[1] L.C. Castañeda, J.A.D. Muñoz, J.Ancheyta, Combined process schemes for upgrading of heavy petroleum, Fuel 100 (2012) 110–127. [2] G. Díaz-Boffelli, J. Ancheyta, J.A.D. Muñoz, G.Centeno, Experimental study and economic analysis of heavy oil partial upgrading by solvent deasphalting-hydrotreating, Energy Fuels 32 (1) (2018) 55–59. [3] F.E. Biasca, R.L. Dickenson, E. Chang, H.E. Johnson, R.T. Bailey, D.R. Simbeck. Upgrading Heavy Crude Oils and Residues to Transportation Fuels: Technology, Economics, and Outlook, phase VII, SFA Pacific Inc. Mountain View, CA., 2003. [4] S.Y. Sun, F.D.Meng, Study on solvent deasphalting process for upgrading of hydrocracking unconverted oil, Ind. Eng. Chem. Res. 60 (1) (2021) 652–658. [5] C. Takeuchi, Y. Fukui, M. Nakamura, Y.Shiroto, Asphaltene cracking in catalytic hydrotreating of heavy oils. 1. Processing of heavy oils by catalytic hydroprocessing and solvent deasphalting, Ind. Eng. Chem. Proc. Des. Dev. 22 (2) (1983) 236–242. [6] A. Zachariah, A.de Klerk, Partial upgrading of bitumen: Impact of solvent deasphalting and visbreaking sequence, Energy Fuels 31 (9) (2017) 9374–9380. [7] J.M. Zhao, L. Ren, T. Liu, L.S. Dai, L. Zhang, W. Han, D.D.Li, An insight into the evolution of sulfur species during the integration process of residue hydrotreating and delayed coking, Ind. Eng. Chem. Res. 59 (28) (2020) 12719–12728. [8] E.V. Parkhomchuk, K.V. Fedotov, A.I. Lysikov, A.V. Polukhin, E.E. Vorob’eva, I.A. Shamanaeva, N.N. San’kova, D.O. Shestakova, Y.O. Chikunova, S.E. Kuznetsov, A.V. Kleimenov, V.N.Parmon, Technology for the multifunctional hydrothermal treatment of oil residues (mazut and tar) on catalysts with a hierarchical structure of pores, Catal. Ind. 14 (1) (2022) 86–114. [9] L. Ye, X.L. Qin, A. Murad, L.X. Hou, J.C. Liu, J.Q. Xie, W.X. Yu, X. Pu, X. Han, J.G. Zhao, H. Sun, H.Ling, Coupling simulation of delayed coking and hydrotreating process at molecular level, Chem. Eng. J. 449 (2022) 137543. [10] A. Alvarez, J.Ancheyta, Modeling residue hydroprocessing in a multi-fixed-bed reactor system, Appl. Catal. A Gen. 351 (2) (2008) 148–158. [11] J. Martinez, J. Ancheyta, Modeling the kinetics of parallel thermal and catalytic hydrotreating of heavy oil, Fuel 138 (2014) 27–36. [12] J. Martínez, J.Ancheyta, Modeling the kinetics of parallel thermal and catalytic hydrotreating of heavy oil, Fuel 138 (2014) 27–36. [13] J. Martinez, J. Ancheyta, Kinetic model for hydrocracking of heavy oil in a CSTR involving short term catalyst deactivation, Fuel 100 (2012) 193–199. [14] J.A.D. Muñoz, R. Aguilar, L.C. Castañeda, J.Ancheyta, Comparison of correlations for estimating product yields from delayed coking, Energy Fuels 27 (11) (2013) 7179–7190. [15] N. Ashish, B. Aniruddha, D. Shriniwas, B. Jyeshtharaj. Petroleum residue upgrading via delayed coking: A Review. Canadian Journal of Chemical Engineering 85 (2007) 1-128. [16] M. Volk, K. Wisecarver, C. Sheppard. Fundamentals of Delayed Coking Joint Industry Project, US: n.p. (2003) doi: 10.21721902706. [17] L.C. Castañeda, J.A.D. Muñoz, J.Ancheyta, Comparison of approaches to determine hydrogen consumption during catalytic hydrotreating of oil fractions, Fuel 90 (12) (2011) 3593–3601. [18] J. Ancheyta, J.A.D. Muñoz, R.A. Aguilar, E. Martínez, T. Mata, H. Chávez. Definition of the Economic Viability of the Application of the HIDRO-IMP® Technology in Pemex Refining, Technical report, Instituto Mexicano del Petróleo, Mexico City, Mexico, 2011 (in Spanish). [19] Hyrocarbon Processing, Refining Processes Handbook, Gulf Publishing Company, Houston TX, 2011. [20] G. Farrar, Yearly refinery Construction Indexes Listed for 80+ Years, Oil & Gas Journal, 106 (2008), 54–55. [21] Nelson-Farrar cost index, http://www.bakerrisk.com, Accessed: 28 February 2022. [22] Pemex Refinacion. Long term price catalog for Pemex Refining operation results, Price catalog, Pemex Mexico City, Mexico, 2021 (in Spanish). [23] J. Ancheyta, Petroleum refining. Modeling and Simulation of Catalytic Reactors for Petroleum Refining. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2011: 1–52. [24] G. Centeno, J. Ancheyta, A. Alvarez, G. Marroquín, F. Alonso, A.Castillo, Effect of different heavy feedstocks on the deactivation of a commercial hydrotreating catalyst, Fuel 100 (2012) 73–79. [25] J. Ancheyta, G. Betancourt, G. Centeno, G. Marroquín, F. Alonso, E.Garciafigueroa, Catalyst deactivation during hydroprocessing of maya heavy crude oil. 1. evaluation at constant operating conditions, Energy Fuels 16 (6) (2002) 1438–1443. [26] J. Ancheyta, G. Betancourt, G. Centeno, G.Marroquín, Catalyst deactivation during hydroprocessing of maya heavy crude oil. (II) effect of temperature during time-on-stream, Energy Fuels 17 (2) (2003) 462–467. |