Structural evolution and catalytic performance of DuPont V-P-O/SiO2 materials designed for fluidized bed applications

被引:19
作者
Dummer, Nicholas F. [1 ]
Weng, Weihao [2 ]
Kiely, Carol [2 ]
Carley, Albert F. [1 ]
Bartley, Jonathan K. [1 ]
Kiely, Christopher J. [2 ]
Hutchings, Graham J. [1 ]
机构
[1] Cardiff Univ, Cardiff Catalysis Inst, Sch Chem, Cardiff CF10 3AT, S Glam, Wales
[2] Lehigh Univ, Dept Mat Sci & Engn, Bethlehem, PA 18015 USA
基金
英国工程与自然科学研究理事会;
关键词
V-P-O catalyst; n-Butane oxidation; Maleic anhydride; XuM; Silica shell; N-BUTANE OXIDATION; VANADIUM PHOSPHATE CATALYSTS; PHOSPHORUS OXIDE CATALYSTS; P-O CATALYSTS; MALEIC-ANHYDRIDE; SELECTIVE OXIDATION; VPO CATALYSTS; SUPPORTED VPO; PYROPHOSPHATE;
D O I
10.1016/j.apcata.2009.10.004
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
An industrial V-P-O catalyst (DuPont), comprising vanadyl pyrophosphate crystallites encapsulated by a silica shell, has been investigated. Reaction evaluation for butane oxidation was conducted over (i) the catalyst precursor, (ii) the calcined precursor and (iii) equilibrated material (2 years on-line) in a fixed-bed reactor. Characterization was conducted on these three samples by XRD, SEM, TEM and XPS. The core-shell particles have also been examined with a novel X-ray ultramicroscopy (XuM) technique which reveals the internal structure without having to section the material. The microstructural and surface compositional changes that have occurred over the course of its industrial lifespan in a fluidized bed reactor are correlated with the catalytic activity measurements. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:47 / 55
页数:9
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