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
  • [1] Fischer-Tropsch synthesis: Effect of ammonia in syngas on the Fischer-Tropsch synthesis performance of a precipitated iron catalyst
    Ma, Wenping
    Jacobs, Gary
    Sparks, Dennis E.
    Pendyala, Venkat Ramana Rao
    Hopps, Shelley G.
    Thomas, Gerald A.
    Hamdeh, Hussein H.
    MacLennan, Aimee
    Hu, Yongfeng
    Davis, Burtron H.
    JOURNAL OF CATALYSIS, 2015, 326 : 149 - 160
  • [2] FISCHER-TROPSCH SYNTHESIS ON A PRECIPITATED IRON CATALYST
    MADON, RJ
    TAYLOR, WF
    JOURNAL OF CATALYSIS, 1981, 69 (01) : 32 - 43
  • [3] Fischer-Tropsch Synthesis: Effects of Hydrohalic Acids in Syngas on a Precipitated Iron Catalyst
    Ma, Wenping
    Jacobs, Gary
    Thomas, Gerald A.
    Shafer, Wilson D.
    Sparks, Dennis E.
    Hamdeh, Hussein H.
    Davis, Burton H.
    ACS CATALYSIS, 2015, 5 (05): : 3124 - 3136
  • [4] Effect of Iron Precursor on Catalytic Performance of Precipitated Iron Catalyst for Fischer-Tropsch Synthesis Reaction
    Di, Zuoxing
    Feng, Xuleng
    Yang, Zhi
    Luo, Mingsheng
    CATALYSIS LETTERS, 2020, 150 (09) : 2640 - 2647
  • [5] Effect of Hydrothermal Treatment on Precipitated Iron Catalyst for Fischer-Tropsch Synthesis
    Ma, Cailian
    Chen, Jiangang
    CATALYSIS LETTERS, 2015, 145 (02) : 702 - 711
  • [6] Effects of halogenated acids and hydrogen cyanide in syngas on a precipitated iron Fischer-Tropsch synthesis catalyst
    Ma, Wenping
    Jacobs, Gary
    Sparks, Dennis E.
    Davis, Burtron H.
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2014, 248
  • [7] Detailed kinetics of Fischer-Tropsch synthesis on a precipitated iron catalyst
    Pour, Ali Nakhaei
    Khodabandeh, Hamideh
    Izadyar, Mohammad
    Housaindokht, Mohammad Reza
    REACTION KINETICS MECHANISMS AND CATALYSIS, 2014, 111 (01) : 29 - 44
  • [8] KINETICS OF FISCHER-TROPSCH SYNTHESIS OVER PRECIPITATED IRON CATALYST
    SHEN Wen-Jie ZHOU Jing-Lai ZHANG Bi-JiangInstitute of Coal Chemistry
    Journal of Natural Gas Chemistry, 1994, (04) : 385 - 400
  • [9] Preparation of a new precipitated iron catalyst for Fischer-Tropsch synthesis
    Hayakawa, Hiroshi
    Tanaka, Hisanori
    Fujimoto, Kaoru
    CATALYSIS COMMUNICATIONS, 2007, 8 (11) : 1820 - 1824
  • [10] CHARACTERIZATION OF A PROMOTED PRECIPITATED IRON CATALYST FOR FISCHER-TROPSCH SYNTHESIS
    LOX, ES
    MARIN, GB
    DEGRAVE, E
    BUSSIERE, P
    APPLIED CATALYSIS, 1988, 40 (1-2): : 197 - 218