化学工业与工程
Home  |   |  About Journal  |  Editorial Board  |  Instruction  |  Subscriptions  |  Download  |  Publication Ethics  |  Contacts Us  |  Chinese
Chemcial Industry and Engineering 2003, Vol. 20 Issue (6) :425-428    DOI:
Article Current Issue | Next Issue | Archive | Adv Search << | >>
Catalytic Behavior of Fluidized-Bed Catalystfor Oxidation of n-Butane to Maleic Anhydride
WEN Yu-long,XU Wen(School of Chemical Engineering,Tianjin University,Tianjin 300072,China)
(School of Chemical Engineering,Tianjin University,Tianjin 300072,China

Abstract
Reference
Related Articles
Download: PDF (0KB)   HTML 0KB   Export: BibTeX or EndNote (RIS)      Supporting Info
Abstract The effects of orthophosphoric acid concentration in precursor preparation on the catalyst behavior have been studied.For the catalysts prepared at higher concentrations of acid,the quantity of V~(4+) phase (VO)_2P_2O_7 is quite large,and the n-butane conversions are all considerably high.With decreasing the acid concentration in precursor preparation,the relative amount of V~(5+) phase ��-VOPO_4 and the n-butane conversion increase continuously,whereas the selectivity to MA increases at beginning and then decreases after it reaches a maximum value.The catalyst prepared at the acid concentration of 95.0% gave the maximum yield of MA of 45.49% at an inlet n-butane concentration of 4.0% and a space velocity of 500h~(-1).
Service
Email this article
Add to my bookshelf
Add to citation manager
Email Alert
RSS
Articles by authors
Keywords��   
Received 2003-11-15; published 2003-11-15
Cite this article:   
WEN Yu-long,XU Wen.Catalytic Behavior of Fluidized-Bed Catalystfor Oxidation of n-Butane to Maleic Anhydride[J]  Chemcial Industry and Engineering, 2003,V20(6): 425-428
Copyright 2010 by Chemcial Industry and Engineering