[1] Wang, F., Qi, B., Wang, G. and Li, L., “
Methane steam reforming: Kinetics and modeling over coating catalyst in micro-channel reactor”, Int. J. Hydrog. Energy,
38 (14), 5693 (2013).
[2] Bej, B., Pradhan, N.C. and Neogi, S., “Production of hydrogen by steam reforming of methane over alumina supported nano-NiO/SiO2 catalyst”, Catal. Today, 207, 28 (2013).
[3] Song, C., Liu, Q., Ji, N., Kansha, Y. and Tsutsumi, A., “Optimization of steam methane reforming coupled with pressure swing adsorption hydrogen production process by heat integration”,
Appl. Energy,
154, 392 (2015).
[4]
Barelli, L.,
Bidini, G.,
Gallorini, F. and
Servili, S., “Hydrogen production through sorption-enhanced steam methane reforming and membrane technology: A review”,
Energy,
33 (4), 554 (2008).
[6] Hufton, J.R., Mayorga, S. and Sircar, S., “Sorption-enhanced reaction process for hydrogen production”, AIChE J., 45 (2), 248 (1999).
[7] Westerterp, K.R. and Kuczynski, M., “A model for a counter current gas-solid-solid trickle flow reactor for equilibrium reactions”, Chem. Eng. Sci., 42 (8), 1871 (1987).
[8] Ding, Y. and Alpay, E., “Equilibria and kinetics of CO2 adsorption on hydrotalcite adsorbent”, Chem. Eng. Sci., 55 (17), 3461 (2000).
[9] Gunduz, S. and Dogu, T., “Sorption enhanced ethanol reforming of ethanol over Ni- and Co-incorporated MCM-41 type catalysts”, Ind. Eng. Chem. Res., 51 (26), 8796 (2012).
[10] Bayat, M., Hamidi, M., Dehghani, Z., Rahimpour, M.R. and Shariati, A., “Hydrogen/methanol production in a novel multifunctional reactor with in situ adsorption: Modeling and optimization”, Int. J. Energy Res., 38 (8), 978 (2014).
[11] Dehghani, Z., Bayat, M. and Rahimpour, M.R., “Sorption-enhanced methanol synthesis: Dynamic modeling and optimization”, J. Taiwan. Inst. Chem. Eng., 45 (4), 1490 (2014).
[12] Bayat, M., Dehghani, Z. and Rahimpour, M.R., “Sorption-enhanced methanol synthesis in a dual-bed reactor: Dynamic modeling and simulation”, J. Taiwan. Inst. Chem. Eng., 45 (5), 2307 (2014).
[13] Van, D.D. and Staatsmijnen, D., French Pat. 978287, Lumburg, (1948).
[14] Fourth methanol documents of Lurgi. Zagros Petrochemical Complex in Assaluyeh, Iran.
[15] Xiu, G.H., Lia, P. and Rodrigues, A.E., “Sorption-enhanced reaction process with reactive regeneration”, Chem. Eng. Sci., 57 (18), 3893 (2002).
[16] Arab Aboosadi, Z., Rahimpour, M.R. and Jahanmiri. A., “A novel integrated thermally coupled configuration for methane-steam reforming and hydrogenation of nitrobenzene to aniline”, Int. J. Hydrog. Energy, 36 (4), 2960 (2011).
[17] Mbodji, M., Commenge, J.M., Falk, L., Di Marco, D., Rossignol, F., Prost, L., Valentin, S., Joly, R. and Del-Gallo, P., “
Steam methane reforming reaction process intensification by using a millistructured reactor: Experimental setup and model validation for global kinetic reaction rate estimation”, Chem. Eng. J.,
207-208, 871 (2012).
[18] Gosiewski, K., Bartmann, U., Moszczynski, M. and Mleczko, L., “
Effect of the intraparticle mass transport limitations on temperature profiles and catalytic performance of the reverse-flow reactor for the partial oxidation of methane to synthesis gas”, Chem. Eng. Sci.,
54 (20), 4589 (1999).
[19] Ranz, W.E. and Marshall. W.R., “Evaporation from drops II”, Chem. Eng. Prog., 48 (141), 173 (1952).
[20] Claus, G., Vergnes, F. and Le Goff, P., “Hydrodynamic study of gas and solid flow through a screen-packing”, Can. J. Chem. Eng., 54 (3), 143 (1976).
[21] Predojevic, Z.J., Lj Petrovic, D. and Dudukovic, A.P., “Pressure drop in a countercurrent gas−flowing solids−packed bed contactor”, Ind. Eng. Chem. Res., 40 (25), 6039 (2001).
[23] Nikacevic, N., Jovanovic, M. and Petkovska, M., “Enhanced ammonia synthesis in multifunctional reactor with in-situ adsorption”, Chem. Eng. Res. Des., 89 (4), 398 (2011).
[24] Spasic, A.M. and Hsu, J.P., Finely dispersed particles. micro-, nano-, and atto-engineering, CRC Press, Taylor & Francis, Boca Raton, p.371 (2006).
[25] Perry, R.H. and Green, D.W., Perry’s Chemical Engineers’ Handbook, 8th ed., McGraw-Hill, Singapore, p.420 (2008).
[26] Cussler, E.L., Diffusion: Mass transfer in fluid systems, Cambridge University Press, (1984).
[27] Wilke, C.R. “Estimation of liquid diffusion coefficients”, Chem. Eng. Prog., 45 (3), 218 (1949).
[28] Reid, R.C., Sherwood, T.K. and Prausnitz, J., The properties of gases and liquids, 3rd ed., McGraw-Hill, New York, (1977).
[29] Dudukovic, A.P., Nikacevic, N.M., Lj Petrovic, D. and Predojevic, Z.J. “Solids holdup and pressure drop in gas-flowing solids-fixed bed contactors”, Ind. Eng. Chem. Res., 42 (12), 2530 (2003).
[30] Perry, R.H. and Green, D.W., Perry’s Chemical Engineers’ Handbook, 8th ed., McGraw-Hill, Singapore, p.433 (2008).
[31] Hartig, F. and Keil, F.J. “Large-scale spherical fixed bed reactor: Modeling and optimization”, Ind. Eng. Chem. Res., 32 (3), 424 (1993).
[32] Rajesh, J.K., Gupta, S.K., Rangaiah, G.P. and Ray, A.K., “Multi-objective optimization of steam reformer performance using genetic algorithm”, Ind. Eng. Chem. Res., 39 (3), 706 (2000).
[33] Luo, X., Hu, J., Zhao, J., Zhang, B., Chen, Y. and Mo, S., “Multi-objective optimization for the design and synthesis of utility systems with emission abatement technology concerns”, Appl. Energy, 136, 1110 (2014).
[34] Deb, K., Pratap, A., Agarwal, S. and Meyarivan, T., “A Fast and elitist multi-objective genetic algorithm: NSGA-II”, IEEE Trans. Evol. Comput., 6 (2), 182 (2002).
[35] Bayat, M., Dehghani, Z. and Rahimpour, M.R., “Dynamic multi-objective optimization of industrial radial-flow fixed-bed reactor of heavy paraffin dehydrogenation in LAB plant using NSGA-II method”, J. Taiwan. Inst. Chem. Eng., 45 (4), 1474 (2014).