Zeolite catalyzed Friedel-Crafts reactions were examined using acetic anhydride as an acetylating agent and an acetic acid as a solvent. It revealed that the reaction of anisole smoothly occurred quantitatively for 3 ...Zeolite catalyzed Friedel-Crafts reactions were examined using acetic anhydride as an acetylating agent and an acetic acid as a solvent. It revealed that the reaction of anisole smoothly occurred quantitatively for 3 h using mordenite zeolite with SiO2/Al2O3 = 200, and with SiO2/Al2O3 = 110, the increasing of Br?nsted acidity allowed to completely react within 2 h. Furthermore the selectivity of 4-methoxyacetophenone (4-MA) among the isomers was found to be quantitative, no by-products and/or isomers were not detectable. With the excellent recyclability and reusability, the mordenite zeolite exhibited at least 30 times quantitatively both conversion of anisole and selectivity of 4-MA. The mordenite catalysts of fresh and the used after 30 times were characterized. This opportunity obviously indicates the sufficient shape selective catalyst of mordenite zeolite and gives a green synthetic tool for heterogeneous acylation reaction.展开更多
以高硅(n(Si O2)/n(Al2O3)=373)HZSM-5分子筛为母体,采用浸渍法制备了一系列NH4F/Pt复合改性催化剂(w2)Pt-(w1)F-ZSM-5,以4-甲基联苯(4-MBP)与甲醇的烷基化为探针反应,考察了NH4F用量、Pt用量、NH4F改性后盐酸洗涤以及向反应体系添加水...以高硅(n(Si O2)/n(Al2O3)=373)HZSM-5分子筛为母体,采用浸渍法制备了一系列NH4F/Pt复合改性催化剂(w2)Pt-(w1)F-ZSM-5,以4-甲基联苯(4-MBP)与甲醇的烷基化为探针反应,考察了NH4F用量、Pt用量、NH4F改性后盐酸洗涤以及向反应体系添加水蒸气对反应的影响。结果表明,经复合改性后,0.75Pt-HCl-5F-ZSM-5催化剂用于4-MBP甲基化反应,其稳定性及二甲基联苯(DMBPs)的产率得到明显提高,反应2 h DMBPs产率为9.6%,反应20 h后,4-MBP转化率为9.1%,4,4’-DMBP选择性可达76.1%。而未改性HZSM-5催化剂上,反应2 h DMBPs产率为4.2%。向反应体系添加水蒸气可进一步提高(w2)Pt-(w1)F-ZSM-5催化剂的稳定性和4,4’-DMBP选择性,反应30 h 4,4’-DMBP选择性仍高达90%。展开更多
Toluene was alkylated with methanol in a flow type reactor at temperatures between 300 and 500 °C using H-ZSM-5 zeolite, 0.2%Pt/H-ZSM-5 and hydrofluorinated 0.2%Pt/H-ZSM-5 with HF concentrations of 1.0%, 2.0%, 3....Toluene was alkylated with methanol in a flow type reactor at temperatures between 300 and 500 °C using H-ZSM-5 zeolite, 0.2%Pt/H-ZSM-5 and hydrofluorinated 0.2%Pt/H-ZSM-5 with HF concentrations of 1.0%, 2.0%, 3.0%, or 4.0%. Pt primarily enhances toluene conversion, total xylenes production, and p-xylene relative to its thermodynamic equilibrium. As the concentration of HF increases from 1.0% to 3.0%, the catalyst activity increases because of the increase in the number of acid sites and their strength. Additionally, the surface area and Pt dispersion also increases. An advantage of increased HF doping is that the formation of voluminous trimethylbenzene (TMB) byproducts is inhibited. However, at a HF concentration of 4.0%, Al and Si are partially leached and then deposited mostly in the wider catalytic pores. This was determined by evaluating the pore volume distribution and we determined that reactivity inhibition was ob-viously present and was due to diffusion restriction.展开更多
文摘Zeolite catalyzed Friedel-Crafts reactions were examined using acetic anhydride as an acetylating agent and an acetic acid as a solvent. It revealed that the reaction of anisole smoothly occurred quantitatively for 3 h using mordenite zeolite with SiO2/Al2O3 = 200, and with SiO2/Al2O3 = 110, the increasing of Br?nsted acidity allowed to completely react within 2 h. Furthermore the selectivity of 4-methoxyacetophenone (4-MA) among the isomers was found to be quantitative, no by-products and/or isomers were not detectable. With the excellent recyclability and reusability, the mordenite zeolite exhibited at least 30 times quantitatively both conversion of anisole and selectivity of 4-MA. The mordenite catalysts of fresh and the used after 30 times were characterized. This opportunity obviously indicates the sufficient shape selective catalyst of mordenite zeolite and gives a green synthetic tool for heterogeneous acylation reaction.
文摘以高硅(n(Si O2)/n(Al2O3)=373)HZSM-5分子筛为母体,采用浸渍法制备了一系列NH4F/Pt复合改性催化剂(w2)Pt-(w1)F-ZSM-5,以4-甲基联苯(4-MBP)与甲醇的烷基化为探针反应,考察了NH4F用量、Pt用量、NH4F改性后盐酸洗涤以及向反应体系添加水蒸气对反应的影响。结果表明,经复合改性后,0.75Pt-HCl-5F-ZSM-5催化剂用于4-MBP甲基化反应,其稳定性及二甲基联苯(DMBPs)的产率得到明显提高,反应2 h DMBPs产率为9.6%,反应20 h后,4-MBP转化率为9.1%,4,4’-DMBP选择性可达76.1%。而未改性HZSM-5催化剂上,反应2 h DMBPs产率为4.2%。向反应体系添加水蒸气可进一步提高(w2)Pt-(w1)F-ZSM-5催化剂的稳定性和4,4’-DMBP选择性,反应30 h 4,4’-DMBP选择性仍高达90%。
文摘Toluene was alkylated with methanol in a flow type reactor at temperatures between 300 and 500 °C using H-ZSM-5 zeolite, 0.2%Pt/H-ZSM-5 and hydrofluorinated 0.2%Pt/H-ZSM-5 with HF concentrations of 1.0%, 2.0%, 3.0%, or 4.0%. Pt primarily enhances toluene conversion, total xylenes production, and p-xylene relative to its thermodynamic equilibrium. As the concentration of HF increases from 1.0% to 3.0%, the catalyst activity increases because of the increase in the number of acid sites and their strength. Additionally, the surface area and Pt dispersion also increases. An advantage of increased HF doping is that the formation of voluminous trimethylbenzene (TMB) byproducts is inhibited. However, at a HF concentration of 4.0%, Al and Si are partially leached and then deposited mostly in the wider catalytic pores. This was determined by evaluating the pore volume distribution and we determined that reactivity inhibition was ob-viously present and was due to diffusion restriction.
