Abstract
The catalyst pore structure is important to accommodate deposits in the hydrotreatment processes. In the current study, urchin alumina with large pore mouths was successfully synthesized by template free method, and was used as catalyst support for the hydrodesulfurization (HDS) of Siberian crude oil. Commercial alumina was used as reference. The catalysts were characterized by XRD, N2 physisorption, TPR, NH3-TPD, SEM, and was evaluated in a trickle-bed reactor. The urchin alumina exhibits smaller surface area and larger average pore diameter than the commercial alumina. NiMo/ur-Al2O3 shows similar activity and better stability within the long-term HDS run of 100 h. After the HDS test, the weight loss of coke over NiMo/ur-Al2O3 is about half of that over NiMo/com-Al2O3; however, the urchin morphology of NiMo/ur-Al2O3 is not retained due to the high pressure during the reaction. The better performance in carbon resistance is consistent with the “chestnut bur” catalyst reported by IFP; this work supplements the synthesis detail and characterizations for the urchin-alumina supported catalyst, and provides important information for industrial hydrotreatment catalyst development.
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Babich IV, Moulijn JA (2003) Science and technology of novel processes for deep desulfurization of oil refinery streams: A review. Fuel 82:607–631
Srivastava VC (2012) An evaluation of desulfurization technologies for sulfur removal from liquid fuels. Rsc Adv 2:759–783
Rana MS, Ancheyta J, Maity SK, Rayo P (2004) Characteristics of maya crude hydrodemetallization and hydrodesulfurization catalysts. Abstr Pap Am Chem S 228:U660–U660
Li X, Han DZ, Xu YQ, Liu XM, Yan ZF (2011) Bimodal mesoporous gamma-Al2O3: A promising support for CoMo-based catalyst in hydrodesulfurization of 4,6-DMDBT. Mater Lett 65:1765–1767
Lopez-Salinas E, Espinosa JG, Hernandez-Cortez JG, Sanchez-Valente J, Nagira J (2005) Long-term evaluation of NiMo/alumina-carbon black composite catalysts in hydroconversion of Mexican 538 degrees C+ vacuum residue. Catal Today 109:69–75
Liu H, Li YP, Yin CL, Wu YL, Chai YM, Dong DM, Li XH, Liu CG (2016) One-pot synthesis of ordered mesoporous NiMo-Al2O3 catalysts for dibenzothiophene hydrodesulfurization. Appl Catal B-Environ 198:493–507
Han W, Yuan P, Fan Y, Shi G, Liu HY, Bai DJ, Bao XJ (2012) Preparation of supported hydrodesulfurization catalysts with enhanced performance using Mo-based inorganic-organic hybrid nanocrystals as a superior precursor. J Mater Chem 22:25340–25353
Liu YJ, Song SZ, Deng X, Huang W (2017) Diesel ultradeep hydrodesulfurization over trimetallic wmoni catalysts by a liquid-phase preparation method in a slurry bed reactor. Energ Fuel 31:7372–7381
Mouli KC, Soni K, Dalai A, Adjaye J (2011) Effect of pore diameter of Ni-Mo/Al-SBA-15 catalysts on the hydrotreating of heavy gas oil. Appl Catal a-Gen 404:21–29
Yuan P, Liu JX, Li YT, Fan Y, Shi G, Liu HY, Bao XJ (2014) Effect of pore diameter and structure of mesoporous sieve supported catalysts on hydrodesulfurization performance. Chem Eng Sci 111:381–389
Jiao JQ, Fu JY, Wei YC, Zhao Z, Duan AJ, Xu CM, Li JM, Song H, Zheng P, Wang XL, Yang YN, Liu Y (2017) Al-modified dendritic mesoporous silica nanospheres-supported NiMo catalysts for the hydrodesulfurization of dibenzothiophene: Efficient accessibility of active sites and suitable metal-support interaction. J Catal 356:269–282
Shi Y, Xiao CK, Mei JL, Alabsi MH, Wang G, Ni Y, Zhao Z, Duan AJ, Wang XL (2020) Modified dendritic mesoporous silica nanospheres composites: superior pore structure and acidity for enhanced hydrodesulfurization performance of dibenzothiophene. Energ Fuel 34:8759–8768
Zhang D, Liu WQ, Liu YA, Etim UJ, Liu XM, Yan ZF (2017) Pore confinement effect of MoO3/Al2O3 catalyst for deep hydrodesulfurization. Chem Eng J 330:706–717
Huirache-Acuna R, Pawelec B, Loricera CV, Rivera-Munoz EM, Nava R, Torres B, Fierro JLG (2012) Comparison of the morphology and HDS activity of ternary Ni(Co)-Mo-W catalysts supported on Al-HMS and Al-SBA-16 substrates. Appl Catal B-Environ 125:473–485
Valencia D, Klimova T (2013) Citric acid loading for MoS2-based catalysts supported on SBA-15. New catalytic materials with high hydrogenolysis ability in hydrodesulfurization. Appl Catal B-Environ 129:137–145
Liu M, Zhao D, Zhao S, Ding W (2014) Macro-pore Volume Mesoporous Alumina: A Promising Support for Mo-Ni-P Catalyst in Hydrodesulfurization. Petrol Sci Technol 32:1426–1431
Mansouri A, Semagina N (2018) Promotion of Niobium Oxide Sulfidation by Copper and Its Effects on Hydrodesulfurization Catalysis. Acs Catal 8:7621–7632
Chen YD, Wang L, Liu XY, Liu TF, Huang BK, Li P, Jiang ZX, Li C (2015) Hydrodesulfurization of 4,6-DMDBT on multi-metallic bulk catalyst NiAlZnMoW: Effect of Zn. Appl Catal a-Gen 504:319–327
Zhou WW, Zhang YA, Tao XJ, Zhou YS, Wei Q, Ding SJ (2018) Effects of gallium addition to mesoporous alumina by impregnation on dibenzothiophene hydrodesulfurization performances of the corresponding NiMo supported catalysts. Fuel 228:152–163
Kressmann, S. K. S.; Guillaume, D.; Roy, M (2004) A new generation of hydroconversion and hydrodesulfurization catalysts. In 14th Annual Symposium, Catalysis in Petroleum Refining & Petrochemicals,, King Fahd University of Petroleum & Minerals-KFUPM, The Research Institute, Dhahran, Saudi Arabia, December 5–6.
Huang HH, Wang L, Cai Y, Zhou CC, Yuan YW, Zhang XJ, Wan H, Guan GF (2015) Facile fabrication of urchin-like hollow boehmite and alumina microspheres with a hierarchical structure via Triton X-100 assisted hydrothermal synthesis. CrystEngComm 17:1318–1325
Rui XH, Tan HT, Sim DH, Liu WL, Xu C, Hng HH, Yazami R, Lim TM, Yan QY (2013) Template-free synthesis of urchin-like Co3O4 hollow spheres with good lithium storage properties. J Power Sources 222:97–102
Sun K, Ma X, Hou R (2021) Upgrading Siberian (Russia) crude oil by hydrodesulfurization: Kinetic parameter estimation in a trickle-bed reactor. Chin J Chem Eng 29:212–220
Ding LH, Zheng Y, Yang H, Parviz R (2009) LCO hydrotreating with Mo-Ni and W-Ni supported on nano- and micro-sized zeolite beta. Appl Catal a-Gen 353:17–23
Sun K, Ma X, Yang Q, Qiu R, Hou R (2020) Upgrading Siberian (Russia) crude oil by hydrodesulfurization in a slurry reactor: A kinetic study. Chin J Chem Eng 28:3027–3034
Rinaldi N, Kubota T, Okamoto Y (2010) Effect of citric acid addition on the hydrodesulfurization activity of MoO3/Al2O3 catalysts. Appl Catal a-Gen 374:228–236
Qu LL, Zhang WP, Kooyman PJ, Prins R (2003) MAS NMR, TPR, and TEM studies of the interaction of NiMo with alumina and silica-alumina supports. J Catal 215:7–13
Yun G, Guan Q, Li W (2017) The synthesis and mechanistic studies of a highly active nickel phosphide catalyst for naphthalene hydrodearomatization. Rsc Adv 7:8677–8687
Ramesh S, Venkatesha NJ (2017) Template Free Synthesis of Ni-Perovskite: An Efficient Catalyst for Hydrogen Production by Steam Reforming of Bioglycerol. ACS Sustainable Chemistry & Engineering 5:1339–1346
Kohli K, Prajapati R, Maity SK, Sau M, Sharma BK (2019) Accelerated pre-coking of NiMo/gamma-Al2O3 catalyst: Effect on the hydroprocessing activity of vacuum residue. Fuel 235:437–447
Boumaza A, Favaro L, Ledion J, Sattonnay G, Brubach JB, Berthet P, Huntz AM, Roy P, Tetot R (2009) Transition alumina phases induced by heat treatment of boehmite: An X-ray diffraction and infrared spectroscopy study. J Solid State Chem 182:1171–1176
Acknowledgement
The work carried out at Beijing Key Laboratory for Chemical Power Source and Green Catalysis was sponsored by National Natural Science Foundation of China 21606017. We thank Analysis & Testing Center at Beijing Institute of Technology for the supports on catalyst characterization.
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Nie, M., Ma, X., Sun, K. et al. Application of Urchin-Alumina as Catalyst Support in Hydrodesulfuization of Siberian (Ruassia) Crude Oil. Catal Lett 151, 3451–3461 (2021). https://doi.org/10.1007/s10562-021-03582-z
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DOI: https://doi.org/10.1007/s10562-021-03582-z