CN104607238B - A kind of composite catalyst containing modified montmorillonite used and ZSM-8 and preparation method thereof - Google Patents
A kind of composite catalyst containing modified montmorillonite used and ZSM-8 and preparation method thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 30
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical class O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- 239000002131 composite material Substances 0.000 title claims abstract description 5
- 229910052733 gallium Inorganic materials 0.000 claims abstract description 6
- CHPZKNULDCNCBW-UHFFFAOYSA-N gallium nitrate Chemical compound [Ga+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O CHPZKNULDCNCBW-UHFFFAOYSA-N 0.000 claims description 18
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000008367 deionised water Substances 0.000 claims description 9
- 229910021641 deionized water Inorganic materials 0.000 claims description 9
- 229940044658 gallium nitrate Drugs 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 8
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 6
- 239000012153 distilled water Substances 0.000 claims description 5
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 5
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 claims description 3
- 239000012265 solid product Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- 239000011230 binding agent Substances 0.000 abstract description 5
- 229910052725 zinc Inorganic materials 0.000 abstract description 4
- 150000004945 aromatic hydrocarbons Chemical class 0.000 abstract description 2
- 230000009849 deactivation Effects 0.000 abstract description 2
- 239000012188 paraffin wax Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 4
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
本发明提供了一种含改性蒙脱石和ZSM-8的复合催化剂及其制备方法,该催化剂采用了La改性蒙脱石作为粘结剂,同时采用了Ga和Zn改性的ZSM-8,由此得到的催化剂比现有技术中常规的催化剂具有更高的链烷烃转化率和更高的芳烃收率,且该催化剂的失活速率大大降低,使用寿命得到有效延长。The invention provides a composite catalyst containing modified montmorillonite and ZSM-8 and a preparation method thereof. The catalyst adopts La modified montmorillonite as a binder, and simultaneously uses Ga and Zn modified ZSM-8 The catalyst thus obtained has higher paraffin conversion rate and higher aromatic hydrocarbon yield than conventional catalysts in the prior art, and the deactivation rate of the catalyst is greatly reduced, and the service life is effectively extended.
Description
技术领域 technical field
本发明涉及一种包含ZSM-8和改性蒙脱石的催化剂组合物。 The present invention relates to a catalyst composition comprising ZSM-8 and modified montmorillonite.
背景技术 Background technique
将饱和低链烷烃转化成化工上可直接利用的芳烃一直是人们广泛关注的课题。过去的若干年中,先后开发出利用沸石基催化剂使轻烃芳构化制备芳烃的方法,然而轻烃在催化剂上转化为芳烃是一个涉及多种反应的复杂过程,催化活性、选择性的控制一直是该领域中关注的焦点。 The conversion of saturated low-alkanes into aromatics that can be directly used in chemical industry has been a subject of widespread concern. In the past several years, a method of aromatizing light hydrocarbons to aromatics using zeolite-based catalysts has been developed successively. However, the conversion of light hydrocarbons to aromatics on catalysts is a complex process involving multiple reactions. The control of catalytic activity and selectivity has always been the focus of attention in this field.
现有技术中已知的可以用作低级链烷烃转化为芳烃的催化剂中常采用含有稀土金属并任选地与合适的粘结剂粘结。氧化铝和氧化硅是这类催化剂中常用的粘结剂。此外,该类催化剂中常用沸石作为主要组分,对于沸石的改性主要通过浸渍、离子交换以及机械混合等方法将改性元素引入分子筛中。 Catalysts known in the prior art that can be used as catalysts for the conversion of lower paraffins to aromatics usually contain rare earth metals and are optionally bonded with a suitable binder. Alumina and silica are commonly used binders in such catalysts. In addition, zeolite is commonly used as the main component in this type of catalyst, and the modification of zeolite is mainly through impregnation, ion exchange, and mechanical mixing to introduce modifying elements into molecular sieves.
发明内容 Contents of the invention
本发明的目的是提供一种含改性蒙脱石和ZSM-8的复合催化剂组合物,该催化剂中使用了La改性的蒙脱石作为粘结剂,并结合了Ga和Zn改性的ZSM-8,由于采用了该特殊的组分,使催化剂具有良好的链烷烃转化率和良好的芳烃总收率。 The purpose of this invention is to provide a composite catalyst composition containing modified montmorillonite and ZSM-8, used La modified montmorillonite as binding agent in this catalyst, and combined Ga and Zn modified ZSM -8, due to the use of this special component, the catalyst has a good conversion rate of paraffins and a good total yield of aromatics.
为达到上述目的,本发明采用的技术方案是: In order to achieve the above object, the technical scheme adopted in the present invention is:
一种含改性蒙脱石和ZSM-8的复合催化剂制备方法,其特征在于,包含如下步骤: A method for preparing a composite catalyst containing modified montmorillonite and ZSM-8, characterized in that it comprises the steps:
a)La改性蒙脱石的制备:取0.20g硝酸镧,将其溶解于140ml去离子水中,将该溶液加热至70℃,而后加入15g粒度为500目的蒙脱石,持续搅拌30分钟,待蒙脱石分散开后,升温至110℃,在该温度下搅拌10h,过滤,用去离子水洗涤3次,干燥固体产物,将干燥后的固体粉末置于马弗炉中空气气氛中550℃焙烧5小时,得到La改性蒙脱石; a) Preparation of La-modified montmorillonite: Take 0.20 g of lanthanum nitrate, dissolve it in 140 ml of deionized water, heat the solution to 70 ° C, then add 15 g of montmorillonite with a particle size of 500 mesh, and continue stirring for 30 minutes. After the montmorillonite is dispersed, heat up to 110°C, stir at this temperature for 10h, filter, wash with deionized water for 3 times, dry the solid product, and place the dried solid powder in a muffle furnace in an air atmosphere for 550 ℃ roasting for 5 hours to obtain La modified montmorillonite;
b)Ga/Zn-ZSM-8的制备:取硝酸镓和硝酸锌溶于250ml的去离子水中,其中硝酸镓和硝酸锌的总重量为0.825g,搅拌溶解后备用;将ZSM-8分散在硝酸铵水溶液中,100℃下保持5小时,过滤后干燥,将干燥粉末15g加入上述硝酸镓和硝酸锌的溶液中,而后升温至100℃,恒温搅拌20小时,过滤并干燥固体物质,得到Ga和Zn改性的ZSM-8; b) Preparation of Ga/Zn-ZSM-8: Dissolve gallium nitrate and zinc nitrate in 250ml of deionized water, wherein the total weight of gallium nitrate and zinc nitrate is 0.825g, stir and dissolve for later use; disperse ZSM-8 in In the ammonium nitrate aqueous solution, keep at 100°C for 5 hours, filter and dry, add 15g of dry powder to the above solution of gallium nitrate and zinc nitrate, then raise the temperature to 100°C, stir at constant temperature for 20 hours, filter and dry the solid matter to obtain Ga and Zn-modified ZSM-8;
c)催化剂的制备:取质量比为3:1的Ga/Zn-ZSM-8和La改性蒙脱石,加入搅拌器中,而后加入适量硅溶胶和蒸馏水,打浆、过滤后干燥,450℃焙烧0.5h后,破碎过筛,取20-100目的颗粒作为催化剂成品。 c) Catalyst preparation: take Ga/Zn-ZSM-8 and La modified montmorillonite with a mass ratio of 3:1, add them to the mixer, then add appropriate amount of silica sol and distilled water, beat, filter and dry at 450°C After roasting for 0.5h, crush and sieve, and take 20-100 mesh particles as the finished catalyst.
所述步骤a)中的搅拌速率均为400转/分。 The stirring rate in the step a) is 400 rpm.
所述步骤b)中的升温速率均为10℃/分。 The heating rate in the step b) is 10°C/min.
所述步骤c)中的升温速率为10℃/分。 The heating rate in step c) is 10°C/min.
有益效果Beneficial effect
本发明由于采用了上述技术方案,与现有技术相比具有如下有益效果:本发明的催化剂采用了La改性蒙脱石作为粘结剂,同时采用了Ga和Zn改性的ZSM-8,由此得到的催化剂比现有技术中常规的催化剂具有更高的链烷烃转化率和更高的芳烃收率,且该催化剂的失活速率大大降低,使用寿命得到有效延长。 Compared with the prior art, the present invention has the following beneficial effects due to the adoption of the above-mentioned technical scheme: the catalyst of the present invention adopts La modified montmorillonite as the binding agent, and simultaneously adopts Ga and Zn modified ZSM-8, The catalyst thus obtained has higher paraffin conversion rate and higher aromatic hydrocarbon yield than conventional catalysts in the prior art, and the deactivation rate of the catalyst is greatly reduced, and the service life is effectively extended.
具体实施方式 Detailed ways
下面通过实施例对本发明作进一步说明。 Below by embodiment the present invention will be further described.
实施例1Example 1
La改性蒙脱石的制备:取0.20g硝酸镧,将其溶解于140ml去离子水中,将该溶液加热至70℃,而后加入15g粒度为500目的蒙脱石,持续搅拌30分钟,搅拌速率为400转/分,待蒙脱石分散开后,升温至110℃,在该温度下搅拌10h,搅拌速率为400转/分,过滤,用去离子水洗涤3次,干燥固体产物,将干燥后的固体粉末置于马弗炉中空气气氛中550℃焙烧5小时,得到La改性蒙脱石; Preparation of La modified montmorillonite: Take 0.20g of lanthanum nitrate, dissolve it in 140ml of deionized water, heat the solution to 70°C, then add 15g of montmorillonite with a particle size of 500 mesh, and continue to stir for 30 minutes. After the montmorillonite is dispersed, raise the temperature to 110°C, stir at this temperature for 10 h at a stirring rate of 400 rpm, filter, wash 3 times with deionized water, dry the solid product, and dry The final solid powder is placed in a muffle furnace in an air atmosphere at 550° C. for 5 hours and calcined to obtain La modified montmorillonite;
Ga/Zn-ZSM-8的制备:取硝酸镓和硝酸锌溶于250ml的去离子水中,其中硝酸镓和硝酸锌的总重量为0.825g,搅拌溶解后备用;将ZSM-8分散在硝酸铵水溶液中,升温速率10℃/分,100℃下保持5小时,过滤后干燥,将干燥粉末15g加入上述硝酸镓和硝酸锌的溶液中,而后升温至100℃,升温速率10℃/分,恒温搅拌20小时,过滤并干燥固体物质,得到Ga和Zn改性的ZSM-8; Preparation of Ga/Zn-ZSM-8: Dissolve gallium nitrate and zinc nitrate in 250ml of deionized water, wherein the total weight of gallium nitrate and zinc nitrate is 0.825g, stir and dissolve for later use; disperse ZSM-8 in ammonium nitrate In the aqueous solution, the heating rate is 10°C/min, kept at 100°C for 5 hours, filtered and dried, and 15g of dry powder is added to the above solution of gallium nitrate and zinc nitrate, and then the temperature is raised to 100°C, the heating rate is 10°C/min, constant temperature Stir for 20 hours, filter and dry the solid matter to obtain Ga and Zn modified ZSM-8;
催化剂的制备:取质量比为3:1的Ga/Zn-ZSM-8和La改性蒙脱石,加入搅拌器中,而后加入适量硅溶胶和蒸馏水,打浆、过滤后干燥,升温速率10℃/分,450℃焙烧0.5h后,破碎过筛,取20-100目的颗粒作为催化剂成品。 Catalyst preparation: Take Ga/Zn-ZSM-8 and La modified montmorillonite with a mass ratio of 3:1, add them to the mixer, then add appropriate amount of silica sol and distilled water, beat, filter and dry, the heating rate is 10°C After roasting at 450°C for 0.5h, crush and sieve, and take 20-100 mesh particles as the finished catalyst.
对比例1Comparative example 1
取质量比为3:1的实施例1制备的Ga/Zn-ZSM-8和普通粘土,加入搅拌器中,而后加入适量硅溶胶和蒸馏水,打浆、过滤后干燥,以升温速率10℃/分升至450℃,焙烧0.5h后,破碎过筛,取20-100目的颗粒作为催化剂成品。 Take the Ga/Zn-ZSM-8 and ordinary clay prepared in Example 1 with a mass ratio of 3:1, add them to the mixer, and then add an appropriate amount of silica sol and distilled water, beat, filter, and dry, at a heating rate of 10°C/min Raise to 450°C, roast for 0.5h, crush and sieve, and take 20-100 mesh particles as the finished catalyst.
对比例2Comparative example 2
取质量比为3:1的ZSM-8和La改性蒙脱石,加入搅拌器中,而后加入适量硅溶胶和蒸馏水,打浆、过滤后干燥,以升温速率10℃/分升至450℃,焙烧0.5h后,破碎过筛,取20-100目的颗粒作为催化剂成品。 Take ZSM-8 and La modified montmorillonite with a mass ratio of 3:1, add them to the mixer, then add appropriate amount of silica sol and distilled water, beat, filter and dry, and raise the temperature to 450°C at a heating rate of 10°C/min. After roasting for 0.5h, crush and sieve, and take 20-100 mesh particles as the finished catalyst.
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