IRON CATALYST DEACTIVATION BY CARBON DEPOSITION FROM SYNTHESIS GAS.

Item

Title
IRON CATALYST DEACTIVATION BY CARBON DEPOSITION FROM SYNTHESIS GAS.
Identifier
AAI8601637
identifier
8601637
Creator
FERNANDEZ-RAONE, ELVIO DANIEL.
Contributor
Alberto LaCava
Date
1985
Language
English
Publisher
City University of New York.
Subject
Engineering, Chemical
Abstract
The kinetics of C deposition and CO(,2) formation from CO over Fe powders, foils and supported pellets was studied at temperatures ranging from 250 to 450 C, using a microbalance tubular flow reactor. Carbon deposition proceeds at constant rates over all catalysts. The dependence of the rates on the CO partial pressure seems to follow a zero order power law kinetics in the range of study. Arrhenius plots show the activation energies for the rates of deposition and formation to be 31-32 Kcal/gmol.;The kinetics of carbon gasification with H(,2), from C deposited on Fe supported pellets was studied on the same system, at temperatures in the range 350-450 C. CH(,4) was the only detectable gaseous product. Constant rates of C gasification and CH(,4) formation could be maintained for 2 to 3 days of continuous operation. Activation energies of 48 Kcal/gmol were obtained for both reactions.;Deactivation of commercial iron pellets by C deposition from pure CO was studied in the range 280 to 320 C. After an initial deactivation process, constant rates of deposition were achieved through filamentous growths. A pore blocking mechanism seems to explain the behaviour of these catalysts for the C deposition reaction.;Non-porous iron pellets were deactivated by C deposition (300-350 C) from pure CO and regenerated by hydrogenation (370-415 C). Both reactions behave similarly. An initial constant high rate is followed by deactivation and a much lower constant final rate. This can be explained by assuming an uneven patch-like iron distribution on the pellet surface.;C deposits from pure CO were readily gasified to methane from porous and non-porous pellets. The order of reaction with respect to hydrogen partial pressure appears to be 1. This seems to be consistent with a mechanism in which the formation of a CH(,2)M group is the rate limiting step.;Hydrogen increases the rate of C formation from pure CO. The order of reaction with respect to the hydrogen partial pressure varies with the hydrogen partial pressure.
Type
dissertation
Source
PQT Legacy CUNY.xlsx
degree
Ph.D.
Program
Engineering
Item sets
CUNY Legacy ETDs