Диссертация (1173077), страница 16
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I., Okunev A. G., Parunin P. D., SemeikinaV. S., Ayupov A. B., Parmon V. N. Meso/macroporous CoMo alumina pelletsfor hydrotreating of heavy oil //Industrial & Engineering Chemistry Research.– 2013. – V. 52. – N. 48. – P. 17117-17125.44. Sun Z. X., Zheng T. T., Bo Q. B., Du M., Forsling W. Effects of calcinationtemperature on the pore size and wall crystalline structure of mesoporousalumina //Journal of colloid and interface science. – 2008. – V. 319. – N. 1. –P. 247-251.45.
Suzuki N., Yamauchi Y. One-step synthesis of hierarchical porous γ-aluminawith high surface area //Journal of sol-gel science and technology. – 2010. –V. 53. – N. 2. – P. 428-433.46. Wu W., Wan Z., Zhu M., Zhang D. A facile route to aqueous phase synthesisof mesoporous alumina with controllable structural properties //Microporousand Mesoporous Materials. – 2016.
– V. 223. – P. 203-212.47.Wu W., Wan Z., Chen W., Zhu M., Zhang D. Synthesis of mesoporousalumina with tunable structural properties //Microporous and MesoporousMaterials. – 2015. – V. 217. – P. 12-20.12248. Grant S. M., Vinu A., Pikus S., Jaroniec M. Adsorption and structuralproperties of ordered mesoporous alumina synthesized in the presence of F127block copolymer //Colloids and Surfaces A: Physicochemical and EngineeringAspects.
– 2011. – V. 385. – N. 1. – P. 121-125.49. Bleta R., Alphonse P., Pin L., Gressier M., Menu M. J. An efficient route toaqueous phase synthesis of nanocrystalline γ-Al2O3 with high porosity: fromstable boehmite colloids to large pore mesoporous alumina //Journal of colloidand interface science. – 2012. – V. 367.
– № 1. – P. 120-128.50. Taromi A. A., Kaliaguine S. Synthesis of ordered mesoporous γ-alumina–Effects of calcination conditions and polymeric template concentration//Microporous and Mesoporous Materials. – 2017. – V. 248. – P. 179-191.51. A Hardin A. H., Packwood R. H., Ternan M. Effects of median pore diametersin co-mo-Al2O3 catalysts on conversion of athabasca bitumen //abstracts ofpapers of the American Chemical Society. – 1155 16th st, nw, Washington, dc20036 : Amer Chemical Coc. – 1978. – V.
176. – N. Sep. – P. 69-69.52.Hardin A. H., Ternan M., Packwood R. H. The Effect of Pore Size in MoO3CoO3-Al2O3 Hydroprocessing Catalysts, CANMET Report 81-4E //Energy,Mines and Resources, Canada. – 1981.53. Shimura M., Shiroto Y., Takeuchi C. Effect of catalyst pore structure onhydrotreating of heavy oil //Industrial & engineering chemistry fundamentals.– 1986. – V. 25. – N. 3. – P. 330-337.54.
Marafi A., Fukase S., Al-Marri M., Stanislaus A. A comparative study of theeffect of catalyst type on hydrotreating kinetics of Kuwaiti atmospheric residue//Energy & fuels. – 2003. – V. 17. – N. 3. – P. 661-668.55. Ancheyta-Juarez J., Maity S. K., Betancourt-Rivera G., Centeno-Nolasco G.,Rayo-Mayoral, P., Gómez-Pérez M. T. Comparison of different NiMo/alumina catalysts on hydrodemetallization of Maya crude oil //AppliedCatalysis A: General. – 2001. – V.
216. – N. 1. – P. 195-208.12356. Rana M. S., Ancheyta J., Rayo P., Maity, S. K. Effect of alumina preparationon hydrodemetallization and hydrodesulfurization of Maya crude //Catalysistoday. – 2004. – V. 98. – N. 1. – P. 151-160.57. Ancheyta J., Rana M. S., Furimsky E. Hydroprocessing of heavy petroleumfeeds: Tutorial //Catalysis Today. – 2005. – V. 109. – N. 1. – P. 3-15.58.Rana M. S., Ancheyta J., Rayo P. A comparative study for heavy oilhydroprocessing catalysts at micro-flow and bench-scale reactors //Catalysistoday.
– 2005. – V. 109. – N. 1. – P. 24-32.59. Liu T., Ju L., Zhou Y., Wei Q., Ding S., Zhou W., Tao X.. Effect of pore sizedistribution (PSD) of Ni-Mo/Al 2 O 3 catalysts on the Saudi Arabia vacuumresiduum hydrodemetallization (HDM) //Catalysis Today. – 2016. – V. 271. –P. 179-187.60. Gualda G., Kasztelan S.
Coke versus metal deactivation of residuehydrodemetallization catalysts //Studies in Surface Science and Catalysis. –1994. – V. 88. – P. 145-154.61. Hydroprocessing catalyst: патент US 5221656: МПК C 10G 49/04 / ClarkF.T., Hensley A.L., Kukes S.G., Arters D.C. Заявитель и патентообладательBP Corporation North America Inc.; Заявл.
25.03.1992; опубл. 22.06.1993.62.Hydroconversion process employing catalyst with specified pore distributionand no added silica. Патент US 5827421 МПК B01J 23/85; Sherwood D.E.;Заявитель IFP Energies Nouvelles; Патентообладатель Texaco; заявл.24.08.1995; опубл. 27.10.1998.63.Hydroconversion process and catalyst: патент US 5622616 A: МПК C 10G47/12 / Porter M.K., Clausen G.A. Заявитель и патентообладатель TexacoDevelopment Corp.; Заявл. 30.01.1995; опубл. 22.04.1997.64. Catalyst for hydrotreating and/or hydroconversion and its use inhydrotreatment process for batches containing hydrocarbons / патент US7119045 B2: МПК B 01J 35/10 / Magual L., Roulean L., Kressman S.,Guillaume D.J.M.; Заявитель и патентообладатель IFP Energies Nouvelles;Заявл. 24.05.2002; опубл.
27.05.2003.12465.Hydrodemetalationandhydrodesulphurizationcatalystofspecialmacroporosity: патент US 5089463: МПК C 10 G 45/04 / Johnson D.R.Заявитель и патентообладатель Chevron Research and Technology Co.;Заявл. 04.10.1988; опубл. 18.02.1992.66. Катализаторгидродеметаллированияигидродесульфуризациииприменение в способе соединения в одном составе: пат. 2444406 Россия:, МПК B 01J 23/882; 23/883; 21/04; 21/02; 35/10; C 10G 45/08; 49/12 /Гишар Б., Гийом Д. Заявитель и патентообладатель ИФП Франция; заявл.17.12.2009; опубл.
10.03.2012.67. Пармон В. Н. Каталитическая гидропереработка тяжелого нефтяногосырья //Успехи химии. – 2015. – Т. 84. – №. 9. – С. 981-999.68. Marafi M., Stanislaus A., Furimsky E. Handbook of spent hydroprocessingcatalysts. – Elsevier, 2017.69. Quann R. J., Ware R. A., Hung C.
W., Wei J. Catalytic hydrodemetallation ofpetroleum //Advances in chemical engineering. – Academic Press. – 1988. –V. 14. – P. 95-259.70. Deepa G., Ajgaonkar A. V., Shanthi K., Sivasanker S. Hydrodemetallation andHydrogenation Activity of Ni–Mo (S) Supported on Porous Materials:Investigations Using Model Compounds //Advanced Porous Materials. – 2016.– V. 4. –N. 2. – P. 144-149.71. Alfadhli J., Alhindi A., Alotaibi A., Bahzad D. Performance assessment ofNiMo/γ-Al2O3 catalysts for upgrading KEC-AR: An assessment of selectedapparent kinetic parameters of selected hydrotreating reactions //Fuel. – 2016.– V. 164.
– P. 38-45.72. Li J., Xia Z., Lai W., Zheng J., Chen B., Yi X.,Fang W. Hydrodemetallation(HDM) of nickel-5, 10, 15, 20-tetraphenylporphyrin (Ni-TPP) over NiMo/γAl2O3 catalyst prepared by one-pot method with controlled precipitation ofthe components //Fuel. – 2012. – V.
97. – P. 504-511.12573. Gulyaeva L. A., Khavkin V. A., Shmel’kova O. I., Vinogradova N. Y.,Bitiev G. V., Krasil’nikova L. A., Nikul’shin P. A. // Chemistry andTechnology of Fuels and Oils. – 2019. – V. 54. – N. 6. – P. 669-675.74. Núñez M., Villamizar M. Optimization of the design of catalysts for thehydrodemetallation of deasphalted vacuum bottoms //Applied Catalysis A:General. – 2003. – V. 252. – N. 1. – P. 51-56.75.
Stanislaus A., Al-Dolama K., Absi-Halabi M. Preparation of a large porealumina-based HDM catalyst by hydrothermal treatment and studies on poreenlargement mechanism //Journal of Molecular Catalysis A: Chemical. – 2002.– V. 181. – N. 1-2. – P.
33-39.76. Loos M., Ascone I., Goulon-Ginet C., Goulon J., Guillard C., Lacroix M., DesCourieres T. XAFS study of model vanadium sulphide phases suspected toform on HDM catalyst surfaces //Catalysis Today. – 1990. – V. 7. – N. 4. – P.515-529.77. Zhao X. J., Wei J. Interaction of nickel deposits with catalytic metals onCoMo/Al2O3 hydrodemetalation catalysts //Journal of Catalysis. – 1994. – V.147. –N. 2. – P. 429-440.78.Rautiainen E.
P. H., Wei J. Hydrodemetallation catalyst deactivation—effectof metals accumulation on hydrogenation and hydrogenolysis activities//Chemical engineering communications. – 1990. – V. 98. – N. 1. – P. 113127.79. Pat. 3553106 USA, Catalytic removal of vanadium and nickel from oils. /Hamilton H. A., Mcilvried H. G., Sebulsky R. T.; Current Assignee ChevronResearch and Technology Co Gulf Research and Development Co; Publ.01.05.1971.80.
Catalystsandadsorbents[Электронныйhttps://www.axens.net/search.html?q=Catalysts31.08.2019).ресурс].(датаURL:обращения:12681. Mozhaev A. V., Nikulshin P. A., Pimerzin A. A., Maslakov K. I., Pimerzin A.A. Investigation of co-promotion effect in NiCoMoS/Al2O3 catalysts based onCo2Mo10-heteropolyacid and nickel citrate // Catalysis Today. 2016. – V.
271.– P. 80-90.82. Topsøe H., Clausen B.S., Massoth F.E. Hydrotreating Catalysis. Science andtechnology. Catalysis – Science and Technology. –1996. –V.11. –P.310.83. Eijsbouts S. On the flexibility of the active phase in hydrotreating catalysts. //Applied Catalysis A: General. –1997. –N. 158. –P.53-92.84. Grønborg S. S., Salazar N., Bruix A., Rodríguez-Fernández J., Thomsen S. D.,Hammer B., Lauritsen J. V.