Effect of H2S in syngas on the Fischer-Tropsch synthesis performance of a precipitated iron catalyst

被引:17
|
作者
Ma, Wenping [1 ]
Jacob, Gary [1 ]
Sparks, Dennis E. [1 ]
Shafer, Wilson D. [1 ]
Hamdeh, Hussein H. [2 ]
Hopps, Shelley D. [1 ]
Pendyala, Venkat Ramana Rao [1 ]
Hu, Yongfeng [3 ]
Xiao, Qunfeng [3 ]
Davis, Burtron H. [1 ]
机构
[1] Univ Kentucky, Ctr Appl Energy Res, 2540 Res Pk Dr, Lexington, KY 40511 USA
[2] Wichita State Univ, Dept Phys, 1845 Fairmount, Wichita, KS 67260 USA
[3] Canadian Light Source Inc, 44 Innovat Blvd, Saskatoon, SK S7N 2V3, Canada
基金
加拿大健康研究院; 加拿大创新基金会; 加拿大自然科学与工程研究理事会;
关键词
Fischer-Tropsch synthesis; Fe catalyst; XTL; Slurry phase reactor; H2S; Mossbauer spectroscopy; XANES; XRD; TRANSPORTATION FUELS; SULFUR; BIOMASS;
D O I
10.1016/j.apcata.2015.12.035
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The sulfur limit, the relationship between the sulfur added and the surface Fe atoms lost (Fe/S), and mechanism of sulfur poisoning were studied using an iron Fischer-Tropsch synthesis (FTS) catalyst (100 Fe/5.1 Si/2.0Cu/3.0K). The FTS reaction was carried out at 230-270 degrees C, 13 MPa, H-2/CO = 0.67-0.77 and 30-70% CO conversion using a 1-L slurry phase reactor. The used Fe catalysts were characterized by XRD, Mossbauer spectroscopy and XANES spectroscopy to understand the deactivation mechanism of the Fe based catalyst after adding up to 1 ppm H2S in the feed. Co-feeding of 0.1 ppm H2S in syngas for 70 h caused a very small change in the activity of the Fe catalyst, but increasing the H2S level to 0.2 ppm or above resulted in measurable deactivation of the Fe catalyst over a similar time period. The limit of sulfur level in the syngas feed (sensitivity) was determined to be 50 ppb. The added sulfur improved the selectivities of the secondary reactions of olefins and the WGS reaction even though the rates for these declined. The addition of H2S decreased CH4 selectivity and increased C5+ selectivities of the Fe catalyst. The Fe/S ratio, which can be used to define the poisoning ability of sulfur for the iron catalyst, was quantified based on the deactivation data obtained. The Fe/S ratio strongly depended on temperature and decreased remarkably with increasing temperature. At 270 degrees C one sulfur atom was found to eliminate similar to 6 surface Fe atoms, and the ratio increased to 7.2 at 260 degrees C and increased further to 13.5 at 230 degrees C. The Fe/S relationship with increasing temperature is in good agreement with sulfur sorption theory. The changes in FTS and WGS rates of the Fe catalyst by sulfur were also studied. The decreases in rates of the two reactions were nearly the same. The results of XRD and Mossbauer spectroscopy indicated that the online addition of sulfur did not greatly alter the distributions of iron carbide and magnetite. Both data sets consistently suggest an adsorption mechanism, in line with the results of reaction testing. XANES results at the S K-edge further confirmed sulfur adsorption, and some sulfide and sulfate species, likely confined to the surface zone, were detected. In this study, the sulfur tolerances of the precipitated Fe and a supported Co catalyst were compared at an identical temperature (i.e., 230 degrees C), and similar M/S ratios (13.5-15.0) were obtained. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:127 / 137
页数:11
相关论文
共 50 条
  • [31] Studies with a precipitated iron Fischer-Tropsch catalyst reduced by H2 or CO.
    Bian, G
    Oonuki, A
    Fujishita, N
    Koizumi, N
    Nomoto, H
    Yamada, M
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2002, 223 : U574 - U574
  • [32] Precipitated iron Fischer-Tropsch catalyst manufacturing: impact of Hematite
    Duvenhage, Dawid J.
    Schmidt, Christine
    Wright, Harold W.
    JOURNAL OF MATERIALS SCIENCE, 2014, 49 (07) : 2810 - 2823
  • [33] ACTIVATION STUDIES WITH A PROMOTED PRECIPITATED IRON FISCHER-TROPSCH CATALYST
    BUKUR, DB
    LANG, XS
    ROSSIN, JA
    ZIMMERMAN, WH
    ROSYNEK, MP
    YEH, EB
    LI, CP
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (08) : 1130 - 1140
  • [34] Studies on precipitated iron catalysts for Fischer-Tropsch synthesis
    Hayakawa, Hiroshi
    Tanaka, Hisanori
    Fujimoto, Kaoru
    APPLIED CATALYSIS A-GENERAL, 2006, 310 (1-2) : 24 - 30
  • [35] Activation studies with a promoted precipitated iron Fischer-Tropsch catalyst
    Bukur, Dragomir
    Lang, Xiaosu
    Rossin, Joseph A.
    Zimmerman, William H.
    Rosynek, Michael P.
    Yeh, Eshan B.
    Li, Chiuping
    Industrial and Engineering Chemistry Research, 1992, v (0n): : 1130 - 1140
  • [36] Pretreatment effect studies with a precipitated iron Fischer-Tropsch catalyst in a slurry reactor
    Bukur, DB
    Lang, XS
    Ding, YJ
    APPLIED CATALYSIS A-GENERAL, 1999, 186 (1-2) : 255 - 275
  • [37] ACTIVATION OF PRECIPITATED IRON FISCHER-TROPSCH SYNTHESIS CATALYSTS
    SHROFF, MD
    KALAKKAD, DS
    COULTER, KE
    KOHLER, SD
    HARRINGTON, MS
    JACKSON, NB
    SAULT, AG
    DATYE, AK
    JOURNAL OF CATALYSIS, 1995, 156 (02) : 185 - 207
  • [38] ACTIVATION STUDIES WITH A PRECIPITATED IRON CATALYST FOR FISCHER-TROPSCH SYNTHESIS .2. REACTION STUDIES
    BUKUR, DB
    NOWICKI, L
    MANNE, RK
    LANG, XS
    JOURNAL OF CATALYSIS, 1995, 155 (02) : 366 - 375
  • [39] Effect of Iron Precursor on Catalytic Performance of Precipitated Iron Catalyst for Fischer–Tropsch Synthesis Reaction
    Zuoxing Di
    Xuleng Feng
    Zhi Yang
    Mingsheng Luo
    Catalysis Letters, 2020, 150 : 2640 - 2647
  • [40] Effect of strain on the performance of iron-based catalyst in Fischer-Tropsch synthesis
    Xue, Yingying
    Ge, Hui
    Chen, Zheng
    Zhai, Yongbiao
    Zhang, Juan
    Sun, Jiaqiang
    Abbas, Mohamed
    Lin, Ke
    Zhao, Wentao
    Chen, Jiangang
    JOURNAL OF CATALYSIS, 2018, 358 : 237 - 242