Zobrazeno 1 - 10
of 41
pro vyhledávání: '"R. R. HUDGINS"'
Autor:
P. L. Silveston, R. R. Hudgins
This comprehensive review, prepared by 24 experts, many of whom are pioneers of the subject, brings together in one place over 40 years of research in this unique publication. This book will assist R & D specialists, research chemists, chemical engin
Autor:
P. L. Silveston and, R. R. Hudgins
Publikováno v:
Industrial & Engineering Chemistry Research. 36:2884-2884
Publikováno v:
Chemical Engineering & Technology; May2005, Vol. 28 Issue 5, p581-586, 6p
Publikováno v:
The Canadian Journal of Chemical Engineering. 63:86-92
Publikováno v:
Water Science and Technology. 14:1510-1513
Experiments on a 4-ft (1.2-m) diameter model circular clarifier operating at overflow rates and suspension concentrations corresponding to municipal treatment practice show that baffles designed to function as wave traps suppress low-frequency, large
Autor:
R. R. Hudgins, P. L. Silveston
Publikováno v:
Catalysis Reviews. 11:167-196
Our purpose is to review current and past research on the unusual influence of inert, diluent gases on the observed rate of heterogeneous and catalytic reactions. This is a subject that has received little attention in the literature since Forestier'
Autor:
R. R. Hudgins, P. L. Silveston
Publikováno v:
Water Quality Research Journal. 9:282-293
A study was made of the wet air oxidation of eight Ontario sludges containing phosphates. Sludges were obtained from primary or secondary clarifiers in which lime, ferric chloride, or alum had been used to precipitate phosphates. A further set of slu
Publikováno v:
Canadian Journal of Chemistry. 48:1175-1182
A study was made of the influence of diluent gases on the reaction rate and activation energy of the oxidation of sulfur dioxide over vanadium pentoxide catalyst, an effect noted by Baron, Manning, and Johnstone in 1952. Results confirmed the occurre
Publikováno v:
Canadian Journal of Chemistry. 47:323-329
Isomerization runs were performed in a micro-reactor at 325 °C over a range of butene partial pressure of 84 to 763 mm Hg and at a total pressure of approximately 1 atm. The isomerization rate of 1-butene passed through a maximum with increasing 1-b
Publikováno v:
The Canadian Journal of Chemical Engineering. 41:220-225
The kinetics of the vapor-phase oxidation of benzene over a sulphate-promoted vanadium oxide catalyst were studied in a differential flow-reactor. Rates of oxidation of benzene were measured at temperatures in the range 324° to 400°C., for benzene