Zobrazeno 1 - 6
of 6
pro vyhledávání: '"Kelfin M. Hardiman"'
Publikováno v:
Chemical Engineering Journal. 143:273-281
H2 recovery from large quantities of toxic H2S, the by-product of various minerals, coal and petroleum processing operations is an attractive proposition for efficient resource and energy utilization. This study has examined the analysis of a double-
Autor:
Tuan-Huy Nguyen, Adesoji A. Adesina, Tomasz Safinski, Cyrus G. Cooper, Kelfin M. Hardiman, Frank P. Lucien, Y.J. Lee
Publikováno v:
Catalysis Today. 131:255-261
An evaluative investigation of the Fischer–Tropsch performance of two catalysts (20%Co/Al2O3 and 10%Co:10%Mo/Al2O3) has been carried out in a slurry reactor at 2 MPa and 220–260 °C. The addition of Mo to the Co-catalyst significantly increased t
Publikováno v:
Chemical Engineering Science. 61:2565-2573
The physicochemical properties of used catalysts obtained from propane steam reforming under steam-to-carbon (S:C) of 0.8 and 1.6 at operating temperatures of 773–873 K were investigated using BET, H 2 chemisorption, total organic carbon (TOC) cont
Publikováno v:
Chemical Engineering Journal. 102:119-130
Although the catalytic steam reforming of hydrocarbon for synthesis gas production is often carried out with excess steam-to-carbon ratio (S:C>3), on-line catalyst deactivation due to coking invariably affects reformer performance. It is therefore ne
Publikováno v:
Industrial & Engineering Chemistry Research. 43:6006-6013
The effect of major preparation variables on the innate characteristics of an alumina-supported Co−Ni catalyst system has been examined via a factorial design. Both calcination temperature and time...