Kinetic study of high-temperature removal of H2S by novel metal oxide sorbents

被引:44
作者
Garcia, E
Cilleruelo, C
Ibarra, JV
Pineda, M
Palacios, JM
机构
[1] CSIC,INST CARBOQUIM,ZARAGOZA 50015,SPAIN
[2] CSIC,INST CATALISIS & PETR QUIM,MADRID 28049,SPAIN
关键词
D O I
10.1021/ie960194k
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The behavior of different mixed oxides, including zinc titanates (ZT) and zinc ferrites modified with CuO (ZFC) or TiO2 (ZFT), as hot gas desulfurizing sorbents was investigated. The sorbents were prepared by calcination at 650 degrees C of a mixture of bulk oxides in three different stoichiometries in order to form new phases and modify their textural properties. Tests of stability against reduction were obtained by thermoprogrammed reduction, and kinetic studies of the sulfidation reaction were carried out in a thermobalance in the temperature range of 550-650 degrees C. Kinetic parameters of the intrinsic reaction were obtained assuming a grain model. The sulfidation behavior of the sorbents as extrudates was investigated in a fixed-bed reactor in terms of breakthrough curves. Fresh and sulfided samples were characterized by Hg porosimetry, X-ray diffraction, and SEM-EDX. The study shows that the addition of TiO2 or CuO to zinc ferrite based sorbents calcined at 650 degrees C has little effect on the stability against reduction but markedly influences their textural properties. The stabilizing effect of Ti is observed in samples calcined at higher temperature or in non-iron-containing sorbents. The calculated kinetic constants indicate that the Zn content and the incorporation of Cu have an enhancing effect on the kinetics of the sulfidation process. Including H-2 in the feed gas decreases the reactivity and increases the activation energy. Extrudated sorbents showed a good performance as desulfurizing agents and maintained the H2S concentration in the outlet gas below 20 ppm. ZT sorbent exhibited a poor efficiency, which makes the addition of Ti questionable.
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页码:846 / 853
页数:8
相关论文
共 15 条
[1]  
CILLERUELO C, 1995, COAL SCI, V2, P1883
[2]  
FLYTZANISTEPHAN.M, 1990, PREPR PAP AM CHEM SO, V35, P77
[3]   HIGH-TEMPERATURE DESULFURIZATION USING ZINC FERRITE - REDUCTION AND SULFIDATION KINETICS [J].
FOCHT, GD ;
RANADE, PV ;
HARRISON, DP .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (11) :3005-3013
[4]   DEVELOPMENT OF ZINC FERRITE SORBENTS FOR DESULFURIZATION OF HOT COAL-GAS IN A FLUID-BED REACTOR [J].
GUPTA, R ;
GANGWAL, SK ;
JAIN, SC .
ENERGY & FUELS, 1992, 6 (01) :21-27
[5]  
GUPTA R, 1993, AICHE ANN M S GAS PU
[6]  
Levenspiel O, 1988, CHEM REACTION ENG
[7]   HIGH-TEMPERATURE H2S REMOVAL FROM FUEL GASES BY REGENERABLE ZINC-OXIDE TITANIUM-DIOXIDE SORBENTS [J].
LEW, S ;
JOTHIMURUGESAN, K ;
FLYTZANI-STEPHANOPOULOS, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (05) :535-541
[8]   THE REDUCTION OF ZINC TITANATE AND ZINC-OXIDE SOLIDS [J].
LEW, S ;
SAROFIM, AF ;
FLYTZANI-STEPHANOPOULOS, M .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (06) :1421-1431
[9]   DESULFURIZATION OF HOT COAL-GAS IN FLUIDIZED-BED WITH REGENERABLE ZINC TITANATE SORBENTS [J].
MOJTAHEDI, W ;
SALO, K ;
ABBASIAN, J .
FUEL PROCESSING TECHNOLOGY, 1994, 37 (01) :53-65
[10]   Kinetic behaviour and reactivity of zinc ferrites for hot gas desulphurization [J].
Pineda, M ;
Fierro, JLG ;
Palacios, JM ;
Cilleruelo, C ;
Ibarra, JV .
JOURNAL OF MATERIALS SCIENCE, 1995, 30 (24) :6171-6178