3865 - 3870 |
One-pot synthesis of dimethyl carbonate using ethylene oxide, methanol, and carbon dioxide under supercritical conditions Cui HY, Wang T, Wang FJ, Gu CR, Wang PL, Dai YY |
3871 - 3880 |
Synthesis and characterization of Cu-TiPILCs for selective catalytic reduction of NO by propylene in the presence of oxygen and H2O: Influence of the calcination temperature, the copper content, and the cation promoter (Ce/Ag) Valverde JL, Dorado F, Sanchez P, Asencio I, Romero A |
3881 - 3885 |
Kinetics of liquid-phase hydrogenation of furfuraldehyde to furfuryl alcohol over a Pt/C catalyst Vaidya PD, Mahajani VV |
3886 - 3892 |
Development of an empirical model for catalyst lifetime in isobutane/butene alkylation Kazemeini M, Sahebdelfar S, Khorasheh F, Badakhshan A |
3893 - 3899 |
Evaluation of polymer-supported rhodium catalysts in 1-octene hydroformylation in supercritical carbon dioxide Lopez-Castillo ZK, Flores R, Kani I, Fackler JP, Akgerman A |
3900 - 3913 |
A new phase-equilibrium model for simulating industrial nylon-6 production trains Seavey KC, Khare NP, Liu YA, Williams TN, Chen CC |
3914 - 3921 |
Coke aging and its incidence on catalyst regeneration Aguayo AT, Gayubo AG, Erena J, Atutxa A, Bilbao J |
3922 - 3928 |
Effect of heating rate on steam gasification of biomass. 1. Reactivity of char Fushimi C, Araki K, Yamaguchi Y, Tsutsumi A |
3929 - 3936 |
Effect of heating rate on steam gasification of biomass. 2. Thermogravimetric-mass spectrometric (TG-MS) analysis of gas evolution Fushimi C, Araki K, Yamaguchi Y, Tsutsumi A |
3937 - 3942 |
New experimental procedure for monitoring molecular weight breakdown during enzymatic degradation of polygalacturonic acid in continuous membrane reactors Gallifuoco A, Alfani F, Cantarella M, Viparelli P |
3943 - 3951 |
Kinetic study of the pyrolysis of H2S Binoist M, Labegorre B, Monnet F, Clark PD, Dowling NI, Huang M, Archambault D, Plasari E, Marquaire PM |
3952 - 3961 |
Valorization of polyolefins dissolved in light cycle oil over HY zeolites under fluid catalytic cracking unit conditions Arandes JM, Erena J, Bilbao J, Lopez-Valerio D, De la Puente G |
3962 - 3972 |
Process analysis for the production of diacetone alcohol via catalytic distillation Zheng YX, Ng FTT, Rempel GL |
3973 - 3981 |
On the mechanism of bubbling fluidized-bed combustion of gas oil Miccio F, Miccio M, Olivieri G, Silvestre A |
3982 - 3988 |
Single- and two-step emulsification to prepare a persistent multiple emulsion with a surfactant-polymer mixture Allouche J, Tyrode E, Sadtler V, Choplin L, Salager JL |
3989 - 4000 |
Structure and properties of Al-MSU-S mesoporous catalysts: Structure modification with increasing Al content Bagshaw SA, Jaenicke S, Khuan CG |
4001 - 4008 |
Attrition resistance of supports for iron Fischer-Tropsch catalysts Pham HN, Nowicki L, Xu J, Datye AK, Bukur DB, Bartholomew C |
4009 - 4018 |
Mathematical programming model for heat-exchanger network synthesis including detailed heat-exchanger designs. 1. Shell-and-tube heat-exchanger design Mizutani FT, Pessoa FLP, Queiroz EM, Hauan S, Grossmann IE |
4019 - 4027 |
Mathematical programming model for heat-exchanger network synthesis including detailed heat-exchanger designs. 2. Network synthesis Mizutani FT, Pessoa FLP, Queiroz EM, Hauan S, Grossmann IE |
4028 - 4042 |
Dynamic model of an industrial steam reformer and its use for multiobjective optimization Nandasana AD, Ray AK, Gupta SK |
4043 - 4049 |
Incorporating prior knowledge in a cubic spline approximation-application to the identification of reaction kinetic models Madar J, Abonyi J, Roubos H, Szeifert F |
4050 - 4054 |
Removal of Bi, Cd, Co, Cu, Fe, Ni, Pb, and Zn from an aqueous nitrate medium with bis(2-ethylhexyl)phosphoric acid impregnated kapok fiber Huynh HT, Tanaka M |
4055 - 4067 |
Separation of FTC-ester enantiomers using a simulated moving bed Xie Y, Hritzko B, Chin CY, Wang NHL |
4068 - 4076 |
Reactive extraction of zinc sulfate with bis(2-ethylhexyl)phosphoric acid in a short Kuhni column used in batch mode Mansur MB, Slater MJ, Biscaia EC |
4077 - 4083 |
Extraction equilibrium of zinc from sulfate solutions with bis(2-ethylhexyl)thiophosphoric acid Reis MTA, Carvalho JMR |
4084 - 4100 |
Aqueous absorption and oxidation of nitric oxide with oxone for the treatment of tail gases: Process feasibility, stoichiometry, reaction pathways, and absorption rate Adewuyi YG, Owusu SO |
4101 - 4108 |
Liquid-phase behavior during the cracking of asphaltenes Rahmani S, McCaffrey W, Elliott JAW, Gray MR |
4109 - 4122 |
Understanding wheat grain steaming Horrobin DJ, Landman KA, Ryder L |
4123 - 4131 |
Molecular modeling of fluid-phase equilibria using an isotropic multipolar potential Muller EA, Gelb LD |
4132 - 4142 |
New compositional models for calculating the viscosity of crude oils Elsharkawy AM, Hassan SA, Hashim YSK, Fahim MA |
4143 - 4145 |
Predictions of activity coefficients of nearly athermal binary mixtures using cubic equations of state Sacomani PA, Brignole EA |
4146 - 4146 |
Liquid-phase mixing in stirred vessels: Turbulent flow regime (vol 42, pg 2695, 2003) Nere NK, Patwardhan AW, Joshi JB |