83 - 88 |
Modelling and simulation of the continuous power cable processing Kosar V, Gomzi Z, Sintic K |
89 - 98 |
Power consumption, mixing time, heat and mass transfer measurements for liquid vessels that are mixed using reciprocating multiplates agitators Masiuk S, Rakoczy R |
99 - 106 |
Marigold (Calendula officinalis L.) oleoresin: Solubility in SC-CO2 and composition profile Danielski L, Campos LMAS, Bresciani LFV, Hense H, Yunes RA, Ferreira SRS |
107 - 118 |
MINLP optimization of butyl acetate synthesis Gangadwala J, Kienle A |
119 - 126 |
WGS reaction in a membrane reactor using a porous stainless steel supported silica membrane Brunetti A, Barbieri G, Drioli E, Lee KH, Sea B, Lee DW |
127 - 138 |
Identification of hydrodynamics characteristics in bubble columns through analysis of acoustic sound measurements - Influence of the liquid phase properties Al-Masry WA, Ali EM |
139 - 149 |
Influence of operating conditions and design parameters on hydrodynamics and mass transfer in an emulsion loop-venturi reactor Gourich B, El Azher N, Vial C, Soulami MB, Ziyad M, Zoulalian A |
150 - 158 |
T-junction separation modelling in gas-liquid two-phase flow Margaris DP |
159 - 164 |
Oxidative dissolution of cobalt oxalate and manganese oxalate in acetic acid solutions Zhu ZQ, Zhang HM, Lu ZH, Chen D |
165 - 174 |
Catalytic and thermal decomposition of ionic liquid monopropellants using a dynamic reactor. Comparison of powder and sphere-shaped catalysts Amariei D, Courtheoux L, Rossignol S, Kappenstein C |