclaim product more according to a conventional method 80-180 ℃ of following crystallization 1 hour to 5 days, preferred 1 hour-3 days.
The resulting titanium-containing mesoporous material of synthetic method provided by the invention, the feature that has similar mesoporous MCM-41 and part micropore Ti-ZSM-5 simultaneously, specifically in the X-ray diffraction spectrogram of this material near 2 θ are 2.3 °, near 4.0 °, there is diffraction peak 4.6 ° of vicinity, the X-ray diffraction of respectively corresponding [100], [110], [200] crystal face is the constitutional features of similar mesoporous MCM-41 molecular sieve; In its infrared spectra at wave number 550cm
-1Near and 960cm
-1There is absorption the vicinity, and wave number is at 550cm
-1Near absorption band illustrate its have the feature of ZSM-5 (J.C.Jans en etc., Zeolite, 1984,4:369), and wave number is at 960cm
-1Near absorption band then is the feature of skeleton titanium, illustrates that Ti has entered skeleton; Near wavelength is 220nm, stronger absorption band is arranged in its ultraviolet-visible spectrum, illustrate that also Ti has entered skeleton.This material has good catalyzed oxidation function, and is better to the reaction effect of macromole participation especially, illustrates that also Ti has entered skeleton and embodied the reaction properties that mesoporous catalysis macromole participates in.
In synthetic method provided by the invention, said ultrasonic agitation evenly is meant under ultrasonic wave and mechanical stirring condition raw material is mixed, promptly utilizes the synthetic technology that ultransonic cavatition and mechanical stirring merge mutually to make it mixing.
In the synthetic method provided by the present invention, said silicon source can be organosilicon source or inorganic silicon source, is preferably the organosilicon source; Said inorganic silicon source can be water glass or various forms of amorphous silica; The preferred organic silicon ester in said organosilicon source, general formula is R
1 4SiO
4Siloxanes, R wherein
1For having the alkyl of 1-4 carbon atom.
In the synthetic method provided by the present invention, said titanium source can be inorganic ti sources or organic titanium source, is preferably the organic titanium source; Said inorganic ti sources is meant TiX
4, TiX
3, TiOX
2Or Ti (SO
4)
2Etc. various forms of metatitanic acid, alkali or the salt of containing, wherein X represents halogen, preferred chlorine; It is Ti (OR that said organic titanium source is selected from general formula
2)
4Organic titanate, R wherein
2For having the alkyl of 1-4 carbon atom.
In synthetic method provided by the invention, said tensio-active agent is meant the tensio-active agent of ordinary meaning.Comprise anion surfactant, cats product and nonionogenic tenside.Wherein cats product CS is meant the cats product on the ordinary meaning, and preferred formula is (R
3R
4NR
5R
6)
+X
-Quaternary ammonium salt surface active agent, wherein X represents halogen, R
3, R
4And R
5Be the alkyl that is less than 3 carbon atoms, R
3, R
4And R
5Carbonatoms can be identical or different, R
6For having the alkyl that is no less than 12 carbon atoms, preferred 12-22 carbon atom, more preferably Tetradecyl Trimethyl Ammonium Bromide or cetyl trimethylammonium bromide.
In the synthetic method provided by the present invention, said organo-alkali compound is selected from fat amine compound, alcamine compound or quaternary amine alkali compounds, or mixes the mixed amine compounds of forming mutually by them.Organic amine the more important thing is the effect of similar molecular sieve structure template except doing alkali source.
Wherein said its general formula of fat amine compound is R
7(NH
2)
n, R wherein
3Be alkyl or alkylidene group with 1-4 carbon atom, n=1 or 2, wherein preferred fat amine compound is ethamine, n-Butyl Amine 99, butanediamine or hexanediamine.
Wherein said its general formula of alcamine compound is (HOR
8)
mH
(3-m)R wherein
4For having the alkylidene group of 1-4 carbon atom; M=1-3; Wherein preferred alcamine compound is monoethanolamine, diethanolamine or trolamine.
Wherein said its general formula of quaternary ammonium hydroxide compounds is (R
3)
4NOH, wherein R
3For having the alkyl of 1-4 carbon atom, preferably propyl group.
In synthetic method provided by the invention, said hydrothermal crystallizing treating processes can be carried out under static state, also can carry out under dynamically.
In synthetic method provided by the invention, the process of said recovery product is meant the drying and the roasting process of crystallization product.Wherein said drying process can be carried out under the temperature between the room temperature to 200 ℃, said roasting can be between 300 to 800 ℃ be carried out in air atmosphere after 0.5-6 hour in nitrogen atmosphere earlier in 3-12 hour, can also remove organic substance in the material duct by means such as organic solvent extractions before the roasting.
Synthetic method provided by the invention has following advantage:
1, utilize the ultrasonic agitation technology to eliminate partial concn inequality in the building-up process, the TiO that makes the titanium source reunite and generate
2Few as far as possible, reduce the generation of extra-framework titanium.
2, since ultrasonic agitation impel silicon source and titanium source with organic bases, tensio-active agent is better combines, and makes organic bases, tensio-active agent better play the effect of template and structure directing, has reduced template agent, has reduced synthetic cost.
3, its catalytic oxidation activity of product and the selectivity of utilizing the ultrasonic agitation technology to synthesize compared with prior art obviously improves, and has stability of catalytic activity preferably simultaneously.
4, the ultrasonic agitation technology is simple and easy to operate, and it is good to repeat preparation property, and the sample homogeneity is good.
5, utilize organic bases as alkali source, can provide alkaline environment for system on the one hand, can play the effect of similar micro porous molecular sieve stay in place form agent on the other hand, make the synthetic mesoporous titanium-silicon molecular screen material have the part pore characteristics, be presented as that promptly prepared material has catalytic activity and activity stability preferably.
6, in the building-up process without other raw materials such as hydrochloric acid, Virahols, reduce cost and environmental pressure.
Description of drawings
Fig. 1 is the X-ray diffraction spectrogram of synthetic mesoporous titanium-silicon molecular screen material among the embodiment 1.
Fig. 2 is the infrared absorption spectrum spectrogram of synthetic mesoporous titanium-silicon molecular screen material among the embodiment 1.
Fig. 3 is the uv-visible absorption spectra spectrogram of synthetic mesoporous titanium-silicon molecular screen material among the embodiment 1.
Embodiment
Following embodiment will be further described the present invention, but therefore not limit the present invention.
The reagent that all are used among the embodiment is commercially available chemically pure reagent, and used ultrasonic wave is KQ-100DE type numerical control supersonic cleanser (220 volts of operating voltage, 50 hertz that Kunshan Ultrasonic Instruments Co., Ltd. produces; 40 kilo hertzs of operating frequencies; 100 watts of ultrasonic electric power).The fourier infrared of sample (FT-IR) spectrogram is measured on Nicolet 8210 type Fourier infrared spectrographs, adopts KBr compressing tablet (sample accounts for 1wt%), test specification 400-1500cm under the vacuum
-1X-ray diffraction (XRD) the crystalline phase figure that carries out sample on Siemens D5005 type x-ray diffractometer measures, and gamma ray source is CuK α (λ=1.5418
), tube voltage 40kV, tube current 40mA, 0.25 °/min of sweep velocity, sweep limit 2 θ=1 °-10 °.Sample solid ultraviolet-visible diffuse reflection spectrum (UV-vis) records on Japanese SHIMADZU UV-3100 type ultraviolet-visual spectrometer, with BaSO
4Be reference substance, test specification 200-800nm.
Comparative Examples 1
According to document (J.C.Jansen etc., Zeolite, 1984,4:369) the synthetic Ti-ZSM-5 of method is TS-1.
The positive tetraethyl orthosilicate of 22.5 grams is mixed with 7.0 gram TPAOH, and add 59.8 the gram distilled water, mix the back in normal pressure and 60 ℃ of following hydrolysis 1.0 hours, obtain the hydrating solution of positive tetraethyl orthosilicate, under vigorous stirring, add the solution of forming by 1.1 gram tetrabutyl titanates and 5.0 gram anhydrous isopropyl alcohols lentamente, the gained mixture was stirred 3 hours down at 75 ℃, obtain the clear colloid.This colloid is put into the stainless steel sealed reactor, and constant temperature was placed 3 days under 170 ℃ temperature, obtained the mixture of crystallization product; This mixture is filtered, washes with water, and, obtain the former powder of TS-1 in 110 ℃ of dryings 60 minutes.With the former powder of this TS-1 in 550 ℃ of roasting temperatures 3 hours, the TS-1 molecular sieve.
Comparative Examples 2
According to document (Corma A. etc., J.Chem.Soc.Chem.Commun., 1994,147-148) the synthetic silicon titanium feed ratio of method is 50 Ti-MCM-41.
Comparative Examples 3
According to document (CN1226187C) embodiment 1 synthesizing titanium-containing meso-porous molecular sieve material.
Earlier the positive tetraethyl orthosilicate of 50 grams is joined in the aqueous solution that TPAOH and cetyl trimethylammonium bromide form, make it to mix at normal pressure and 40 ℃ of following ultrasonic agitation, tetrabutyl titanate is slowly dripped in wherein getting a mixture, the mol ratio of wherein positive tetraethyl orthosilicate, tetrabutyl titanate, TPAOH, cetyl trimethylammonium bromide and water is 1: 0.02: 0.25: 0.15: 95 again; Above-mentioned system is transferred in the stainless steel sealed reactor, first crystallization 5 hours under 100 ℃ temperature and autogenous pressure, crystallization 48 hours under 120 ℃ temperature and autogenous pressure again, the gained crystallization product is filtered, washes with water, and in 110 ℃ of oven dry 120 minutes, 550 ℃ of roasting temperatures 3 hours, obtain mesoporous titanium-silicon molecular screen material A then.
The X-ray diffraction spectrogram (XRD) of A as shown in Figure 1, Small angle promptly 2 θ 2.3 °, 4.0 ° and 4.6 ° of vicinity diffraction peak is arranged, show that composite sample has the two-dimentional hexagonal mesoporous structure of similar MCM-41.
The fourier infrared spectrogram of A as shown in Figure 2, at 960cm
-1The unexistent charateristic avsorption band of total silicon molecular sieve appears in the vicinity, is the feature of skeleton titanium, shows that titanium has entered the sample skeleton.
Visible-UV spectrum of A as shown in Figure 3, the absorption about 220nm is the feature of four-coordination Ti, does not occur absorption band near 340nm, illustrate that Ti in the titanium-containing mesoporous material that present embodiment prepares is nearly all on skeleton.
Earlier the positive tetraethyl orthosilicate of 50 grams is joined in the aqueous solution that TPAOH and cetyl trimethylammonium bromide form, make it to mix at normal pressure and 35 ℃ of following ultrasonic agitation, under ultrasonic agitation tetrabutyl titanate is slowly dripped in wherein getting a mixture, the mol ratio of wherein positive tetraethyl orthosilicate, tetrabutyl titanate, TPAOH, cetyl trimethylammonium bromide and water is 1: 0.08: 0.45: 0.05: 35 again.This mixed solution is put into the stainless steel sealed reactor, crystallization is 72 hours under 100 ℃ temperature and autogenous pressure, the gained crystallization product is filtered, washes with water, and in 110 ℃ of oven dry 120 minutes, then 550 ℃ of roasting temperatures 3 hours, obtain mesoporous titanium-silicon molecular screen material B, this sample characterizes consistent with the SPECTROSCOPIC CHARACTERIZATION of embodiment 1 sample A through X-ray diffraction, Fourier infrared spectrum and visible-UV spectrum.
Earlier the positive tetraethyl orthosilicate of 50 grams is joined in the aqueous solution that TPAOH and cetyl trimethylammonium bromide form, make it to mix at normal pressure and 55 ℃ of following ultrasonic agitation, under ultrasonic agitation tetrabutyl titanate is slowly dripped in wherein getting a mixture, the mol ratio of wherein positive tetraethyl orthosilicate, tetrabutyl titanate, TPAOH, cetyl trimethylammonium bromide and water is 1: 0.04: 0.18: 0.22: 120 again.This mixed solution is put into the stainless steel sealed reactor, first crystallization 5 hours under 100 ℃ temperature and autogenous pressure, crystallization 24 hours under 120 ℃ temperature and autogenous pressure again, the gained crystallization product is filtered, washes with water, and in 110 ℃ of oven dry 120 minutes, 550 ℃ of roasting temperatures 3 hours, obtain mesoporous titanium-silicon molecular screen material C then, this sample characterizes consistent with the SPECTROSCOPIC CHARACTERIZATION of embodiment 1 sample A through X-ray diffraction, Fourier infrared spectrum and visible-UV spectrum.
Earlier the positive tetraethyl orthosilicate of 50 grams is joined in the aqueous solution that TPAOH and Tetradecyl Trimethyl Ammonium Bromide form, make it to mix at normal pressure and 30 ℃ of following ultrasonic agitation, under ultrasonic agitation tetrabutyl titanate is slowly dripped in wherein getting a mixture, the mol ratio of wherein positive tetraethyl orthosilicate, tetrabutyl titanate, TPAOH, Tetradecyl Trimethyl Ammonium Bromide and water is 1: 0.12: 0.15: 0.25: 80 again.This mixed solution is put into the stainless steel sealed reactor, crystallization is 48 hours under 120 ℃ temperature and autogenous pressure, the gained crystallization product is filtered, washes with water, and in 110 ℃ of oven dry 120 minutes, then 550 ℃ of roasting temperatures 3 hours, obtain mesoporous titanium-silicon molecular screen material D, this sample characterizes consistent with the SPECTROSCOPIC CHARACTERIZATION of embodiment 1 sample A through X-ray diffraction, Fourier infrared spectrum and visible-UV spectrum.
Earlier the positive tetraethyl orthosilicate of 50 grams is joined in the aqueous solution that TPAOH and cetyl trimethylammonium bromide form, make it to mix at normal pressure and 60 ℃ of following ultrasonic agitation, under ultrasonic agitation tetrabutyl titanate is slowly dripped in wherein getting a mixture, the mol ratio of wherein positive tetraethyl orthosilicate, tetrabutyl titanate, TPAOH, cetyl trimethylammonium bromide and water is 1: 0.2: 0.4: 0.1: 160 again.This mixed solution is put into the stainless steel sealed reactor, first crystallization 4 hours under 100 ℃ temperature and autogenous pressure, crystallization 24 hours under 160 ℃ temperature and autogenous pressure again, the gained crystallization product is filtered, washes with water, and in 110 ℃ of oven dry 120 minutes, 550 ℃ of roasting temperatures 3 hours, obtain mesoporous titanium-silicon molecular screen material E then, this sample characterizes consistent with the SPECTROSCOPIC CHARACTERIZATION of embodiment 1 sample A through X-ray diffraction, Fourier infrared spectrum and visible-UV spectrum.
The method gained sample of present embodiment explanation the inventive method and Comparative Examples is used for the effect of the catalytic oxidation of phenol hydroxylation.
The sample that the foregoing description and Comparative Examples is prepared is according to sample: phenol: the weight ratio of acetone=1: 25.0: 15.0 mixes in a there-necked flask that has a prolong, be warming up to 80 ℃, then under whipped state according to phenol: it is 27.5% hydrogen peroxide that the weight ratio of hydrogen peroxide=1: 0.35 adds mass percentage concentration, reaction is 6 hours under this temperature, products therefrom uses the OV-101 capillary column on the Varian3400 chromatographic instrument (30m * 0.25mm) measure each product to distribute the results are shown in Table 1.In table 1:
Table 1
The method gained sieve sample of present embodiment explanation the inventive method and Comparative Examples is used for 2,3, the effect of the catalytic oxidation of 6-pseudocuminol hydroxylation reaction.
2,3,6-pseudocuminol hydroxylation reaction is in carrying out in a volume is 30 milliliters the reactor that has circulator bath cover under 80 ℃, the catalyst sample consumption is 0.25 gram, 0.146 2,3 of mole, the 6-pseudocuminol is dissolved in 5 milliliters of acetonitriles, the dilute hydrogen peroxide that disposable adding is 0.055 mole, magnetic agitation reaction extract supernatant liquor and carry out result's test after centrifugal after 2 hours.Product Agilent GC-6890N type gas chromatograph and the HP-5 chromatogram column analysis that has thermal conductance and hydrogen flame dual-detector.The results are shown in Table 2.
In table 2:
Table 2
Phenol transformation efficiency % | Quinone | |
Embodiment | ||
1 | 22.6 | 86 |
|
21.2 | 88 |
|
22.4 | 81 |
|
20.6 | 85 |
|
19.1 | 83 |
Comparative Examples 1 | 1.6 | 75 |
Comparative Examples 2 | 3.4 | 77 |
Comparative Examples 3 | 8.1 | 85 |
As can be seen from Table 2: mesoporous titanium-silicon molecular screen material catalytic effect provided by the invention is significantly better than the molecular sieve of single structure, and its transformation efficiency is improved largely.
Claims (26)
1. the synthetic method of a mesoporous titanium-silicon molecular screen material is characterized in that silicon source, titanium source, organo-alkali compound and tensio-active agent are mixed, and utilizes the ultrasonic agitation technology to make it evenly, with the mixture that obtains through hydrothermal crystallizing and reclaim product.
2. according to the synthetic method of claim 1, it is characterized in that earlier the silicon source being joined in the mixed aqueous solution of being made up of organo-alkali compound and tensio-active agent, utilize the ultrasonic agitation technology to make it mixing, again the titanium source is dripped in wherein, continue ultrasonic agitation and form uniform mixture, through hydrothermal crystallizing and reclaim product.
3. according to the method for claim 1, it is characterized in that said mixture mole consists of the silicon source: titanium source: organic bases: tensio-active agent: water=1: (0.0005-0.5): (0.05-0.8): (0.01-0.5): (5-220), wherein the silicon source is with SiO
2Meter, the titanium source is with TiO
2Meter.
4. according to the method for claim 3, it is characterized in that said mixture mole consists of the silicon source: titanium source: organic bases: tensio-active agent: water=1: (0.005-0.5): (0.05-0.5): (0.05-0.5): (20-180).
5. according to the method for claim 1, it is characterized in that said hydrothermal crystallization process be with mixture in sealed reactor under 20-190 ℃ and autogenous pressure hydrothermal crystallizing handled 2-360 hour, perhaps earlier 60-120 ℃ pre-crystallization 0.5-10 hour down, and then 80-180 ℃ of following crystallization 1 hour to 10 days.
6. according to the method for claim 1, it is characterized in that said silicon source is the organosilicon acid esters.
7. according to the method for claim 6, it is characterized in that said its general formula of organosilicon acid esters is R
1 4SiO
4, R wherein
1Be selected from alkyl with 1-4 carbon atom.
8. according to the method for claim 1, it is characterized in that said titanium source is inorganic titanium salt or organic titanate.
9. according to the method for claim 8, it is characterized in that said inorganic titanium salt is selected from TiX
4, TiX
3, TiOX
2Or Ti (SO
4)
2, wherein X represents halogen.
10. according to the method for claim 9, wherein said halogen is a chlorine.
11. according to the method for claim 8, wherein said its general formula of organic titanate is Ti (OR
2)
4, R wherein
2Be selected from alkyl with 1-6 carbon atom.
12. according to the method for claim 11, wherein R
2Be selected from alkyl with 2-4 carbon atom.
13. according to the method for claim 1, it is characterized in that said silicon source is the organosilicon acid esters, said titanium source is an organic titanate.
14., it is characterized in that said tensio-active agent is a cats product according to the method for claim 1.
15. according to the method for claim 14, said cats product is that general formula is (R
3R
4NR
5R
6)
+X
-Quaternary ammonium salt surface active agent, wherein X represents halogen, R
3, R
4And R
5Be the alkyl that is less than 3 carbon atoms, R
3, R
4And R
5Carbonatoms can be identical or different, R
6For having the alkyl that is no less than 12 carbon atoms.
16. according to the method for claim 15, said R
6Alkyl for 12-22 carbon atom.
17. according to the method for claim 15, said quaternary ammonium salt surface active agent is Tetradecyl Trimethyl Ammonium Bromide or cetyl trimethylammonium bromide.
18., it is characterized in that the mixture that said organo-alkali compound is selected from quaternary ammonium hydroxide compounds, fat amine compound, alcamine compound or is made up of them according to the method for claim 1.
19. according to the method for claim 18, wherein said its general formula of fat amine compound is R
7(NH
2)
n, R wherein
7Be selected from alkyl or alkylidene group, n=1 or 2 with 1-4 carbon atom.
20. according to the method for claim 19, wherein said fat amine compound is ethamine, n-Butyl Amine 99, butanediamine or hexanediamine.
21. according to the method for claim 18, wherein said its general formula of alcamine compound is (HOR
8)
mNH
(3-m)R wherein
8Be selected from alkyl with 1-4 carbon atom; M=1,2 or 3.
22. according to the method for claim 21, wherein said alcamine compound is monoethanolamine, diethanolamine or trolamine.
23. according to the method for claim 18, wherein said its general formula of quaternary ammonium hydroxide compounds is (R
9)
4NOH, wherein R
9For having the alkyl of 1-4 carbon atom.
24. according to the method for claim 18, wherein said quaternary ammonium hydroxide compounds is a TPAOH.
25. method according to claim 1, wherein said hydrothermal crystallizing condition is meant in the 80-180 ℃ of encloses container under the autogenous pressure hydrothermal crystallizing 24-144 hour, perhaps earlier 60-120 ℃ pre-crystallization 1-8 hour down, and then 80-180 ℃ of following crystallization 1 hour to 3 days.
26. according to the method for claim 1, it is characterized in that said hydrothermal crystallizing treating processes static or dynamically under carry out.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2006101442156A CN101190794B (en) | 2006-11-30 | 2006-11-30 | Method for synthesizing mesoporous titanium-silicon molecular screen material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2006101442156A CN101190794B (en) | 2006-11-30 | 2006-11-30 | Method for synthesizing mesoporous titanium-silicon molecular screen material |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101190794A true CN101190794A (en) | 2008-06-04 |
CN101190794B CN101190794B (en) | 2011-08-10 |
Family
ID=39486018
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2006101442156A Active CN101190794B (en) | 2006-11-30 | 2006-11-30 | Method for synthesizing mesoporous titanium-silicon molecular screen material |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101190794B (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102530982A (en) * | 2012-01-09 | 2012-07-04 | 河北科技大学 | Method for preparing titanium silicalite film by dynamic in-situ hydrothermal method |
CN102826566A (en) * | 2012-09-25 | 2012-12-19 | 宁夏兴平精细化工股份有限公司 | Synthetic method of mesoporous molecular sieve used for thioether oxidization |
CN103420393A (en) * | 2012-05-23 | 2013-12-04 | 中国石油化工股份有限公司 | Method for removing templates from original powder of titanium silicalite, titanium silicalite and preparation method and applications thereof |
CN104418344A (en) * | 2013-09-09 | 2015-03-18 | 中国石油化工股份有限公司 | Synthesis method of all-silicon mesoporous material |
CN105921170A (en) * | 2016-05-03 | 2016-09-07 | 新疆大学 | Technical method for novel nano-scale FeZSM-5 catalyst for flue gas denitration |
CN106904631A (en) * | 2015-12-23 | 2017-06-30 | 中国石油化工股份有限公司 | Mesoporous tin silicon materials and its synthetic method and application and a kind of method of oxidizing cyclic ketone |
CN107720771A (en) * | 2017-09-15 | 2018-02-23 | 武汉理工大学 | A kind of macropore microporous molecular sieve catalyst TS 1 preparation method |
CN109647505A (en) * | 2018-12-26 | 2019-04-19 | 南京红宝丽聚氨酯有限公司 | A kind of titanium-silicon molecular sieve catalyst and preparation method thereof |
CN110467193A (en) * | 2018-05-10 | 2019-11-19 | 中国科学院过程工程研究所 | A kind of Titanium Sieve Molecular Sieve, preparation method and application |
CN111186843A (en) * | 2018-11-15 | 2020-05-22 | 中国科学院大连化学物理研究所 | Method for preparing hierarchical porous titanium silicon TS-1 molecular sieve |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107032365B (en) * | 2015-07-29 | 2019-01-29 | 武汉理工大学 | A kind of solid phase synthesis process of titanium-silicon molecular sieve TS-1 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1050584C (en) * | 1996-06-05 | 2000-03-22 | 中国石油化工总公司 | Method for preparing titanium-silicon molecular sieve (TS-1) |
CN1245089A (en) * | 1998-08-18 | 2000-02-23 | 中国石油化工集团公司 | Process for preparing Ti-Si molecular sieve |
CN1137048C (en) * | 2001-08-20 | 2004-02-04 | 复旦大学 | Process for synthesizing mesoporous silicon oxide molecular sieve material by ultrasonic system |
CN1254436C (en) * | 2004-11-12 | 2006-05-03 | 太原理工大学 | Spherical mesoporous molecular sieve with narrow particle size distribution and its prepn |
-
2006
- 2006-11-30 CN CN2006101442156A patent/CN101190794B/en active Active
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102530982A (en) * | 2012-01-09 | 2012-07-04 | 河北科技大学 | Method for preparing titanium silicalite film by dynamic in-situ hydrothermal method |
CN103420393A (en) * | 2012-05-23 | 2013-12-04 | 中国石油化工股份有限公司 | Method for removing templates from original powder of titanium silicalite, titanium silicalite and preparation method and applications thereof |
CN102826566A (en) * | 2012-09-25 | 2012-12-19 | 宁夏兴平精细化工股份有限公司 | Synthetic method of mesoporous molecular sieve used for thioether oxidization |
CN104418344A (en) * | 2013-09-09 | 2015-03-18 | 中国石油化工股份有限公司 | Synthesis method of all-silicon mesoporous material |
CN106904631B (en) * | 2015-12-23 | 2019-04-16 | 中国石油化工股份有限公司 | Mesoporous tin silicon materials and its synthetic method and application and a kind of method of oxidizing cyclic ketone |
CN106904631A (en) * | 2015-12-23 | 2017-06-30 | 中国石油化工股份有限公司 | Mesoporous tin silicon materials and its synthetic method and application and a kind of method of oxidizing cyclic ketone |
CN105921170A (en) * | 2016-05-03 | 2016-09-07 | 新疆大学 | Technical method for novel nano-scale FeZSM-5 catalyst for flue gas denitration |
CN107720771A (en) * | 2017-09-15 | 2018-02-23 | 武汉理工大学 | A kind of macropore microporous molecular sieve catalyst TS 1 preparation method |
CN110467193A (en) * | 2018-05-10 | 2019-11-19 | 中国科学院过程工程研究所 | A kind of Titanium Sieve Molecular Sieve, preparation method and application |
CN110467193B (en) * | 2018-05-10 | 2023-06-27 | 中国科学院过程工程研究所 | Titanium-silicon molecular sieve, preparation method and application thereof |
CN111186843A (en) * | 2018-11-15 | 2020-05-22 | 中国科学院大连化学物理研究所 | Method for preparing hierarchical porous titanium silicon TS-1 molecular sieve |
CN111186843B (en) * | 2018-11-15 | 2021-12-14 | 中国科学院大连化学物理研究所 | Method for preparing hierarchical porous titanium silicon TS-1 molecular sieve |
CN109647505A (en) * | 2018-12-26 | 2019-04-19 | 南京红宝丽聚氨酯有限公司 | A kind of titanium-silicon molecular sieve catalyst and preparation method thereof |
CN109647505B (en) * | 2018-12-26 | 2021-12-24 | 南京红宝丽聚氨酯有限公司 | Titanium-silicon molecular sieve catalyst and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN101190794B (en) | 2011-08-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101190794B (en) | Method for synthesizing mesoporous titanium-silicon molecular screen material | |
CN101190793B (en) | Method for synthesizing TS-1 molecular screen | |
CN101190792A (en) | Method for synthesizing titanium-silicon molecular screen | |
CN104556111B (en) | A kind of Titanium Sieve Molecular Sieve and its synthetic method | |
Hulea et al. | Styrene oxidation with H2O2 over Ti-containing molecular sieves with MFI, BEA and MCM-41 topologies | |
CN101172243B (en) | Mesoporous material/micropore molecular sieve composite material and preparation method thereof | |
CN104556114B (en) | A kind of method of the micro- mesoporous composite material of synthesis of titanium silicon | |
CN105728013B (en) | Vanadium doping aoxidizes silicon substrate mesoporous molecular sieve catalyst and the preparation method and application thereof | |
CN110180586A (en) | The alkali metal ion modifying titanium-silicon molecular sieve TS-1 and preparation method thereof reacted for propylene and hydrogen peroxide gas-phase epoxidation | |
CN101497450B (en) | Method for preparing titanium-containing mesoporous material | |
Luo et al. | Study on Ti-MCM-41 zeolites prepared with inorganic Ti sources: synthesis, characterization and catalysis | |
CN105271294B (en) | Tin-silicon molecular sieve and synthetic method and application thereof, and phenol hydroxylation method | |
CN107188194B (en) | A method of preparing high catalytic activity Ti-MWW molecular sieve | |
Moliner et al. | Synthesis of expanded titanosilicate MWW-related materials from a pure silica precursor | |
CN101205075B (en) | Method for synthesizing titanium-containing molecular sieve material | |
CN104512904B (en) | A kind of method preparing mesoporous titanium-silicon material | |
CN103818924B (en) | Preparation method of titanium-silicon molecular sieve and application | |
CN103395798B (en) | Synthesis method of Ti-Beta molecular sieve | |
CN101519213B (en) | Synthetic method of titanium-containing mesoporous materials | |
CN101497451B (en) | Method for preparing mesoporous titanium-silicon material | |
CN104556109B (en) | Method for preparing titanosilicate molecular sieve and phenol oxidation method | |
CN106904633A (en) | Modified with noble metals mesoporous titanium-silicon molecular screen and its synthetic method and application and a kind of method of oxidizing cyclic ketone | |
Mutlu et al. | Synthesis of butyl glucoside over sulphated Zr-SBA-15 and tungstophosphoric acid incorporated SBA-15 catalysts | |
CN105217650B (en) | Mesoporous titanium silicate molecular sieve, synthetic method therefor and application thereof as well as method for oxidizing 2,6-di-tert-butylphenol | |
CN101314136B (en) | Titanium containing composite material with mesoporous and cellular structure, and preparation thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |