[1] X.T. Wang, W.R. Li, H.X. Weng, J.D. Liu, S.R. Qi, Q.T. Ma, Research on slight expandedbed oil residue hydrotreating reactor, Chem. Eng. (Xi'an, China) 34(9) (2006) 28-31(in Chinese). [2] M.R. Khadilkar, Y.X. Wu, M.H. Al-Dahhan, M.P. Dudukovic, M. Colakyan, Comparison of trickle-bed and upflow reactor performance at high pressure:model predictions and experimental observations, Chem. Eng. Sci. 51(10) (1996) 2139-2148. [3] J.F. Chen, Green chemical engineering, Eng. 3(3) (2017) 283-284. [4] M. Ji, Z. Yang, X.J. Lou, Y.M. Yong, C. Yang, Fluid flow and backmixing characteristics of up-flow reactor, Chem. Eng. (Xi'an, China) 43(11) (2015) 41-46(in Chinese). [5] W.J. Wang, Y.M. Yong, C. Yang, K. Yu, Flow and back-mixing characteristics in three dimensional up-flow reactor, CIESC J. 69(1) (2018) 381-388(in Chinese). [6] B. Hadi, J.R.V. Ommen, M.O. Coppens, Enhanced particle mixing in pulsed fluidized beds and the effect of internals, Ind. Eng. Chem. Res. 51(4) (2012) 1713-1720. [7] R.N. Maiti, K.D.P. Nigam, Gas-liquid distributors for trickle-bed reactors:a review, Ind. Eng. Chem. Res. 46(19) (2007) 6164-6182. [8] F. Bazer-Bachi, Y. Haroun, F. Augier, C. Boyer, Experimental evaluation of distributor technologies for trickle-bed reactors, Ind. Eng. Chem. Res. 52(32) (2013) 11189-11197. [9] B.E. Reynolds, F.W. Lam, J. Chabot, F.J. Antezana, R. Bachtel, K.R. Gibson, R. Threlkel, P.C. Leung, Upflow reactor system with layered catalyst bed for hydrotreating heavy feedstocks, U.S. Pat., 6554994 B1(2003). [10] S.L.P. Lee, H.I.D. Lasa, Phase holdups in three-phase fluidized beds, AICHE J. 33(8) (1987) 1359-1370. [11] S. Rabha, M. Schubert, M. Wagner, D. Lucas, U. Hampel, Bubble size and radial gas hold-up distributions in a slurry bubble column using ultrafast electron beam Xray tomography, AICHE J. 59(5) (2013) 1709-1722. [12] H.M. Jena, G.K. Roy, B.C. Meikap, Prediction of gas holdup in a three-phase fluidized bed from bed pressure drop measurement, Chem. Eng. Res. Des. 86(11) (2008) 1301-1308. [13] Z.X. Chen, J. Yang, D. Ling, P. Liu, I.M.S.K. Ilankoon, Z.B. Huang, Z.M. Cheng, Packing size effect on the mean bubble diameter in a fixed bed under gas-liquid concurrent upflow, Ind. Eng. Chem. Res. 56(45) (2017) 13490-13496. [14] A.M. Anter, Q. Xiao, Z.M. Cheng, W.K. Yuan, Liquid holdup measurements in downward flow and upward flow fixed-bed reactors, CIESC J. 51(4) (2000) 535-539(in Chinese). [15] M. Cassanello, O. Martínez, A.L. Cukierman, Liquid hold-up and backmixing in cocurrent upflow three-phase fixed-bed reactors, Chem. Eng. Sci. 53(5) (1998) 1015-1025. [16] J.G.G. Maldonado, D. Bastoul, S. Baig, M. Roustan, G. Hébrard, Effect of solid characteristics on hydrodynamic and mass transfer in a fixed bed reactor operating in cocurrent gas-liquid up flow, Chem. Eng. Process. 47(8) (2008) 1190-1200. [17] M.F.P. Moreira, M.C. Ferreira, J.T. Freire, Total liquid saturation in gas-liquid cocurrent downflow and upflow through packed beds and analysis of correlations for predicting the total liquid saturation, Ind. Eng. Chem. Res. 43(4) (2004) 1096-1102. [18] V. Sivakumar, G.S. Nirmala, T. Murugesan, Gas phase hold up in gas-liquid cocurrent upflow packed bed reactors at low Reynold's number, Bioprocess Eng. 21(1) (1999) 41-43. [19] P. Therning, A. Rasmuson, Liquid dispersion and gas holdup in packed bubble columns at atmospheric pressure, Chem. Eng. J. 81(1-3) (2001) 69-81. [20] F. Larachi, A. Laurent, G. Wild, N. Midoux, Some experimental liquid saturation results in fixed-bed reactors operated under elevated pressure in cocurrent upflow and downflow of the gas and the liquid, Ind. Eng. Chem. Res. 30(11) (1991) 2404-2410. [21] H. Sindhu, P.S.T. Sai, A model for pressure drop and liquid saturation in gas-liquid cocurrent upflow through packed beds, Chem. Eng. J. 93(2) (2003) 135-142. [22] A.K. Saroha, R. Khera, Hydrodynamic study of fixed beds with cocurrent upflow and downflow, Chem. Eng. Process. 45(6) (2006) 455-460. [23] E.J. Molga, K.R. Westerterp, Experimental study of a cocurrent upflow packed bed bubble column reactor:pressure drop, holdup and interfacial area, Chem. Eng. Process. 36(6) (1997) 489-495. [24] E.J. Molga, K.R. Westerterp, Gas-liquid interfacial area and holdup in a cocurrent upflow packed bed bubble column reactor at elevated pressures, Ind. Eng. Chem. Res. 36(3) (1997) 622-631. [25] J.H.P. Collins, A.J. Sederman, L.F. Gladden, M. Afeworki, J.D. Kushnerick, H. Thomann, Characterising gas behaviour during gas-liquid co-current up-flow in packed beds using magnetic resonance imaging, Chem. Eng. Sci. 157(2017) 2-14. [26] V. Alexander, H. Albazzaz, M. Al-Dahhan, Gas phase dispersion/mixing investigation in a representative geometry of gas-liquid upflow moving bed hydrotreater reactor (MBR) using developed gas tracer technique and method based on convolution/regression, Chem. Eng. Sci. 195(2019) 671-682. [27] S. Kumar, R.A. Kumar, P. Munshi, A. Khanna, Gas hold-up in three phase co-current bubble columns, Procedia Eng. 42(2012) 782-794. [28] A. Attou, G. Ferschneider, A simple model for pressure drop and liquid hold-up in packed-bed bubble reactors, Chem. Eng. Sci. 54(21) (1999) 5139-5144. [29] A. Montagna, Y.T. Shah, Backmixing effect in an upflow cocurrent hydrodesulfurization reactor, Chem. Eng. J. 10(1) (1975) 99-105. [30] T. Burkhardt, J. Verstraete, P. Galtier, M. Kraume, Residence time distributions with a radiotracer in a hydrotreating pilot plant:upflow versus downflow operation, Chem. Eng. Sci. 57(11) (2002) 1859-1866. [31] Z.S. Mao, J.Y. Chen, Chemical Reaction Engineering Fundamentals, Science Press, Beijing, 2004(in Chinese). [32] P.V. Danckwerts, Continuous flow systems, distribution of residence times, Chem. Eng. Sci. 2(1) (1953) 1-13. [33] O. Levenspiel, W.K. Smith, Notes on the diffusion-type model for the longitudinal mixing of fluids in flow, Chem. Eng. Sci. 6(4-5) (1957) 227-233. [34] M.L. Bordas, A. Cartellier, P. Sechet, Ch. Boyer, Bubbly flow through fixed beds:micro-scale experiments in the dilute regime and modelling, AICHE J. 52(11) (2006) 3722-3743. [35] M.H. Al-Dahhan, H. Al-Bazzaz, V. Alexander, A. Toukan, Recent advances on the hydrodynamics of two-phase flow moving bed for catalytic hydrotreating:Experimentation and computing investigations, The 10th International Symposium on Catalysis in Multiphase Reactors (CAMURE-10) and the 9th International Symposium on Multifunctional Reactors (ISMR-9), 2017, Qingdao. [36] S.O. Rastegar, T.Y. Gu, Empirical correlations for axial dispersion coefficient and Peclet number in fixed-bed columns, J. Chromatogr. A 1490(2017) 133-137. |