CIESC Journal

• 催化、动力学与反应器 • 上一篇    下一篇

正丁烷氧化制顺酐流化床催化剂性能

许文;陈明鸣   

  1. 天津大学化工学院,天津 300072

  • 出版日期:2003-08-25 发布日期:2003-08-25

BEHAVIOR OF FLUIDIZED BED CATALYST FOR OXIDATION OF n-BUTANE TO MALEIC ANHYDRIDE

XU Wen;CHEN Mingming   

  • Online:2003-08-25 Published:2003-08-25

摘要: 实验考察了以正戊醇为还原剂的前驱体制备过程中磷酸浓度对催化剂性能的影响.在较高的磷酸浓度范围内制得的催化剂,V4+相(VO)2P2O7的量较大,正丁烷的转化率都较高.磷酸浓度减少,V5+δ-VOPO4的相对量逐渐增大,正丁烷的转化率随之升高,而对顺酐的选择性开始时升高,达到最大点后则逐渐降低.在最佳磷酸浓度101.7% 时制备出的催化剂,在进气丁烷浓度为4.0 %、空速为500h-1的反应条件下,顺酐的最高收率为47.67%(mol).

Abstract: The effects of orthophosphoric acid concentration in precursor preparation with n-pentanol as reductive agent on vanadium catalyst behavior were studied. For the catalysts prepared at higher concentrations of the acid, the quantity of V4+ phase (VO)2P2O7 is very large,and conversions of n-butane to maleic anhydride(MA)are all comparatively high. With decreasing acid concentration in precursor preparation, the relative amount of V5+ phase δ-VOPO4 and n-butane conversion increase continuously, whereas the selectivity to MA increases at the beginning and then decreases when it reaches a maximum value. The catalyst prepared at the optimal acid concentration of 101.7% gave the maximum yield of MA of 47.67 %(mol) at an inlet n-butane concentration of 4.0% and space velocity of 500 h-1.