Abstract
It was reported in earlier studies that a linear correlation existed between the total sulfur exchange capacity and thiophene hydrodesulfurization activity of different, alumina- or silica-supported molybdenum- or tungsten-sulfide based porous catalysts promoted with different metals: Co, Ni, Pt and Pd. The aim of this study was to clear up how general the linear correlation is, whether that correlation is generally applicable, whether it shows a particular character of the active sites in thiophene hydrodesulfurization (HDS). Industrial catalysts are more complex than typical model catalysts so the extents of thiophene HDS were determined on six industrially manufactured catalysts available today (combinations of Mo, W and Ni supported on alumina and of one NiW on silica-alumina) and compared to their sulfur uptake, and radiosulfur exchange capacity at 623 K. The majority of these catalyst samples also contained some phosphorus in different amounts. The results of the cyclohexane dehydrogenation as a model reaction indicated the absence of metallic nickel on the surface of the catalysts. A linear correlation was observed between the sulfur exchange capacity and HDS activity of these catalysts (with the exception of the sample supported on silica-alumina) similar to that observed previously.
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References
BP Statistical Review of World Energy 2015
Directive 2009/30/EC (2009) Specification of petrol, diesel and gas-oil and introducing a mechanism to monitor and reduce greenhouse gas emissions, Official Journal of the European Union, L 140/88- L 140/113
Manufacturers of Emission Controls Association (2013) The Impact of Gasoline Fuel Sulfur on Catalytic Emission Control Systems
Topsoe H, Clausen BS, Massoth FE (1996) Hydrotreating catalysis, science and technology. In: Anderson R, Boudart M (eds) Catalysis, Science and Technology. Springer, Berlin/New York
Eijsbouts S (1999) Life cycle of hydroprocessing catalysts and total catalyst management. Stud Surf Sci Catal 121:21–36
Egorova M, Prins R (2004) Hydrodesulfurization of dibenzothiophene and 4,6-dimethyldibenzothiophene over sulfided NiMo/γ-Al2O3, CoMo/γ- Al2O3, and Mo/γ- Al2O3 catalysts. J Catal 225:417–427
Kogan VM (2005) 35S Tracer study of the effect of support nature on the dynamics of the active sites of CoMo and NiMo sulfide catalysts supported on Al2O3 and activated carbon. Kinet Catal 46:77–87
Dobrovolszky M, Tétényi P, Paál Z (1989) Sulfur uptake and release by Mo and Co-Mo catalysts as studied by H 352 S radiotracer. Chem Eng Commun 83:1–8
Afanasiev P (2008) Synthetic approaches to the molybdenum sulfide materials. C. R. Chim 11:159–182
Ledoux M, Hantzer S, Guille J (1987) A comparative study of the influence of the preparation on the activity of NiMo and NiW hydrodesulfurization (HDS) catalysts. Bull Soc Chim Belg 96:855–864
Stanislaus A, Marafi A, Rana MS (2010) Recent advances in the science and technology of ultra low sulfur diesel (ULSD) production. Catal Today 153:1–68
Vit Z, Gulkova D, Kaluza L, Zdrazil M (2005) Synergetic effects of Pt and Ru added to Mo/Al2O3 sulfide catalyst in simultaneous hydrodesulfurization of thiophene and hydrogenation of cyclohexene. J Catal 232:447–455
Tétényi P (2006), in: Hargreaves SJ, Jackson SD, Webb G (Eds.) Isotopes in Heterogeneous Catalysis. Catal. Science Ser., Imp. Coll. Press London
Massoth FE, Zeuthen P (1994) Sulfur exchange studies on a Mo/Al2O3 catalyst. J Catal 145:216–222
Massoth FE, Koltai T, Tétényi P (2001) Theoretical analysis of sulfur exchange experiments. J Catal 203:33–40
Koltai T, Massoth FE, Tétényi P (2000) A radioisotope flow-circulation tracer method for determination of sulfur uptake and exchange. React Kinet Catal Lett 71:85–92
Tétényi P, Ollár T, Szarvas T (2012) Sulfur exchange capacity and thiophene hydrodesulfurization activity of sulfided molybdena-alumina catalysts promoted by nickel. Catal Today 181:148–155
Morales A, Salazar JA, Ramírez de Agudelo MM, Martinez NP, Carraaquel A, US Patent 4600703 (Cited from: M.M. Ramírez de Agudelo, A. Morales, in M.J. Phillips, M. Ternan, (Eds): Proc. 9th Int. Congress on Catalysis. Vol. 1. 42–57
Hilfman L, US Patent 3617528; (Cited from: M.M. Ramírez de Agudelo, A. Morales, in M.J. Phillips, M. Ternan, (Eds): Proc. 9th Int. Congress on Catalysis. Vol. 1. 42–57
Morales A, Ramirez de Agudelo NM (1986) Promoter role of octahedral Co (and Ni) in modified Co(Ni)Mo-Al2O3 catalysts for hydrodesulfurization reactions. Appl Catal 23:23–34
Tétényi P, Ollár T, Schay Z, Schnörch P, Szarvas T (2008) Sulfur uptake determination on Ni containing molybdena-alumina samples by radioisotope tracer technique. Appl Radiat Isot 66:1190–1195
Ripperger W, Saum W, (1977) in Proc. Clymax Intern. Conference on the Chemistry and Uses of Molybdena. (Mitchell P.C.H. Ed.) p.175. (Cited from: M.M. Ramírez de Agudelo, A. Morales, in M.J. Phillips, M. Ternan, (Eds): Proc. 9th Int. Congress on Catalysis, Vol. 1. 42-57
Koltai T, Galsán V, Tétényi P (1999) Effect of pretreatment on HDS activity of supported NiW and NiMo catalysts. React Kinet Catal Lett 67:391–396
Balandin AA, (1969) Modern state of the multiplet theor of heterogeneous catalysis. Adv Catalysis, 19: 1–210. (The paper was prepared for publication by E.I. Klabunovskii.)
Chianelli RR, Prestridge EB, Pecoraro TA, Deneufville JP (1979) Molybdenum disulfide in the poorly crystalline “rag” structure. Science 203:1105–1107
Paál Z (1988) Hydrocarbon product selectivity: a tool for characterizing the active state of platinum catalysts. Catal Today 2:595–604
Chianelli RR, Prestridge EB, Pecoraro TA, Deneufville JP (1979) Molybdenum disulfide in the poorly crystalline “rag” structure. Science 203:1105–1107
Chadwick D, Breysse M (1981) The nature of hydrodesulphurization on MoS2. J Catal 71:226–227
Massoth FE (1975) Studies of molybdena-alumina catalysts: IV. Rates and stoichiometry of sulfidation. J Catal 36:164–184
Cottrell TL (1954) The strengths of chemical bonds, London. Publ, Butterworth’s Sci
van Haandel L, Bremmer GM, Hensen EJM, Weber Th (2016) Influence of sulfiding agent and pressure on structure and performance of CoMo/Al2O3 hydrodesulfurization catalysts. J Catal 342:27–39
Kogan VM, Isaguliants GV (2008) The HDS mechanism: Which “auxiliary” process takes place—sulfur isotopic exchange or replacement—and why is it important to know it? Catal Today 130:243–248
Nagai M, Thanh Tung N, Adachi Y, Kobayashi K (2016) New approach to active sites analysis of molybdenum-containing catalysts for hydrodesulfurization and hydrodenitrogenation based on inverse problem, fractal and site-type analyses. Catal Today 271:91–101
Acknowledgements
The authors express their gratitude to + Professor Z. Paál (Surface Chemistry and Catalysis Department, Centre for Energy Research,) for valuable discussions during these studies. They express their gratefulness to the Company MOL for the support of studies presented here. One of the authors, Tamás Ollár, participated in the experiments, serving a significant part of this research in the frames of TÁMOP 4.2.4. A/2-11-1-2012-0001 “National Excellence Program—Elaborating and operating an inland student and researcher personal support system convergence program” The project was subsidized by the European Union and co-financed by the European Social Fund.
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Varga, Z., Szarvas, T., Tétényi, P. et al. The particular characteristics of the active sites of MoS2, WS2 catalysts in thiophene hydrodesulfurization. Reac Kinet Mech Cat 124, 61–74 (2018). https://doi.org/10.1007/s11144-017-1283-y
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DOI: https://doi.org/10.1007/s11144-017-1283-y