聚碳酸酯连续熔融酯交换过程的反应闪蒸模拟

A model of the continuous melt transesterification process of bisphenol-A and diphenyl carbonate in a continuous stirred tank reactor to produce polycarbonate is presented. The model is developed by using the molecular species model of polycarbonate melt polycondensation and the modeling method of reactive flash. Liquid phase is treated as perfect mixed flow and the vapor phase is assumed following the ideal gas law. With this model, the continuous melt transesterification process of bisphenol-A and diphenyl carbonate is examined with respect to different orocess parameters.     

制氢装置用深度脱硫剂的开发

针对大型制氢装置原料天然气中含硫的新要求,通过实验室试验和工业试应用,开发出一种深度脱硫剂产品。该深度脱硫剂在(330~380)℃和空速不大于2 000 h~(-1)条件下,与有机硫加氢催化剂配套使用,可将气体中的总硫净化度由100×10~(-9)提高至低于20×10~(-9)的水平。     

碱改性对甲醇芳构化催化剂Zn/La-HZSM-5性能的影响

采用碱处理对Zn/La-HZSM-5分子筛进行改性,调变分子筛的酸性和择形性能,评价其在甲醇芳构化反应中的性能。采用N_2低温吸附-脱附、NH_3-TPD和XRD等方法表征催化剂。结果表明,碱处理的Zn/La-HZSM-5分子筛催化剂孔体积和比表面积增加,酸量碱处理后降低,Zn改性后增加,催化剂的催化性能显著改善。0.3 mol·L~(-1 )NaOH溶液处理的Zn/La-HZSM-5分子筛催化剂在0.1 Mpa、TOS=10 h、WHSV=0.8 h~(-1)、437℃的反应条件下轻质芳烃收率41.82%,具有较高的芳烃收率和反应稳定性。