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
The utilization of CO2 as raw material for chemical synthesis has the potential for substantial economic and green benefits. Thermal decomposition of hexamethylene-1,6-dicarbamate （HDC） is a promising approach for i...The utilization of CO2 as raw material for chemical synthesis has the potential for substantial economic and green benefits. Thermal decomposition of hexamethylene-1,6-dicarbamate （HDC） is a promising approach for indirect utilization of CO2 to produce hexamethylene-1,6-diisocyanate （HDI）. In this work, a green route was developed for the synthesis of HD1 by thermal decomposition of HDC over Co3O4/ZSM-5 catalyst, using chlorobenzene as low boiling point solvent. Different metal oxide supported catalysts were prepared by incipient wetness impregnation （IWI）, PEG-additive （PEG） and deposition precipitation with ammonia evaporation （DP） methods. Their catalytic performances for the thermal decomposition of HDC were tested. The catalyst screening results showed that Co3O4/ZSM-525 catalysts prepared by different methods showed different performances in the order of Co3O4/ZSM-5 25（PEG） 〉 Co3O4/ZSM-525（IWI） 〉 Co3O4/ZSM-525（DP）. The physicochemical properties of Co3O4/ZSM- 52s catalyst were characterized by XRD, FTIR, N2 adsorption-desorption measurements, NH3-TPD and XPS. The superior catalytic performance of Co3O4/ZSM-52S（PEG） catalyst was attributed to its relative surface content of Co3 ＋, surface lattice oxygen content and total acidity. Under the optimized reaction conditions： 6.5% HDC concentration in chlorobenzene, 1 wt% Co3O4/ZSM-525（PEG） catalyst, 250℃ temperature, 2.5 h time, 800 ml.min 1 nitrogen flow rate and 1.0 MPa pressure, the HDC conversion and HDI yield could reach 100% and 92.8% respectively. The Co3O4/ZSM-525（PEG） catalyst could be facilely separated from the reaction mixture, and reused without degradation in catalytic performance. Furthermore, a possible reaction mechanism was proposed based on the physicochemical properties of the Co3O4/ZSM-5 25 catalysts.展开更多
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%。
基金National Natural Science Foundation of China(21476244 and 21406245)Youth Innovation Promotion Association CAS
文摘The utilization of CO2 as raw material for chemical synthesis has the potential for substantial economic and green benefits. Thermal decomposition of hexamethylene-1,6-dicarbamate （HDC） is a promising approach for indirect utilization of CO2 to produce hexamethylene-1,6-diisocyanate （HDI）. In this work, a green route was developed for the synthesis of HD1 by thermal decomposition of HDC over Co3O4/ZSM-5 catalyst, using chlorobenzene as low boiling point solvent. Different metal oxide supported catalysts were prepared by incipient wetness impregnation （IWI）, PEG-additive （PEG） and deposition precipitation with ammonia evaporation （DP） methods. Their catalytic performances for the thermal decomposition of HDC were tested. The catalyst screening results showed that Co3O4/ZSM-525 catalysts prepared by different methods showed different performances in the order of Co3O4/ZSM-5 25（PEG） 〉 Co3O4/ZSM-525（IWI） 〉 Co3O4/ZSM-525（DP）. The physicochemical properties of Co3O4/ZSM- 52s catalyst were characterized by XRD, FTIR, N2 adsorption-desorption measurements, NH3-TPD and XPS. The superior catalytic performance of Co3O4/ZSM-52S（PEG） catalyst was attributed to its relative surface content of Co3 ＋, surface lattice oxygen content and total acidity. Under the optimized reaction conditions： 6.5% HDC concentration in chlorobenzene, 1 wt% Co3O4/ZSM-525（PEG） catalyst, 250℃ temperature, 2.5 h time, 800 ml.min 1 nitrogen flow rate and 1.0 MPa pressure, the HDC conversion and HDI yield could reach 100% and 92.8% respectively. The Co3O4/ZSM-525（PEG） catalyst could be facilely separated from the reaction mixture, and reused without degradation in catalytic performance. Furthermore, a possible reaction mechanism was proposed based on the physicochemical properties of the Co3O4/ZSM-5 25 catalysts.
