CN1194942A - Process for synthesizing high-silicon ZSM-5 molecular sieve - Google Patents
Process for synthesizing high-silicon ZSM-5 molecular sieve Download PDFInfo
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- CN1194942A CN1194942A CN97103679A CN97103679A CN1194942A CN 1194942 A CN1194942 A CN 1194942A CN 97103679 A CN97103679 A CN 97103679A CN 97103679 A CN97103679 A CN 97103679A CN 1194942 A CN1194942 A CN 1194942A
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Abstract
A process for synthesizing molecular sieve ZSM-5 with solid silica gel as Si source, aluminium sulfate or sodium meta-aluminate as Al source and alkylamines of organic substance (Q) as organic templating agent includes such technological steps as preparing reaction mixture with mole ratio of 100-1000 for SiO2/Al2O3, 1-9.5 for H2O/SiO2, 0.02-0.3 for Na2O/SiO2, and 0.02-0.5 for Q/SiO2, and hydrothermal crystallizing or higher temp crystallizing after ageing at 20-105 deg.C for 4-48 hr. Its advantages are high synthesis efficiency and less consumption of organic templating agent.
Description
The present invention relates to a kind of synthetic method of high silica ZSM-5 molecular sieve.
The ZSM-5 molecular sieve (USP 3702886,1972 years) of U.S. Mobil oil company invention has obtained using extremely widely in petrochemical process such as the shape slective cracking of hydro carbons, alkylation, isomerization, disproportionation, dewaxing, etherificate.The method of being reported among the USP 3702886 can only synthesizing Si-Al than less than 100 ZSM-5 molecular sieve, and to use expensive TPAOH organic formwork agent.
The ZSM-5 molecular sieve of high silica alumina ratio ZSM-5 molecular sieve than low silica-alumina ratio in many chemical processes is more useful.The ZSM-5 molecular sieve of low silica-alumina ratio can synthesize by the reaction mixture that does not contain organic template, but the ZSM-5 zeolite of high silica alumina ratio generally need use organic formwork agent just can be synthesized, and that is to say the synthetic difficulty of wanting relatively of high silica ZSM-5.USP 3941871 and USP 4061724 have reported silica alumina ratio synthetic greater than 200 ZSM-5 molecular sieve, but employed organic formwork agent still is quaternary ammonium compound or organophosphorus compound, costs an arm and a leg.In addition, also adopting organo phosphorous compounds among the USP 4528172 is the synthetic ZSM-5 of template.
In the synthetic method of the ZSM-5 molecular sieve that USP 4526879 is reported, adopting the mixture of alkylamine and haloalkane is template (R), and adds a kind of solvent that dissolves each other, and the mole proportioning of its reaction mixture is SiO
2/ Al
2O
3=10～500, H
2O/SiO
2=10～100, Na
2O/SiO
2=0.1～2.0, R/SiO
2=0.05～1.0.
How improving single-autoclave yield rate and reducing cost also is a big problem in the synthetic field of ZSM-5, especially in the building-up process of high silica ZSM-5, because silica alumina ratio is than higher, when synthesizing with the silica-alumina gel system, the colloid viscosity is bigger, needed template consumption is also relatively large, otherwise the degree of crystallinity of product is lower.
The synthetic method that the purpose of this invention is to provide a kind of high silica ZSM-5 molecular sieve, the water yield that feeds intake when synthesizing to reduce improves single-autoclave yield rate, can make product reach higher degree of crystallinity when hanging down the template consumption simultaneously.
The synthetic method of high silica ZSM-5 molecular sieve provided by the present invention is to be the silicon source with the solid silicone, is the aluminium source with Tai-Ace S 150 or sodium metaaluminate, and (Q) is organic formwork agent with the alkyl amine organism, and preparing mole proportioning is SiO
2/ Al
2O
3=100～1000, H
2O/SiO
2=1～9.5, Na
2O/SiO
2=0.02～0.3, Q/SiO
2=0.02～0.5 reaction mixture is then with this reaction mixture hydrothermal crystallizing according to a conventional method.
The granularity of said solid silicone is 20～200 orders in the method provided by the present invention, and pore volume is 0.4ml/g at least.
Said template is that general formula is RNH in the method provided by the present invention
2Alkylamine, wherein R is C
1～C
6Alkyl.
The condition of said crystallization is that temperature is 110～220 ℃ in the method provided by the present invention, and the time is 8 hours to 10 days, and wherein preferred condition is that temperature is 130～200 ℃, and the time is 1～6 day.
In the method for synthesizing high-silicon ZSM-5 molecular sieve provided by the present invention, can be before crystallization with made reaction mixture in 20～105 ℃ of ageings 4～48 hours, preferably 30～90 ℃ of following ageings 8～24 hours.
The principle of the method for synthesizing high-silicon ZSM-5 molecular sieve provided by the present invention is that the employing solid silicone is a raw material, make liquid reactions material (organic formwork agent, aluminium source, alkali and water) on this solid surface, adsorb, the reaction while dissolving, concentrate effect by the surface, can reduce the water yield in the reaction system greatly, improve single still combined coefficient; In addition, the present invention can make product reach higher degree of crystallinity when hanging down the template consumption, and prior art is because the throwing water yield is bigger, its concentration is lower when the template consumption is low, the degree of crystallinity of product is also relatively low, increase degree of crystallinity and just need increase the template consumption, thereby so the present invention owing to throw the consumption that the reduction of the water yield also can further reduce organic formwork agent and reduce cost.In addition, adopt first low temperature maturation can make the degree of crystallinity of product higher during the method synthesizing high-silicon ZSM-5 molecular sieve of high temperature crystallization again according to the present invention.
X-ray diffraction (XRD) figure of the sample that Fig. 1 is synthesized for embodiment 1.
The following examples will the present invention is described further, but do not limit the present invention.In each embodiment and Comparative Examples, relative crystallinity be with product and standard specimen separately the ratio of the peak height sum of five the XRD diffraction peaks of 2 θ angles between 22.5～25 ° of X-ray diffraction (XRD) represent the sample that standard specimen herein (degree of crystallinity is decided to be 100%) is obtained for embodiment 1.
Each embodiment and Comparative Examples raw materials used except that other have dated, be commercially available chemically pure reagent.
Embodiment 1
With 10.5 grams, 80～120 purpose silochrom (SiO
2Content is 94%, and pore volume is 0.79ml/g, and silica gel factory in Qingdao produces, down with) with by 0.67 gram NaOH, 0.6 gram n-Butyl Amine 99,23 gram water and 0.56 gram Al
2(SO
4)
318H
2The solution that O formed mixes, and the mole proportioning of gained reaction mixture is:
SiO
2/ Al
2O
3=200, H
2O/SiO
2=7.8, Na
2O/SiO
2=0.05, n-Butyl Amine 99/SiO
2=0.05
Said mixture pack into reactor in 170 ℃ of crystallization 24 hours, and with the reactor cooling, product after filtration, after the washing, drying, identify to have the crystal phase structure (see figure 1) of ZSM-5 through XRD stipulated that its degree of crystallinity is 100%, product S iO after reaction finished
2/ Al
2O
3=165.
Embodiment 2
10.5 grams, 80～120 purpose silochroms and the ethylamine solution, 8 that by 1.34 gram NaOH, 5.4 gram concentration is 28 heavy % are restrained water and 1.1 gram Al
2(SO
4)
318H
2The solution that O formed mixes, and the mole proportioning of gained reaction mixture is:
SiO
2/ Al
2O
3=100, H
2O/SiO
2=4, Na
2O/SiO
2=0.1, ethamine/SiO
2=0.2
Said mixture pack into reactor in 170 ℃ of crystallization 40 hours, after reaction finishes with the reactor cooling, product after filtration, after the washing, drying, it is identical with Fig. 1 to record its XRD crystalline phase figure, relative crystallinity is 95%, product S iO
2/ Al
2O
3=65.
Embodiment 3
With 10.5 gram 40～120 purpose silochroms and by 0.67 gram NaOH, 1.8 gram n-Butyl Amine 99s, 11.5 gram water and 0.56 gram Al
2(SO
4)
318H
2The solution that O formed mixes, and the mole proportioning of gained reaction mixture is:
SiO
2/ Al
2O
3=200, H
2O/SiO
2=4, Na
2O/SiO
2=0.05, n-Butyl Amine 99/SiO
2=0.15
Said mixture pack into reactor in 120 ℃ of crystallization 7 days, after reaction finishes with the reactor cooling, product after filtration, after the washing, drying, it is identical with Fig. 1 to record its XRD crystalline phase figure, relative crystallinity is 110%, product S iO
2/ Al
2O
3=160.
Embodiment 4
With 10.5 grams, 80～120 purpose Kiselgel A (SiO
2Content is 94%, and pore volume is 0.50ml/g, and silica gel factory in Qingdao produces, down with) with by 2.07 gram NaOH, 2.4 gram n-Butyl Amine 99s, 24 gram water and 0.56 gram Al
2(SO
4)
318H
2The solution that O formed mixes, and the mole proportioning of gained reaction mixture is:
SiO
2/ Al
2O
3=200, H
2O/SiO
2=8, Na
2O/SiO
2=0.15, n-Butyl Amine 99/SiO
2=0.2
Said mixture pack into reactor in 170 ℃ of crystallization 50 hours, after reaction finishes with the reactor cooling, product after filtration, after the washing, drying, it is identical with Fig. 1 to record its XRD crystalline phase figure, relative crystallinity is 101%, product S iO
2/ Al
2O
3=170.
Embodiment 5
With 10.5 gram 80～120 purpose silochroms and by 0.67 gram NaOH, 2.4 gram n-Butyl Amine 99s, 11.5 gram water and 0.09 gram sodium metaaluminate (Al
2O
3Content is 45 heavy %) solution formed mixes, and the mole proportioning of gained reaction mixture is:
SiO
2/ Al
2O
3=414, H
2O/SiO
2=4, Na
2O/SiO
2=0.05, n-Butyl Amine 99/SiO
2=0.2
Said mixture pack into reactor in 170 ℃ of crystallization 20 hours, after reaction finishes with the reactor cooling, product after filtration, after the washing, drying, it is identical with Fig. 1 to record its XRD crystalline phase figure, relative crystallinity is 105%, product S iO
2/ Al
2O
3=340.
Embodiment 6
10.5 grams, 40～120 purpose Kiselgel As and the ethylamine solution and 4.0 solution formed of gram water that by 0.67 gram NaOH, 10.8 gram concentration are 28 heavy % are mixed, the mole proportioning of gained reaction mixture is for (aluminium is provided by the impurity aluminum in the silica gel, the impurity A l in the silica gel
2O
3Content is 0.27 heavy %):
SiO
2/ Al
2O
3=620, H
2O/SiO
2=4, Na
2O/SiO
2=0.05, n-Butyl Amine 99/SiO
2=0.4
Said mixture pack into reactor in 30 ℃ of ageings 24 hours, then in 140 ℃ of crystallization 48 hours, after reaction finishes with the reactor cooling, product after filtration, after the washing, drying, it is identical with Fig. 1 to record its XRD crystalline phase figure, relative crystallinity is 100%, product S iO
2/ Al
2O
3=560.
Embodiment 7
The proportioning of reaction mixture is identical with embodiment 1, different is crystallization condition changes into earlier with reaction mixture in 30 ℃ of ageings 10 hours, then 170 ℃ of following crystallization 16 hours, other steps are identical with embodiment 1, the XRD crystalline phase figure of products therefrom is identical with Fig. 1, relative crystallinity is 110%, product S iO
2/ Al
2O
3=160.
Embodiment 8
Repeat the step of embodiment 1, different is changes earlier with reaction mixture crystallization condition in 60 ℃ of ageings 8 hours into, and in 170 ℃ of crystallization 16 hours, the relative crystallinity of products therefrom was 120% then.
Embodiment 9
Repeat the step of embodiment 1, different is changes earlier with reaction mixture crystallization condition in 90 ℃ of ageings 16 hours into, is warming up to 140 ℃ of crystallization then 48 hours, and the relative crystallinity of products therefrom is 110%.
Comparative Examples 1
With 10.5 gram 80～120 purpose silochroms and by 0.67 gram NaOH, 0.69 gram n-Butyl Amine 99,88.6 gram water and 0.56 gram Al
2(SO
4)
318H
2The solution that O formed mixes, and the mole proportioning of gained reaction mixture is:
SiO
2/ Al
2O
3=200, H
2O/SiO
2=30, Na
2O/SiO
2=0.05, n-Butyl Amine 99/SiO
2=0.05
Said mixture pack into reactor in 170 ℃ of crystallization 24 hours, after reaction finishes with the reactor cooling, product after filtration, after the washing, drying, it is identical with Fig. 1 to record its XRD crystalline phase figure, degree of crystallinity is 75%, product S iO
2/ Al
2O
3=160.
Claims (7)
1. the synthetic method of a high silica ZSM-5 molecular sieve is characterized in that it is the silicon source that this method comprises with the solid silicone, is the aluminium source with Tai-Ace S 150 or sodium metaaluminate, and (Q) is template with the alkyl amine organism, and preparing mole proportioning is SiO
2/ Al
2O
3=100～1000, H
2O/SiO
2=1～9.5, Na
2O/SiO
2=0.02～0.3, Q/SiO
2=0.02～0.5 reaction mixture is then with this reaction mixture hydrothermal crystallizing according to a conventional method.
2. according to the method for claim 1, the granularity that it is characterized in that said solid silicone is 20～200 orders, and pore volume is at least 0.4 milliliter/gram.
3. according to the method for claim 1, it is characterized in that said template is that general formula is RNH
2Alkylamine, wherein R is C
1～C
6Alkyl.
4. according to the method for claim 1, the condition that it is characterized in that said crystallization is that temperature is 110～220 ℃, and the time is 8 hours to 10 days.
5. according to the method for claim 4, the condition that it is characterized in that said crystallization is that temperature is 130～200 ℃, and the time is 1～6 day.
6. according to the method for claim 1 or 4, it is characterized in that before said crystallization said reaction mixture in 20～105 ℃ of ageings 4～48 hours.
7. according to the method for claim 6, it is characterized in that before said crystallization said reaction mixture in 30～90 ℃ of ageings 8～24 hours.
Priority Applications (1)
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|---|---|---|---|
| CN97103679A CN1057066C (en) | 1997-03-31 | 1997-03-31 | Process for synthesizing high-silicon ZSM-5 molecular sieve |
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|---|---|---|---|
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| CN1194942A true CN1194942A (en) | 1998-10-07 |
| CN1057066C CN1057066C (en) | 2000-10-04 |
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|---|---|---|---|
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100364890C (en) * | 2005-06-14 | 2008-01-30 | 大连理工大学 | Synthesis method of fine grain ZSM-5 zeolite molecular sieve with high silicon aluminium ratio |
| CN100408181C (en) * | 2005-08-15 | 2008-08-06 | 中国石油化工股份有限公司 | Method for preparing catalyst of para xylene through form selected methylation of toluene |
| CN100408180C (en) * | 2005-08-15 | 2008-08-06 | 中国石油化工股份有限公司 | Method for preparing catalyst of para xylene through methylation of toluene |
| CN100457623C (en) * | 2005-10-26 | 2009-02-04 | 中国石油化工股份有限公司 | Preparation method of ZSM-5 zeolite molecular sieve |
| CN102009986A (en) * | 2010-09-29 | 2011-04-13 | 中国科学院广州能源研究所 | Method for co-production of zeolite molecular sieves, high-grade activated carbon and industrial alkali metal salt from wastes in biomass power plants |
| CN101559955B (en) * | 2008-04-17 | 2011-04-27 | 中国石油天然气集团公司 | Method of preparing ZSM-5 molecular sieves |
| CN112624145A (en) * | 2020-12-25 | 2021-04-09 | 南开大学 | Synthesis method of MFI molecular sieve nanosheet |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3702886A (en) * | 1969-10-10 | 1972-11-14 | Mobil Oil Corp | Crystalline zeolite zsm-5 and method of preparing the same |
| US4061724A (en) * | 1975-09-22 | 1977-12-06 | Union Carbide Corporation | Crystalline silica |
| US4526879A (en) * | 1978-11-13 | 1985-07-02 | Mobil Oil Corporation | Synthesis of zeolite ZSM-5 |
-
1997
- 1997-03-31 CN CN97103679A patent/CN1057066C/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100364890C (en) * | 2005-06-14 | 2008-01-30 | 大连理工大学 | Synthesis method of fine grain ZSM-5 zeolite molecular sieve with high silicon aluminium ratio |
| CN100408181C (en) * | 2005-08-15 | 2008-08-06 | 中国石油化工股份有限公司 | Method for preparing catalyst of para xylene through form selected methylation of toluene |
| CN100408180C (en) * | 2005-08-15 | 2008-08-06 | 中国石油化工股份有限公司 | Method for preparing catalyst of para xylene through methylation of toluene |
| CN100457623C (en) * | 2005-10-26 | 2009-02-04 | 中国石油化工股份有限公司 | Preparation method of ZSM-5 zeolite molecular sieve |
| CN101559955B (en) * | 2008-04-17 | 2011-04-27 | 中国石油天然气集团公司 | Method of preparing ZSM-5 molecular sieves |
| CN102009986A (en) * | 2010-09-29 | 2011-04-13 | 中国科学院广州能源研究所 | Method for co-production of zeolite molecular sieves, high-grade activated carbon and industrial alkali metal salt from wastes in biomass power plants |
| CN112624145A (en) * | 2020-12-25 | 2021-04-09 | 南开大学 | Synthesis method of MFI molecular sieve nanosheet |
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| Publication number | Publication date |
|---|---|
| CN1057066C (en) | 2000-10-04 |
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