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Results: 1-11 |
Results: 11
Calculating distillation efficiencies of multicomponent i-butane/n-butane column
Authors: Ilme, J Klemola, K Aittamaa, J Nystrom, L
Citation: J. Ilme et al., Calculating distillation efficiencies of multicomponent i-butane/n-butane column, CHEM ENG CO, 184, 2001, pp. 1-21
Dynamic simulation of the behaviour of pressure relief systems
Authors: Pokki, JP Hurme, M Aittamaa, J
Citation: Jp. Pokki et al., Dynamic simulation of the behaviour of pressure relief systems, COMPUT CH E, 25(4-6), 2001, pp. 793-798
Vapor-liquid equilibrium for the binary systems of methanol+2,4,4-trimethyl-1-pentene at 331 K and 101 kPa and methanol+2-methoxy-2,4,4-trimethylpentane at 333 K
Authors: Uusi-Kyyny, P Pokki, JP Aittamaa, J Liukkonen, S
Citation: P. Uusi-kyyny et al., Vapor-liquid equilibrium for the binary systems of methanol+2,4,4-trimethyl-1-pentene at 331 K and 101 kPa and methanol+2-methoxy-2,4,4-trimethylpentane at 333 K, J CHEM EN D, 46(5), 2001, pp. 1244-1248
Vapor liquid equilibrium for the binary systems of 2-methyl-2-propanol plus 2,4,4-trimethyl-1-pentene at 333 K and 348 K and 2-butanol plus 2,4,4-trimethyl-1-pentene at 360 K
Authors: Uusi-Kyyny, P Pokki, JP Aittamaa, J Liukkonen, S
Citation: P. Uusi-kyyny et al., Vapor liquid equilibrium for the binary systems of 2-methyl-2-propanol plus 2,4,4-trimethyl-1-pentene at 333 K and 348 K and 2-butanol plus 2,4,4-trimethyl-1-pentene at 360 K, J CHEM EN D, 46(3), 2001, pp. 686-691
Vapor-liquid equilibrium for the binary systems of 3-methylpentane+2-methyl-2-propanol at 331 K and+2-butanol at 331 K
Authors: Uusi-Kyyny, P Pokki, JP Aittamaa, J Liukkonen, S
Citation: P. Uusi-kyyny et al., Vapor-liquid equilibrium for the binary systems of 3-methylpentane+2-methyl-2-propanol at 331 K and+2-butanol at 331 K, J CHEM EN D, 46(3), 2001, pp. 754-758
Appropriate simplifications in calculation of mass transfer in a multicomponent rate-based distillation tray model
Authors: Alopaeus, V Aittamaa, J
Citation: V. Alopaeus et J. Aittamaa, Appropriate simplifications in calculation of mass transfer in a multicomponent rate-based distillation tray model, IND ENG RES, 39(11), 2000, pp. 4336-4345
Novel equipment for testing catalytic cracking and catalyst regeneration with short contact times
Authors: Lipiainen, K Hagelberg, P Aittamaa, J Eilos, I Hiltunen, J Niemi, VM Krause, AOI
Citation: K. Lipiainen et al., Novel equipment for testing catalytic cracking and catalyst regeneration with short contact times, APP CATAL A, 183(2), 1999, pp. 411-421
Approximate high flux corrections for multicomponent mass transfer models and some explicit methods
Authors: Alopaeus, V Aittamaa, J Norden, HV
Citation: V. Alopaeus et al., Approximate high flux corrections for multicomponent mass transfer models and some explicit methods, CHEM ENG SC, 54(19), 1999, pp. 4267-4271
An integrated tool for synthesis and design of reactive distillation
Authors: Kenig, E Jakobsson, K Banik, P Aittamaa, J Gorak, A Koskinen, M Wettmann, P
Citation: E. Kenig et al., An integrated tool for synthesis and design of reactive distillation, CHEM ENG SC, 54(10), 1999, pp. 1347-1352
Modelling of speciality chemicals production in liquid-liquid reactors - Acase study: synthesis of diols
Authors: Lundstrom, L Salmi, T Lehtonen, J Lindfors, LP Toppinen, S Aittamaa, J
Citation: L. Lundstrom et al., Modelling of speciality chemicals production in liquid-liquid reactors - Acase study: synthesis of diols, CHEM ENG SC, 54(1), 1999, pp. 1-18
Application of dynamic pressure probe technique to characterize a circulating fluidized bed
Authors: Parssinen, JH Hagelberg, P Eilos, I Aittamaa, J
Citation: Jh. Parssinen et al., Application of dynamic pressure probe technique to characterize a circulating fluidized bed, CAN J CH EN, 77(2), 1999, pp. 299-304
Risultati: 1-11 |