CN1119202C - Process for preparing Fe-Si Molecular sieve - Google Patents
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- CN1119202C CN1119202C CN 99122123 CN99122123A CN1119202C CN 1119202 C CN1119202 C CN 1119202C CN 99122123 CN99122123 CN 99122123 CN 99122123 A CN99122123 A CN 99122123A CN 1119202 C CN1119202 C CN 1119202C
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- 239000002808 molecular sieve Substances 0.000 title claims abstract description 16
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 229910017082 Fe-Si Inorganic materials 0.000 title 1
- 229910017133 Fe—Si Inorganic materials 0.000 title 1
- 238000004519 manufacturing process Methods 0.000 title 1
- LPSKDVINWQNWFE-UHFFFAOYSA-M tetrapropylazanium;hydroxide Chemical compound [OH-].CCC[N+](CCC)(CCC)CCC LPSKDVINWQNWFE-UHFFFAOYSA-M 0.000 claims abstract description 35
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 25
- 239000010936 titanium Substances 0.000 claims abstract description 21
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 19
- 239000010703 silicon Substances 0.000 claims abstract description 19
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000005216 hydrothermal crystallization Methods 0.000 claims abstract 4
- UGACIEPFGXRWCH-UHFFFAOYSA-N [Si].[Ti] Chemical compound [Si].[Ti] UGACIEPFGXRWCH-UHFFFAOYSA-N 0.000 claims abstract 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 29
- 239000000203 mixture Substances 0.000 claims description 22
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 18
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 16
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 11
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical group CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 10
- 229910052757 nitrogen Inorganic materials 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- 150000003608 titanium Chemical class 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 2
- 239000000741 silica gel Substances 0.000 claims description 2
- 229910002027 silica gel Inorganic materials 0.000 claims description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical group [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 claims 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims 1
- 239000011541 reaction mixture Substances 0.000 claims 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 19
- 238000002425 crystallisation Methods 0.000 description 18
- 230000008025 crystallization Effects 0.000 description 18
- 238000006555 catalytic reaction Methods 0.000 description 12
- 239000000243 solution Substances 0.000 description 11
- 239000010457 zeolite Substances 0.000 description 11
- 229910021536 Zeolite Inorganic materials 0.000 description 10
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 10
- 230000005540 biological transmission Effects 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- -1 comprises Ti-Si-1 Chemical compound 0.000 description 8
- 238000002441 X-ray diffraction Methods 0.000 description 7
- 238000007796 conventional method Methods 0.000 description 7
- 239000013078 crystal Substances 0.000 description 7
- 239000008367 deionised water Substances 0.000 description 7
- 229910021641 deionized water Inorganic materials 0.000 description 7
- 238000001035 drying Methods 0.000 description 7
- UHIFJPAQGVQMPP-UHFFFAOYSA-N N.[Si+4] Chemical compound N.[Si+4] UHIFJPAQGVQMPP-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 6
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 6
- 239000004810 polytetrafluoroethylene Substances 0.000 description 6
- 239000000376 reactant Substances 0.000 description 6
- 229910001220 stainless steel Inorganic materials 0.000 description 6
- 239000010935 stainless steel Substances 0.000 description 6
- 238000013019 agitation Methods 0.000 description 5
- 150000002148 esters Chemical class 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- JMXKSZRRTHPKDL-UHFFFAOYSA-N titanium ethoxide Chemical class [Ti+4].CC[O-].CC[O-].CC[O-].CC[O-] JMXKSZRRTHPKDL-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000009792 diffusion process Methods 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 150000007530 organic bases Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241001502050 Acis Species 0.000 description 1
- 235000011299 Brassica oleracea var botrytis Nutrition 0.000 description 1
- 240000003259 Brassica oleracea var. botrytis Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241001207999 Notaris Species 0.000 description 1
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000006184 cosolvent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000007323 disproportionation reaction Methods 0.000 description 1
- 238000006735 epoxidation reaction Methods 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 230000000640 hydroxylating effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012229 microporous material Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
- 150000005622 tetraalkylammonium hydroxides Chemical class 0.000 description 1
- 150000003609 titanium compounds Chemical class 0.000 description 1
- 238000012876 topography Methods 0.000 description 1
- YFTHZRPMJXBUME-UHFFFAOYSA-N tripropylamine Chemical compound CCCN(CCC)CCC YFTHZRPMJXBUME-UHFFFAOYSA-N 0.000 description 1
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- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
本发明提供了一种具有MFI结构、晶粒尺寸小于0.3微米的钛硅分子筛的制备方法，该方法是按照反应混合物SiO2∶TiO2∶TPA+∶H2O＝1∶0.005～0.1∶0.10～0.20∶20～50的摩尔配比，将硅源、钛源、四丙基氢氧化铵和水混合均匀，在室温下保持0.5～3小时，70～90℃保持3～6小时后，于110～150℃水热晶化1～3天，150～180℃水热晶化0～10小时。与现有技术相比，本发明所提供的方法降低了铵硅比，减少了四丙基氢氧化铵的用量，大大降低了制备成本。The present invention provides a method for preparing a titanium - silicon molecular sieve with an MFI structure and a grain size of less than 0.3 microns. 0.20: 20-50 molar ratio, mix silicon source, titanium source, tetrapropylammonium hydroxide and water evenly, keep at room temperature for 0.5-3 hours, keep at 70-90°C for 3-6 hours, then place at 110 ~150°C hydrothermal crystallization for 1-3 days, 150-180°C hydrothermal crystallization for 0-10 hours. Compared with the prior art, the method provided by the invention reduces the ratio of ammonium to silicon, reduces the consumption of tetrapropylammonium hydroxide, and greatly reduces the preparation cost.
Description
The invention relates to the synthetic method of HTS, more specifically say so about having MFI topological structure, crystallite dimension preparation method less than 0.3 micron HTS.
HTS is that a class is in developing new catalytic material, they have regular pore passage structure, the titanium derivative that belongs to the Silicalite zeolite mainly comprises Ti-Si-1, Ti-Si-2, Ti-β, Ti-MCM-41, Ti-MCM-48, Ti-HMS, Ti-MSU etc.The Ti-Si-1 molecular sieve (being called for short TS-1) that wherein has the MFI topological structure is selected the catalytic performance that has uniqueness in the shape oxidation reaction at the organic compound that with the hydrogen peroxide is oxidant, it can be in reactions such as the oxidation of the oxidation of catalysis saturated hydrocarbons under the mild reaction conditions, alcohol, alkene epoxidation, aromatic hydrocarbon hydroxylating, ammoxidation of cyclohexanone, technology is simple and safe, environmentally friendly, not only conversion ratio height, and selectivity is good.
The TS-1 molecular sieve is general to adopt organic hydro-thermal method synthetic.USP4410501 has at first disclosed its preparation method, this method is after mixing silicon source, titanium source, organic base and water evenly by certain reaction thing proportioning, 130--200 ℃ of following hydrothermal crystallizing is 6-30 days in autoclave, separate then, wash, dry and product.Wherein the silicon source can be the tetraalkyl esters of silicon acis, silica colloidal or alkali silicate, preferred silicon tetraethyl acid esters; The titanium source is hydrolyzable titanium compound, preferred tetraethyl titanate esters; Organic base is a tetra-alkyl ammonium hydroxide, preferred TPAOH (TPAOH).Wherein the mole compositing range of reactant mixture is:
The general range preferable range
SiO
2/TiO
2 5～200 35～65
OH
-/SiO
2 0.1～1.0 0.3～0.6
H
2O/SiO
2 20～200 60～100
RN
+/SiO
2 0.1～2.0 0.4～1.0
Zeolites, Vol 12, and p943 has reported a kind of method of improved synthetic TS-1 molecular sieve in 1992, can make in the framework of molecular sieve Ti content higher.This method is to substitute the tetraethyl titanate esters with the slower tetrabutyl titanate ester of hydrolysis rate, and is cosolvent with anhydrous isopropyl alcohol, is SiO with the mole proportioning
2: xTiO
2: 0.36TPA
+: 35H
2The reactant mixture of O was 170 ℃ of following hydrothermal crystallizings 1～2 day.
We know that TS-1 molecular sieve catalytic oxidation reaction generally mostly is DIFFUSION CONTROLLED, because diffusion-restricted effect in existing, the activity of catalytic reaction is relevant with the macrostructure and the utilization rate of inner surface of TS-1 molecular sieve with selectivity.Catalyst crystal grain is bigger, and the diffusion length in the micropore increases, and the concentration of intragranular each point and temperature distributing disproportionation are even, causes the reaction rate difference of the inner each point of catalyst, thereby influences the activity and the selectivity of catalytic reaction.If catalyst crystal grain is very little, effective diffusion cofficient is very big, the influence of diffusion effect in then can eliminating substantially.Hence one can see that, and the zeolite crystal size is very important in the shape selective catalysis reaction, and crystal grain is more little, and oxidation susceptibility is good more.
Appl.Catal.A 92 (1992) 93-111 system thinkings in preparation process ammonium-silicon ratio to the influence of HTS grain size and surface topography, 175 ℃ of crystallization temperatures, when ammonium-silicon ratio 0.22～0.4 the time, TS-1 zeolite crystal size is less, be about 0.15～0.3 μ m, and ammonium-silicon ratio is beyond this scope, and as 0.11,0.54 and 0.76 o'clock, grain size is all more than 0.6 μ m.
Applied Catalysis A:General, 99 (1993) 71～84 have reported the work of European catalysis association (Eurocat) aspect synthetic, the sign of formulating standard TS-1 molecular sieve and catalytic reaction.The raw material of the synthetic TS-1 molecular sieve that it adopts is silicon tetraethyl acid esters, tetraethyl titanate esters and TPAOH, and the mole proportioning of reactant mixture is SiO
2/ TiO
2=35; TPA
+/ SiO
2=0.36; H
2O/SiO
2=28.2, reaction condition is 175 ℃ of following hydrothermal crystallizings 4 days, and synthetic grain size is about 0.15 μ m.
In addition, be that author's " Studies in SurfaceScience and Catalysis; 37 (1988) 413 " etc. is synthetic or characterize in the document of TS-1 at " Applied Catalysis A:General 110 (1994) 137～151 ", " Journalof Catalysis 129; (1991) 1 ", " Journal of Catalysis 133 (1992) 220～230 ", particularly one of USP4410501 inventor's B.NOTARI, the preparation crystallization temperature that TS-1 adopted is all at 160～180 ℃.
As seen, the existing preparation in the method for TS-1, in order to guarantee the grain size below the molecular sieve 0.3 μ m, all between 0.2～0.4, crystallization temperature is all in 160～180 ℃ of scopes for ammonium-silicon ratio in its batching.
TPAOH (TPAOH) is considered to synthetic optimal alkali source of TS-1 molecular sieve and template agent, but its price is very expensive, if be 0.3～0.4 to calculate synthetic 1 ton of TS-1 with ammonium-silicon ratio, probably need 1～1.33 ton of TPAOH, cause the cost of synthetic TS-1 very high.
The objective of the invention is to provide on the basis of existing technology a kind of TPAOH consumption that reduces, synthetic grain size is less than the method for the HTS of 0.3 μ m.
The inventor finds, TPAOH is as alkali source and template agent, under crystallization temperature, is decomposed into Tri-n-Propylamine easily and loses the effect of template agent.At reaction condition is 170 ℃, in the time of 12 hours, the resolution ratio of TPAOH has reached 87.2%, and the TPAOH in feeding intake is described, under 170 ℃ of crystallization temperatures, really plays template agent and alkali source effect, and only less than 20%, the overwhelming majority has been decomposed; And 110～150 ℃ of temperature ranges, the resolution ratio of TPAOH is only less than 20%.
Method provided by the invention is according to reactant mixture SiO
2: TiO
2: TPA
+: H
2O=1: 0.005～0.1: 0.10～0.20: 20～50 mole proportioning, silicon source, titanium source, TPAOH and water are mixed, at room temperature kept 0.5～3 hour, 70～90 ℃ kept after 3～6 hours, in 110～150 ℃ of hydrothermal crystallizings 1～3 day, 150～180 ℃ of hydrothermal crystallizings 0～10 hour.
Said silicon source is selected from silica gel, Ludox or organosilicon acid esters; Preferred formula is (OR
1)
4The organosilicon acid esters of Si, R
1It is the alkyl of 1～4 carbon atom; More preferably tetraethyl orthosilicate.
Said titanium source is selected from inorganic titanium salt or organic titanate, and inorganic titanium salt is optional from TiCl
4, TiOCl
2, TiOSO
4Or Ti (SO
4)
2One of; Preferred formula is (OR
2)
4The organic titanate of Ti, R
2It is the alkyl of 2～4 carbon atoms; More preferably butyl titanate.When the titanium source is organic titanate, before the use, preferably organic titanate is dissolved in earlier in the anhydrous isopropyl alcohol, the mol ratio of organic titanate and anhydrous isopropyl alcohol is 1: 0～60.
In the method provided by the invention, used silicon source, titanium source and TPAOH, method is they to be cooled to 0 ℃ respectively in advance before mixing preferably; Preferably batching be in proper order earlier with the silicon source be cooled to 0 ℃ after mix in the titanium source and mix with the TPAOH that is cooled to 0 ℃ in advance again.
In the method provided by the invention, for the generation of other compound of preventing titanium better, silicon source, titanium source and TPAOH preferably mix under nitrogen protection, with isolated CO
2Atmosphere.
In order to improve the MFI topology structure of molecular sieve more, after low temperature crystallized end, also crystallization temperature can be brought up to conventional 160～180 ℃, again one short period of crystallization.
Method provided by the invention, having adopted than prior art is low crystallization temperature, 110～150 ℃ of following crystallization, can significantly reduce the decomposition of TPAOH, not only improve the utilization rate of TPAOH, and increased the basicity of system relatively, and then shortened crystallization time.
Method provided by the invention can synthesize little crystal grain TS-1 molecular sieve under low ammonium-silicon ratio condition, by electromicroscopic photograph as can be known, its crystal grain is 0.2～0.3 μ m and cauliflower type of uniform size; Owing to reduced the consumption of TPAOH, synthetic 1 ton of crystallite dimension is less than the TS-1 of 0.3 μ m, and needing 1～1.33 ton TPAOH to reduce to by prior art only needs 0.45～0.67 ton of TPAOH, greatly reduce preparation cost.
Fig. 1 is " Microporous Materials ", and Vol 22, p637, the standard x optical diffraction spectrogram (XRD) of the HTS with MFI structure of record on 1998.
Fig. 2 is the transmission electron microscope photo of sample, and wherein a and b are respectively the transmission electron microscope photo of Comparative Examples 1 and embodiment 1 gained sample.
Following example will the present invention is further illustrated, but the present invention is not subjected to the restriction of these examples.
In each of the embodiments described below, used tetraethyl orthosilicate is Beijing chemical reagents corporation product; Butyl titanate is Beijing imperial chemical reagent of gold Co., Ltd product; TPAOH (TPAOH) changes into product for Tokyo; Anhydrous isopropyl alcohol is a chemical pure, Beijing Chemical Plant's product.
Comparative Examples 1
The explanation of this Comparative Examples is according to Applied Catalysis A:General, and 99 (1993) 71～84 reported method prepare the feature of TS-1 molecular sieve.
According to reactant mixture SiO
2: TiO
2: TPA
+: H
2O=1: 0.029: 0.13: 28.2 mole proportioning; in nitrogen protection; under 35 ℃ 20 gram tetraethyl orthosilicates and tetraethyl titanate are mixed; be cooled to 0 ℃, the TPAOH that is cooled to 0 ℃ is slowly splashed into, form clear liquid; this clear liquid is warmed up under 80～90 ℃ of stirrings kept 4 hours; add a certain amount of deionized water, above-mentioned reactant mixture is moved into autoclave, 175 ℃ of following hydrothermal crystallizings 4 days.Filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS-1 spectrogram, transmission electron microscope photo is seen a of Fig. 2.
Example 1
1.36 gram butyl titanates are dissolved in 7 milliliters of anhydrous isopropyl alcohol solution; under nitrogen protection, pour in the tetraethyl orthosilicate solution, stir half an hour; be cooled to 0 ℃; slowly splash into the TPAOH aqueous solution that has been chilled to 0 ℃ again, stir half an hour, kept 2 hours under the room temperature; being warmed up to 70～80 ℃ again stirred 4 hours; add deionized water, stir, the mole of this mixture consists of:
SiO
2∶TiO
2∶TPA
+∶H
2O＝1∶0.033∶0.13∶25
Said mixture is moved in the stainless steel cauldron of inner liner polytetrafluoroethylene, in 120 ℃ of crystallization 3 days, filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS1 spectrogram, transmission electron microscope photo is seen the b of Fig. 2.
Example 2
0.89 gram butyl titanate is dissolved in 5 milliliters of anhydrous isopropyl alcohol solution; under nitrogen protection, pour in the tetraethyl orthosilicate solution, stir half an hour; be cooled to 0 ℃; slowly splash into the TPAOH aqueous solution that has been chilled to 0 ℃ again, stir half an hour, kept 2 hours under the room temperature; added thermal agitation 5 hours at 70～80 ℃ then; add deionized water, stir, the mole of mixture consists of:
SiO
2∶TiO
2∶TPA
+∶H
2O＝1∶0.022∶0.15∶20
Said mixture is moved in the stainless steel cauldron of inner liner polytetrafluoroethylene, in 130 ℃ of crystallization 2 days, filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS-1 spectrogram, the b of transmission electron microscope photo and Fig. 2 is similar.
Example 3
0.89 gram butyl titanate is dissolved in 5 milliliters of anhydrous isopropyl alcohol solution; under nitrogen protection, pour in the tetraethyl orthosilicate solution, stir half an hour; be cooled to 0 ℃; slowly splash into the TPAOH aqueous solution that has been chilled to 0 ℃ again, stir half an hour, kept 2 hours under the room temperature; added thermal agitation 4 hours at 70～80 ℃ then; add deionized water, stir, the mole of mixture consists of:
SiO
2∶TiO
2∶TPA
+∶H
2O＝1∶0.022∶0.18∶25
Said mixture is moved in the stainless steel cauldron of inner liner polytetrafluoroethylene, in 140 ℃ of crystallization 2 days, filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS-1 spectrogram, the b of transmission electron microscope photo and Fig. 2 is similar.
Example 4
0.68 gram butyl titanate is dissolved in 5 milliliters of anhydrous isopropyl alcohol solution; under nitrogen protection, pour in the tetraethyl orthosilicate solution, stir half an hour; be cooled to 0 ℃; slowly splash into the TPAOH aqueous solution that has been chilled to 0 ℃ again, stir half an hour, kept 2 hours under the room temperature; added thermal agitation 5 hours at 70～80 ℃ then; add deionized water, stir, the mole of mixture consists of:
SiO
2∶TiO
2∶TPA
+∶H
2O＝1∶0.017∶0.20∶25
Said mixture is moved in the stainless steel cauldron of inner liner polytetrafluoroethylene, in 150 ℃ of crystallization 1 day, filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS-1 spectrogram, the b of transmission electron microscope photo and Fig. 2 is similar.
Example 5
0.89 gram butyl titanate is dissolved in 5 milliliters of anhydrous isopropyl alcohol solution; under nitrogen protection, pour in the tetraethyl orthosilicate solution, stir half an hour; be cooled to 0 ℃; slowly splash into the TPAOH aqueous solution that has been chilled to 0 ℃ again, stir half an hour, kept 2 hours under the room temperature; added thermal agitation 4 hours at 70～80 ℃ then; add deionized water, stir, the mole of mixture consists of:
SiO
2∶TiO
2∶TPA
+∶H
2O＝1∶0.022∶0.13∶20
Said mixture is moved in the stainless steel cauldron of inner liner polytetrafluoroethylene, in 125 ℃ of crystallization 3 days, 175 ℃ of following crystallization 8 hours, filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS-1 spectrogram, and the b of transmission electron microscope photo and Fig. 2 is similar.
Example 6
Restrain butyl titanates under nitrogen protection with 1.36; pour in the tetraethyl orthosilicate solution; stir half an hour; slowly splash into the TPAOH aqueous solution, stir half an hour, kept 2 hours under the room temperature; added thermal agitation 3 hours at 70～80 ℃ then; add deionized water, stir, the mole of mixture consists of:
SiO
2∶TiO
2∶TPA
+∶H
2O＝1∶0.01∶0.13∶25
Said mixture is moved in the stainless steel cauldron of inner liner polytetrafluoroethylene, in 120 ℃ of crystallization 3 days, 175 ℃ of following crystallization 10 hours, filter according to a conventional method, wash, drying and roasting get zeolite product, its XRD spectra has the feature of standard TS-1 spectrogram, and the b of transmission electron microscope photo and Fig. 2 is similar.
Claims (11)
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI430951B (en) * | 2011-02-14 | 2014-03-21 | China Petrochemical Dev Corp Taipei Taiwan | Method for preparing large-diameter titanium-silicon molecular sieve and method for producing cyclohexanone oxime using the molecular sieve |
| TWI426050B (en) * | 2011-04-19 | 2014-02-11 | China Petrochemical Dev Corp Taipei Taiwan | A method for preparing titanium-silicon molecular sieve and method for producing cyclohexanone oxime using the molecular sieve |
| CN102502690A (en) | 2011-10-31 | 2012-06-20 | 大连理工大学 | Method for modifying TS (Titanium silicalite)-1 based on mixed liquor of quaternary ammonium salt and inorganic base |
| CN103896301B (en) * | 2012-12-28 | 2015-11-25 | 中国石油化工股份有限公司 | A kind of method of synthesis of titanium silicon molecular sieve |
| CN104944440B (en) * | 2014-03-28 | 2017-11-03 | 中国石油化工股份有限公司 | A kind of HTS poromerics and its synthetic method |
| CN106276944B (en) * | 2015-05-29 | 2019-03-22 | 中国石油化工股份有限公司 | A kind of HTS and its synthetic method and application and a kind of method for hydroxylation of phenol |
| DE102015016908A1 (en) | 2015-12-29 | 2017-06-29 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Nanometer-sized zeolitic particles and process for their preparation |
| CN105692648A (en) * | 2016-04-06 | 2016-06-22 | 上海交通大学 | Method for preparing hierarchical molecular sieve |
| CN107986292B (en) * | 2016-10-27 | 2020-03-24 | 中国石油化工股份有限公司 | A kind of titanium silicon molecular sieve and its synthesis method and application |
| CN109721064B (en) * | 2017-10-31 | 2020-10-27 | 中国石油化工股份有限公司 | Production method of titanium-silicon molecular sieve, titanium-silicon molecular sieve produced by the method and ammoximation reaction method |
| CN109721069B (en) * | 2017-10-31 | 2021-02-09 | 中国石油化工股份有限公司 | Method for producing titanium silicalite molecular sieve, titanium silicalite molecular sieve produced by method and ammoximation reaction method |
| CN112239212B (en) * | 2019-07-19 | 2022-06-07 | 浙江恒逸石化研究院有限公司 | Silicon molecular sieve with MFI topological structure and preparation method and application thereof |
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1999
- 1999-10-27 CN CN 99122123 patent/CN1119202C/en not_active Expired - Lifetime
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