Catalytic reduction of SO2 with CO over supported iron catalysts

被引:48
作者
Wang, Xuehai
Wang, Aiqin
Li, Ning
Wang, Xiaodong
Liu, Zhi
Zhang, Tao
机构
[1] Chinese Acad Sci, Dalian Inst Chem Phys, State Key Lab Catalysis, Dalian 116023, Peoples R China
[2] Chinese Acad Sci, Grad Sch, Beijing, Peoples R China
关键词
D O I
10.1021/ie0600947
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Iron oxides supported on several types of carriers (gamma-Al2O3, HZSM-5, SiO2, and MgO) were investigated for the catalytic reduction of SO2 by CO. The catalytic tests show that the activity of the catalysts followed the order Fe2O3/gamma-Al2O3 > Fe2O3 > HZSM-5 >> Fe2O3/SiO2 > Fe2O3/MgO. The X-ray diffraction analysis characterization of the presulfided catalysts revealed that FeS2 formation was greatly dependent on the acidic nature of the supports, with an evident FeS2 phase detected on both gamma-Al2O3 and HZSM-5, in contrast with Fe7S8 formed on SiO2 and MgO. Presulfidation with a reacting gas mixture above 500 degrees C was necessary for obtaining a high activity because of the formation of active-phase FeS2 during this process. The catalytic activity correlated well with the sulfidation degree of Fe2O3, which is mainly dependent on the acidic nature of the support and the choice of the presulfidation conditions. When the Fe content was at 20 wt %, under the optimal feed compositions (CO/SO2 = 2: 1), the Fe2O3/gamma-Al2O3 catalyst exhibited the best catalytic performance, with 99.31% SO2 conversion and a 99.17% sulfur yield obtained at 380 degrees C.
引用
收藏
页码:4582 / 4588
页数:7
相关论文
共 28 条
[1]   LANTHANUM OXYSULFIDE AS A CATALYST FOR THE OXIDATION OF CO AND COS BY SO2 [J].
BAGLIO, JA .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1982, 21 (01) :38-41
[2]  
CHEN CL, 2004, APPL CATAL B-ENVIRON, V55, P109
[3]   INFLUENCE OF PREPARATION CONDITIONS ON THE STRUCTURE AND CATALYTIC PROPERTIES OF SO42-/ZRO2 SUPERACID CATALYSTS [J].
CORMA, A ;
FORNES, V ;
JUANRAJADELL, MI ;
NIETO, JML .
APPLIED CATALYSIS A-GENERAL, 1994, 116 (1-2) :151-163
[4]   Acid-base properties and active site requirements for elimination reactions on alkali-promoted MgO catalysts [J].
Díez, VK ;
Apesteguía, CR ;
Di Cosimo, JI .
CATALYSIS TODAY, 2000, 63 (01) :53-62
[5]   Ceria-based catalysts for the recovery of elemental sulfur from SO2-laden gas streams [J].
Flytzani-Stephanopoulos, M ;
Zhu, TL ;
Li, Y .
CATALYSIS TODAY, 2000, 62 (2-3) :145-158
[6]   CATALYST EVALUATION FOR SIMULTANEOUS REDUCTION OF SULFUR-DIOXIDE AND NITRIC-OXIDE BY CARBON-MONOXIDE [J].
GOETZ, VN ;
SOOD, A ;
KITTRELL, JR .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1974, 13 (02) :110-114
[7]   KINETIC EVIDENCE OF A REACTIVE INTERMEDIATE IN REDUCTION OF SO2 WITH CO [J].
HAAS, LA ;
KHALAFALLA, SE .
JOURNAL OF CATALYSIS, 1973, 29 (02) :264-269
[8]   LANTHANUM TITANATE CATALYST - SULFUR-DIOXIDE REDUCTION [J].
HAPPEL, J ;
HNATOW, MA ;
BAJARS, L ;
KUNDRATH, M .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1975, 14 (03) :154-158
[9]   FLUE-GAS DESULFURIZATION - CATALYTIC REMOVAL OF SULFUR-DIOXIDE BY CARBON-MONOXIDE ON SULFIDED LA1-XSRXCOO3 .1. ADSORPTION OF SULFUR-DIOXIDE, CARBON-MONOXIDE AND THEIR MIXTURES [J].
HIBBERT, DB ;
CAMPBELL, RH .
APPLIED CATALYSIS, 1988, 41 (1-2) :273-287
[10]   FLUE-GAS DESULFURIZATION - CATALYTIC REMOVAL OF SULFUR-DIOXIDE BY CARBON-MONOXIDE ON SULFIDED LA1-XSRXCOO3 .2. REACTION OF SULFUR-DIOXIDE AND CARBON-MONOXIDE IN A FLOW SYSTEM [J].
HIBBERT, DB ;
CAMPBELL, RH .
APPLIED CATALYSIS, 1988, 41 (1-2) :289-299