Volume 47 Issue 5
May  2019
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WAND Li-wen, LI Feng-xu, LI Ming-feng, CHU Yang, CHEN Ji-xiang. Effect of H2S/H2 sulfuration temperature on performance of MoP/SiO2 catalyst for thioetherification[J]. Journal of Fuel Chemistry and Technology, 2019, 47(5): 621-628.
Citation: WAND Li-wen, LI Feng-xu, LI Ming-feng, CHU Yang, CHEN Ji-xiang. Effect of H2S/H2 sulfuration temperature on performance of MoP/SiO2 catalyst for thioetherification[J]. Journal of Fuel Chemistry and Technology, 2019, 47(5): 621-628.

Effect of H2S/H2 sulfuration temperature on performance of MoP/SiO2 catalyst for thioetherification

Funds:

The project was supported by the State Key Laboratory of Catalytic Materials and Reaction Engineering RIPP, SINOPEC

  • Received Date: 2018-10-17
  • Rev Recd Date: 2019-03-23
  • Available Online: 2021-01-23
  • Publish Date: 2019-05-10
  • The MoP/SiO2 catalyst was prepared from the supported Mo phosphate by the H2-TPR method and treated with 3%H2S/H2 at different temperatures. The as-prepared catalysts were characterized by means of XRD, HRTEM-EDX, XPS, NH3-TPD, ICP-AES and CO chemisorption and tested for the thioetherification of isoprene and n-butylmercaptan. The effects of sulfuration temperature on the MoP/SiO2 catalyst structure and thioetherification performance were investigated. The results showed that the MoP phase was still stable even at the sulfuration temperature of 400 ℃. As the sulfuration temperature increased, the acid amount of the catalysts increased while the surface metal site density decreased. As a result, in the thioetherification of isoprene and n-butylmercaptan, the C-S bond hydrogenolysis and the over-hydrogenation of isoprene were suppressed on the sulfurized catalysts, while the olefin polymerization was promoted. Relatively, the MoP/SiO2 catalyst sulfurized at 120 ℃ had better performance for the thioetherification and the selective hydrogenation of isoprene.
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  • [1]
    BRUNET S, MEY D, PÉROT G, BOUCHY G, DIEHL F. On the hydrodesulfurization of FCC gasoline:A review[J]. Appl Catal A:Gen, 2005, 278(2):143-172. doi: 10.1016/j.apcata.2004.10.012
    [2]
    SONGC.Anoverviewofnewapproachestodeepdesulfurizationforultra-cleangasoline, dieselfuelandjetfuel[J].Catal Today, 2003, 86(1):211-263. https://www.onacademic.com/detail/journal_1000034202600910_0952.html
    [3]
    PETTITI I, BOTTO I L, CABELLO C I, COLONNA C, FATICANTI M, MINELLI G, PORTA P, THOMAS H J. Anderson-type heteropolyoxomolybdates in catalysis 2. EXAFS study on λ-Al2O3-supported Mo, Co and Ni sulfided phases as HDS catalysts[J]. Appl Catal A:Gen, 2001, 220(1):113-121.
    [4]
    孟祥东, 周洪涛, 孙守华.催化裂化汽油选择性加氢脱硫装置的工艺选择[J].石化技术与应用, 2014, 32(4):332-336. doi: 10.3969/j.issn.1009-0045.2014.04.012

    MENG Xiang-dong, ZHOU Hong-tao, SUN Shou-hua. Process selection of selective hydrodesulfurization unit of catalytic cracking gasoline[J]. Petrochem Technol Appl, 2014, 32(4):332-336. doi: 10.3969/j.issn.1009-0045.2014.04.012
    [5]
    肖招金, 黄星亮.镍基催化剂上硫醇与异戊二烯硫醚化反应的研究[J].分子催化, 2005, 19(4):280-284. doi: 10.3969/j.issn.1001-3555.2005.04.009

    XIAO Zhao-jin, HUANG Xing-liang. Study of mercaptans and isoprene thioetherfication reaction on nickel catalyst[J]. J Mol Catal (China), 2005, 19(4):280-284. doi: 10.3969/j.issn.1001-3555.2005.04.009
    [6]
    肖招金, 黄星亮.制备条件对Ni/Al2O3催化剂二烯硫醚化性能的研究[J].石油化工, 2004, 33(s1):381-382. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=syhg2004z1154

    XIAO Zhao-jin, HUANG Xing-liang. Effect of preparation conditions on the catalytic properties of Ni/Al2O3 catalyst in the diene thioetherfication reaction[J]. Petrochem Technol, 2004, 33(s1):381-382. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=syhg2004z1154
    [7]
    肖招金, 黄星亮, 童宗文.制备条件对二烯硫醚化催化剂Ni/Al2O3催化性能的影响[J].石油炼制与化工, 2006, 37(5):24-28. doi: 10.3969/j.issn.1005-2399.2006.05.006

    XIAO Zhao-jin, HUANG Xing-liang, TONG Zong-wen. Effect of preparation conditions on the catalytic properties of Ni/Al2O3 catalyst in the diene thioetherfication reaction[J]. Pet Process Petrochem, 2006, 37(5):24-28. doi: 10.3969/j.issn.1005-2399.2006.05.006
    [8]
    申志兵, 柯明, 张君涛, 张智平, 梁生荣. Mo-Ni/Al2O3催化剂对FCC汽油硫醚化反应的催化性能[J].石油学报(石油加工), 2015, 31(6):1269-1274. doi: 10.3969/j.issn.1001-8719.2015.06.003

    SHEN Zhi-bing, KE Ming, ZHANG Jun-tao, ZHANG Zhi-ping, LIANG Sheng-rong. Catalytic performance of Mo-Ni/Al2O3 for thioetherfication of FCC gasoline[J]. Acta Pet Sin(Pet Process Sect), 2015, 31(6):1269-1274. doi: 10.3969/j.issn.1001-8719.2015.06.003
    [9]
    SHEN Z B, KE M, YU P, HU H Q, SONG Z Z, JIANG Q Z. Reaction mechanisms of thioetherification for mercaptans and olefins over sulfided Mo-Ni/Al2O3 catalysts[J]. J Mol Catal A:Chem, 2015, 396:120-127. doi: 10.1016/j.molcata.2014.09.034
    [10]
    SHEN Z B, KE M, YU P, LIU S D, SONG Z Z, JIANG Q Z. Catalytic activities of mo-modified Ni/Al2O3 catalysts for thioetherification of mercaptans and di-olefins in fluid catalytic cracking naphtha[J]. Transition Met Chem, 2012, 37(6):587-593. doi: 10.1007/s11243-012-9625-0
    [11]
    HUANG D Q, KE M, BAO X J, LIU H Y. Fe-promoted Ni/Al2O3 thioetherification catalysts with enhanced low temperature activity for removing mercaptans from liquefied petroleum gas[J]. Ind Eng Chem Res, 2016, 55(5):1192-1201. doi: 10.1021/acs.iecr.5b03797
    [12]
    OYAMA S T. Novel catalysts for advanced hydroprocessing:Transition metal phosphides[J]. J Catal, 2003, 216(1):343-352. http://cn.bing.com/academic/profile?id=8ca04206cbb6816a006940f96b887358&encoded=0&v=paper_preview&mkt=zh-cn
    [13]
    OYAMA S T, GOTT T, ZHAO H Y, LEE Y K. Transition metal phosphide hydroprocessing catalysts:A review[J]. Catal Today, 2009, 143(1):94-107. http://d.old.wanfangdata.com.cn/NSTLQK/NSTL_QKJJ0226572816/
    [14]
    LEE Y K, OYAMA S T. Bifunctional nature of a SiO2 -supported Ni2P catalyst for hydrotreating:EXAFS and FTIR studies[J]. J Catal, 2006, 239(2):376-389. doi: 10.1016/j.jcat.2005.12.029
    [15]
    CHEN J X, SHI H, LI L, LI K L. Deoxygenation of methyl laurate as a model compound to hydrocarbons on transition metal phosphide catalysts[J]. Appl Catal B:Environ, 2014, 144(2):870-884. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=00b3e67f7ee6f634b85d8c66a8128355
    [16]
    REN T Y, LI M F, CHU Y, CHEN J X. Thioetherification of isoprene and butanethiol on transition metal phosphides[J]. J Energy Chem, 2018, 27(3):930-939. doi: 10.1016/j.jechem.2017.07.017
    [17]
    PHILLIPS D C, SAWHILL S J, SELF R, BUSSELL M E. Synthesis, characterization, and hydrodesulfurization properties of silica-supported molybdenum phosphide catalysts[J]. J Catal, 2002, 207(2):266-273. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=0cf89dcb3cf46344a2cd0f0502028982
    [18]
    CHEN J X, YANG Y, SHI H, LI M F, CHU Y, PAN Z Y, YU X B. Regulating product distribution in deoxygenation of methyl laurate on silica-supported Ni-Mo phosphides:Effect of Ni/Mo ratio[J]. Fuel, 2014, 129(7):1-10. http://cn.bing.com/academic/profile?id=fac1698e18875be086a43c6b56897eea&encoded=0&v=paper_preview&mkt=zh-cn
    [19]
    LI K L, WANG R J, CHEN J X. Hydrodeoxygenation of anisole over silica-supported Ni2P, MoP, and NiMoP catalysts[J]. Energy Fuels, 2011, 25(3):854-863. doi: 10.1021/ef101258j
    [20]
    ZHANG Z N, TANG M X, CHEN J X. Effects of P/Ni ratio and Ni content on performance of λ-Al2O3-supported nickel phosphides for deoxygenation of methyl laurate to hydrocarbons[J]. Appl Surf Sci, 2016, 360(4):353-364. http://www.sciencedirect.com/science/article/pii/S016943321502601X
    [21]
    SUN F X, WU W C, WU Z L, GUO J, WEI Z B, YANG Y X, JIANG Z X, TIAN F P, LI C. Dibenzothiophene hydrodesulfurization activity and surface sites of silica-supported MoP, Ni2P, and NiMoP catalysts[J]. J Catal, 2004, 228(2):298-310. doi: 10.1016/j.jcat.2004.09.002
    [22]
    WU Z L, SUN F X, WU W C, FENG Z C, LIANG C H, WEI Z B, LI C. On the surface sites of MoP/SiO2 catalyst under sulfiding conditions:Ir spectroscopy and catalytic reactivity studies[J]. J Catal, 2004, 222(1):41-52. http://cn.bing.com/academic/profile?id=6520cd12ec9960d32386c397be1f78f6&encoded=0&v=paper_preview&mkt=zh-cn
    [23]
    BAI J, LI X, WANG A J, PRINS R WANG Y. Different role of H2S and dibenzothiophene in the incorporation of sulfur in the surface of bulk MoP during hydrodesulfurization[J]. J Catal, 2013, 300(3):197-200. http://www.wanfangdata.com.cn/details/detail.do?_type=perio&id=f55bf796bc845fe997533f8536141dfd
    [24]
    SHEN Z B, KE M, YU P, HU H Q, SONG Z Z, JIANG Q Z. Reaction mechanisms of thioetherification for mercaptans and olefins over sulfided Mo-Ni/Al2O3catalysts[J]. J Mol Catal A:Chem, 2015, 396:120-127. doi: 10.1016/j.molcata.2014.09.034
    [25]
    WILSON R L, KEMBALL C. Catalytic reactions of methyl mercaptan on disulfides of molybdenum and tungsten[J]. J Catal, 1964, 3(5):426-437. doi: 10.1016/0021-9517(64)90145-9
    [26]
    周志远, 黄星亮, 张燕, 李健.二烯硫醚化酸性催化剂研究[C]//全国青年催化学术会议.北京: 中国石化出版社, 2007.

    ZHOU Zi-yuan, HUANG Xing-liang, ZHANG Yan, LI Jian. Study on the acid catalysts for diene thioetherification[C]//National Youth Catalysis Conference. Beijing: China Petrochemical Press, 2007.
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