Effect of the catalyst pore structure on fixed-bed reactor performance of partial oxidation of n-butane: A simulation study
Tài liệu tham khảo
Ali, 2014, Maleic anhydride production in a cross-flow reactor: a comparative study, Can. J. Chem. Eng., 92, 876, 10.1002/cjce.21951
Alonso, 2001, Butane partial oxidation in an externally fluidized bed-membrane reactor, Catal. Today, 67, 151, 10.1016/S0920-5861(01)00307-8
Anastasov, 2002, A study of the influence of the operating parameters on the temperature of the hot spot in a fixed bed reactor, Chem. Eng. J., 86, 287, 10.1016/S1385-8947(01)00178-4
Benziger, 1997, New precursors to vanadium phosphorus oxide catalysts, Catal. Today, 33, 49, 10.1016/S0920-5861(96)00135-6
Brandstädter, 2007, Maleic anhydride from mixtures of n-butenes and n-butane: simulation of a production-cale nonisothermal fixed-bed reactor, Ind. Eng. Chem. Res., 46, 1475, 10.1021/ie061142q
Carreon, 2002, Macroporous vanadium phosphorus oxide phases displaying three-dimensional arrays of spherical voids, Chem. Mater., 14, 2670, 10.1021/cm0117376
Carreon, 2005, Synthesis of catalytic materials on multiple length scales, Catal. Today, 99, 137, 10.1016/j.cattod.2004.09.033
Cavani, 2006, The dilution of vanadyl pyrophosphate, catalyst for n-butane oxidation to maleic anhydride, with aluminum phosphate: unexpected reactivity due to the contribution of the diluting agent, Top. Catal., 38, 295, 10.1007/s11244-006-0028-3
Centi, 1993, Some prospects and priorities for future research on vanadyl pyrophosphate, Catal. Today, 16, 147, 10.1016/0920-5861(93)85015-R
Coppens, 2001, Synthesis of hierarchical porous silicas with a controlled pore size distribution at various length scales, Catal. Today, 69, 331, 10.1016/S0920-5861(01)00386-8
Diedenhoven, 2012, A model for the phosphorus dynamics of VPO catalysts during the selective oxidation of n-butane to maleic anhydride in a tubular reactor, Chem. Ing. Tech., 84, 517, 10.1002/cite.201100248
Dixon, 2012, Fixed bed catalytic reactor modelling-the radial heat transfer problem, Can. J. Chem. Eng., 90, 507, 10.1002/cjce.21630
Froment, 2011
Glaum, 2012, Resource-efficient alkane selective oxidation on new crystalline solids: searching for novel catalyst materials, Chem. Ing. Tech., 84, 1766, 10.1002/cite.201200078
Guettel, 2010, Assessment of micro-structured fixed-bed reactors for highly exothermic gas-phase reactions, Chem. Eng. Sci., 65, 1644, 10.1016/j.ces.2009.11.002
Guliants, 2000, 130, 1721
Hegedus, 1980, Catalyst pore structures by constrained nonlinear optimization, Ind. Eng. Chem. Prod. Res. Dev., 19, 533, 10.1021/i360076a010
Hunt, 1988, Non-Darcian convection in cylindrical packed beds, J. Heat Transf., 110, 378, 10.1115/1.3250495
Hutchings, 2004, Vanadium phosphate: a new look at the active components of catalysts for the oxidation of butane to maleic anhydride, J. Mater. Chem., 14, 3385, 10.1039/b404610m
Jakobsen, 2014
Johnson, 1965, Pore structure and gaseous diffusion in solid catalysts, J. Catal., 4, 248, 10.1016/0021-9517(65)90015-1
Keil, 1999, Diffusion and reaction in porous networks, Catal. Today, 53, 245, 10.1016/S0920-5861(99)00119-4
Kleiber, 2010, D1 calculation methods for thermophysical properties, 119
Liu, 2013, Templated synthesis of nanostructured materials, Chem. Soc. Rev., 42, 2610, 10.1039/C2CS35369E
Luss, 1990, Reaction engineering of advanced ceramic materials, Chem. Eng. Sci., 45, 1979, 10.1016/0009-2509(90)80072-M
Marín, 2012, Fixed bed membrane reactors for WGSR-based hydrogen production, Int. J. Hydrog. Energy, 37, 4997, 10.1016/j.ijhydene.2011.12.027
Marín, 2010, Analysis of a fluidized bed membrane reactor for butane partial oxidation to maleic anhydride: 2d modelling, Chem. Eng. Sci., 65, 3538, 10.1016/j.ces.2010.02.041
Rieckmann, 1999, Simulation and experiment of multicomponent diffusion and reaction in three-dimensional networks, Chem. Eng. Sci., 54, 3485, 10.1016/S0009-2509(98)00480-1
Schunk, 2008, Oxyfunctionalization of Alkanes, 3400
Sharma, 1991, Kinetics and fixed-bed reactor modeling of butane oxidation to maleic anhydride, AIChE J., 37, 39, 10.1002/aic.690370103
Solsvik, 2012, Impacts on the reactor performance of intra-particle multicomponent mass diffusion limitations: Knudsen diffusion, Energy Proc., 26, 116, 10.1016/j.egypro.2012.06.017
Solsvik, 2012, A survey of multicomponent mass diffusion flux closures for porous pellets: mass and molar forms, Transp. Porous Media, 93, 99, 10.1007/s11242-012-9946-7
Solsvik, 2013, Multicomponent mass diffusion in porous pellets: effects of flux models on the pellet level and impacts on the reactor level. Application to methanol synthesis, Can. J. Chem. Eng., 91, 66, 10.1002/cjce.20680
Stitt, 2015, How good is your model?, Johnson Matthey Technol. Rev., 59, 74, 10.1595/205651315X686804
Szekely, 1971, A structural model for gas–solid reactions with a moving boundary-II, Chem. Eng. Sci., 26, 1901, 10.1016/0009-2509(71)86033-5
Trifirò, 2014, How the yield of maleic anhydride in n-butane oxidation, using VPO catalysts, was improved over the years, Top. Catal., 57, 1188, 10.1007/s11244-014-0285-5
Tsotsas, 2010, M7 heat and mass transfer in packed beds with fluid flow, 1327
Wakao, 1962, Diffusion in catalyst pellets, Chem. Eng. Sci., 17, 825, 10.1016/0009-2509(62)87015-8
Wakao, 1964, Diffusion and reaction in porous catalysts, Ind. Eng. Chem. Fundam., 3, 123, 10.1021/i160010a007
Wei, 2011, Catalyst designs to enhance diffusivity and performance I: concepts and analysis, Chem. Eng. Sci., 66, 4382, 10.1016/j.ces.2011.02.010
Wellauer, 1986, Optimal policies in maleic anhydride production through detailed reactor modelling, Chem. Eng. Sci., 41, 765, 10.1016/0009-2509(86)87156-1
Winterberg, 2000, A simple and coherent set of coefficients for modelling of heat and mass transport with and without chemical reaction in tubes filled with spheres, Chem. Eng. Sci., 55, 967, 10.1016/S0009-2509(99)00379-6
Zou Y.A., R.P., 1996. Wall effect on the packing of cylindrical particles. Chem. Eng. Sci. 51 (7) 1177–1180. doi:10.1016/S0009-2509(96)80017-0. URL 〈http://linkinghub.elsevier.com/retrieve/pii/S0009250996800170〉.