๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

A Study of White-Spirit Vapor Combustion on Pt/Al2O3 Catalyst

โœ Scribed by C. Mihaela Manta; G. Bozga; G. Bercaru; C. Sorin Bildea


Publisher
John Wiley and Sons
Year
2011
Tongue
English
Weight
167 KB
Volume
34
Category
Article
ISSN
0930-7516

No coin nor oath required. For personal study only.

โœฆ Synopsis


Abstract

The objective of the work is to investigate the catalytic combustion of white spirit solvent vapors at low concentration in air, typical for depollution applications, on a commercial catalyst, Pt/ฮณโ€Al~2~O~3~ (0.5โ€‰wtโ€% Pt). To study the influence of the main variables on the process kinetics, experiments were performed under various operating conditions (temperature domain: 150โ€“350โ€‰ยฐC; flow rates: 125โ€“250โ€‰mLโ€‰min^โ€“1^; white spirit concentrations: 220โ€“260โ€‰ppmv). The stoichiometry and kinetics of the vapor combustion was described globally by using a pseudoโ€compound, representing the average molecular weight and the carbon/hydrogen ratio of the mixture. Experimental data were reasonably well correlated by a first order rate expression with respect to the apparent concentration of the lumping pseudoโ€component.


๐Ÿ“œ SIMILAR VOLUMES


Comparative study of aromatization selec
โœ Alfred A Susu ๐Ÿ“‚ Article ๐Ÿ“… 2008 ๐Ÿ› Wiley (John Wiley & Sons) ๐ŸŒ English โš– 245 KB ๐Ÿ‘ 1 views

## Abstract **BACKGROUND:** The metal dispersed over a support can be present as small crystallites with sizes less than 5 nm. The smaller crystallites favour aromatization while larger crystallites favour cracking/hydrogenolysis. Sintering results in the agglomerization of smaller metal crystallit

Effect of drying and calcination on the
โœ Dongfang Wu; Wei Jiang; Jiancheng Zhou ๐Ÿ“‚ Article ๐Ÿ“… 2010 ๐Ÿ› Wiley (John Wiley & Sons) ๐ŸŒ English โš– 268 KB

## Abstract **BACKGROUND:** This paper presents a mathematical modeling and factorial analysis of the toluene combustion activity of a cordierite monolith supported copperโ€“manganeseโ€“silver mixedโ€oxide catalyst in the drying and calcination processes, using response surface methodology. A central co