[1] T. Fronts, Patterns in Catalytic Systems Luss, Dan, Industrial & Engineering Chemistry Research 36 (1997) 2931-2944.
[2] M. Sheintuch, S. Shvartsman, Spatiotemporal patterns in catalytic reactors, AIChE journal 42 (1996) 1041-1068.
[3] R. Henda, K. Alhumaizi, Spatiotemporal patterns in a two-dimensional reaction-diffusion-convection system: Effect of transport parameters, Mathematical and Computer Modelling 36 (2002) 1361-1373.
[4] C.H. Bartholomew, R.J. Farrauto, Fundamentals of industrial catalytic processes, John Wiley & Sons2011.
[5] J.P. Sørensen, W.E. Stewart, Computation of forced convection in slow flow through ducts and packed beds—II velocity profile in a simple cubic array of spheres, Chemical Engineering Science 29 (1974) 819-825.
[6] T.F. McKenna, R. Spitz, D. Cokljat, Heat transfer from catalysts with computational fluid dynamics, AIChE Journal 45 (1999) 2392-2410.
[7] M. Dalman, J. Merkin, C. McGreavy, Fluid flow and heat transfer past two spheres in a cylindrical tube, Computers & fluids 14 (1986) 267-281.
[8] M. Nijemeisland, A.G. Dixon, Comparison of CFD simulations to experiment for convective heat transfer in a gas–solid fixed bed, Chemical Engineering Journal 82 (2001) 231-246.
[9] G. Aparicio-Mauricio, R.S. Ruiz, F. López-Isunza, C.O. Castillo-Araiza, A simple approach to describe hydrodynamics and its effect on heat and mass transport in an industrial wall-cooled fixed bed catalytic reactor: ODH of ethane on a MoVNbTeO formulation, Chemical Engineering Journal 321 (2017) 584-599.
[10] Y. Dong, B. Sosna, O. Korup, F. Rosowski, R. Horn, Investigation of radial heat transfer in a fixed-bed reactor: CFD simulations and profile measurements, Chemical Engineering Journal 317 (2017) 204-214.
[11] S.A. Logtenberg, A.G. Dixon, Computational fluid dynamics studies of fixed bed heat transfer.
[12] B. Partopour, A.G. Dixon, N‐butane partial oxidation in a fixed bed: A resolved particle computational fluid dynamics simulation, The Canadian Journal of Chemical Engineering (2018).
[13] M. Zhang, H. Dong, Z. Geng, Computational study of flow and heat transfer in fixed beds with cylindrical particles for low tube to particle diameter ratios, Chemical Engineering Research and Design 132 (2018) 149-161.
[14] T. Eppinger, K. Seidler, M. Kraume, DEM-CFD simulations of fixed bed reactors with small tube to particle diameter ratios, Chemical Engineering Journal 166 (2011) 324-331.
[15] H.P.A. Calis, J. Nijenhuis, B.C. Paikert, F.M. Dautzenberg, C.M. van den Bleek, CFD modelling and experimental validation of pressure drop and flow profile in a novel structured catalytic reactor packing, Chemical Engineering Science 56 (2001) 1713-1720.
[16] R.K. Reddy, J.B. Joshi, CFD modeling of pressure drop and drag coefficient in fixed beds: Wall effects, Particuology 8 (2010) 37-43.
[17] T. Atmakidis, E.Y. Kenig, CFD-based analysis of the wall effect on the pressure drop in packed beds with moderate tube/particle diameter ratios in the laminar flow regime, Chemical Engineering Journal 155 (2009) 404-410.
[18] S.J.P. Romkes, F.M. Dautzenberg, C.M. van den Bleek, H.P.A. Calis, CFD modelling and experimental validation of particle-to-fluid mass and heat transfer in a packed bed at very low channel to particle diameter ratio, Chemical Engineering Journal 96 (2003) 3-13.
[19] A.G. Dixon, M. Nijemeisland, E.H. Stitt, Systematic mesh development for 3D CFD simulation of fixed beds: Contact points study, Computers & Chemical Engineering 48 (2013) 135-153.
[20] A.G. Dixon, M.E. Taskin, M. Nijemeisland, E.H. Stitt, Wall-to-particle heat transfer in steam reformer tubes: CFD comparison of catalyst particles, Chemical Engineering Science 63 (2008) 2219-2224.
[21] A. Singhal, S. Cloete, S. Radl, R. Quinta-Ferreira, S. Amini, Heat transfer to a gas from densely packed beds of cylindrical particles, Chemical Engineering Science 172 (2017) 1-12.
[22] A.G. Dixon, M. Ertan Taskin, M. Nijemeisland, E.H. Stitt, Systematic mesh development for 3D CFD simulation of fixed beds: Single sphere study, Computers & Chemical Engineering 35 (2011) 1171-1185.
[23] A.G. Dixon, M. Nijemeisland, CFD as a design tool for fixed-bed reactors, Industrial & Engineering Chemistry Research 40 (2001) 5246-5254.
[24] A.G. Dixon, M. Nijemeisland, E.H. Stitt, CFD study of heat transfer near and at the wall of a fixed bed reactor tube: Effect of wall conduction, Industrial & engineering chemistry research 44 (2005) 6342-6353.
[25] F.S. Mirhashemi, S.H. Hashemabadi, S. Noroozi, CFD simulation and experimental validation for wall effects on heat transfer of finite cylindrical catalyst, International Communications in Heat and Mass Transfer 38 (2011) 1148-1155.
[26] A.H. Ahmadi Motlagh, S.H. Hashemabadi, 3D CFD simulation and experimental validation of particle-to-fluid heat transfer in a randomly packed bed of cylindrical particles, International Communications in Heat and Mass Transfer 35 (2008) 1183-1189.
[27] A.H. Ahmadi Motlagh, S.H. Hashemabadi, CFD based evaluation of heat transfer coefficient from cylindrical particles, International Communications in Heat and Mass Transfer 35 (2008) 674-680.
[28] F.S. Mirhashemi, S.H. Hashemabadi, Experimental and CFD study of wall effects on orderly stacked cylindrical particles heat transfer in a tube channel, International Communications in Heat and Mass Transfer 39 (2012) 449-455.
[29] M. Zare, S.H. Hashemabadi, Experimental study and CFD simulation of wall effects on heat transfer of an extrudate multi-lobe particle, International Communications in Heat and Mass Transfer 43 (2013) 122-130.
[30] R. Zou, A. Yu, The packing of spheres in a cylindrical container: the thickness effect, Chemical Engineering Science 50 (1995) 1504-1507.
[31] Y. Matros, Unsteady processes in catalytic reactors, (1985).
[32] S.B. Jaffe, Hot spot simulation in commercial hydrogenation processes, Industrial & Engineering Chemistry Process Design and Development 15 (1976) 410-416.
[33] A. Benneker, A.E. Kronberg, K. Westerterp, Influence of buoyancy forces on the flow of gases through packed beds at elevated pressures, AIChE journal 44 (1998) 263-270.
[34] D. Nguyen, V. Balakotaiah, Flow maldistributions and hot spots in down-flow packed bed reactors, Chemical engineering science 49 (1994) 5489-5505.
[35] O. Korup, S. Mavlyankariev, M. Geske, C.F. Goldsmith, R. Horn, Measurement and analysis of spatial reactor profiles in high temperature catalysis research, Chemical Engineering and Processing: Process Intensification 50 (2011) 998-1009.
[36] O. Bilous, N.R. Amundson, Chemical reactor stability and sensitivity: II. Effect of parameters on sensitivity of empty tubular reactors, AIChE Journal 2 (1956) 117-126.
[37] S.J. Park, J.W. Bae, Y.J. Lee, K.S. Ha, K.W. Jun, P. Karandikar, Deactivation behaviors of Pt or Ru promoted Co/P-Al2O3 catalysts during slurry-phase Fischer–Tropsch synthesis, Catalysis Communications 12 (2011) 539-543.
[38] H. Aligolzadeh, A. Jebreili Jolodar, R. Mohammadikhah, CFD analysis of hot spot formation through a fixed bed reactor of Fischer-Tropsch synthesis, Cogent Engineering 2 (2015).
[39] C. Bendjaouahdou, M.H. Bendjaouahdou, Control of the hot spot temperature in an industrial SO2 converter, Energy Procedia 36 (2013) 428-443.
[40] C. Barkelew, B. Gambhir, Stability of trickle-bed reactors, ACS symposium series, Oxford University Press, 1984, pp. 61-81.
[41] E. Wicke, H. Onken, Periodicity and chaos in a catalytic packed bed reactor for CO oxidation, Tenth International Symposium on Chemical Reaction Engineering, Elsevier, 1988, pp. 2289-2294.
[42] E. Wicke, H. Onken, Bifurcation, periodicity and chaos by thermal effects in heterogeneous catalysis, From Chemical to Biological Organization, Springer1988, pp. 68-82.
[43] G. Boreskov, Y. Matros, O. Klenov, V. Logovkoi, V. Lakhmostov, Local nonuniformities in a catalyst bed, Dokl. Akad. Nauk SSSR, 1981, pp. 1418.
[44] K.M. Ng, R. Gani, K. Dam-Johansen, Chemical product design: towards a perspective through case studies, Elsevier2006.