| 933 - 940 |
A heuristic approach for solution of MINLP problem for production scheduling in preemptive mode
Yuceer M, Berber R |
| 941 - 947 |
Generation of nanometer-scale crystals of hydrophobic compound from aqueous solution
Maeda K, Hayashi A, Iimura K, Suzuki M, Hirota M, Asakuma Y, Fukui K |
| 949 - 957 |
Cooling and seeding effect on supersaturation and final crystal size distribution (CSD) of ammonium sulphate in a batch crystallizer
Hojjati H, Rohani S |
| 959 - 968 |
Monitoring slurry-loop reactors for early detection of hydrodynamic instabilities
Stienstra GJ, Nijenhuis J, Kroezen T, van den Bleek CM, van Ommen JR |
| 969 - 977 |
A TSA process with indirect heating and cooling: parametric analysis and scaling-up to practical sizes
Bonjour J, Clausse M, Meunier F |
| 979 - 986 |
Effect of process parameters on bitumen emulsions
Gingras JP, Tanguy PA, Mariotti S, Chaverot P |
| 987 - 992 |
Deactivation-influenced propane steam reforming: reactor analysis and parameter estimation
Hardiman KM, Trujillo FJ, Adesina AA |
| 993 - 998 |
Determination of representative and instantaneous process side heat transfer coefficients in agitated vessel using heat flux sensors
Delaplace G, Demeyre JF, Guerin R, Debreyne P, Leuliet JC |
| 999 - 1004 |
Simulation and analysis of an industrial water desalination plant
Abbas A |
| 1005 - 1011 |
Optimization of dissolution of ulexite in water saturated with sulphur dioxide
Kucuk O, Kocakerim MM |
| 1013 - 1017 |
Catalytic oxidation of the dye wastewater with hydrogen peroxide
Qiu ZM, He YB, Liu XC, Yu SX |
| 1019 - 1027 |
Separation characteristics of acetic acid-water mixtures by pervaporation using poly(vinyl alcohol) membranes modified with malic acid
Isiklan N, Sanli O |
| 1029 - 1038 |
Activated carbon monolith of high thermal conductivity for adsorption processes improvement Part A: Adsorption step
Menard D, Py X, Mazet N |
| 1039 - 1046 |
Sulphur dioxide absorption in air-lift-tube absorbers by sodium citrate buffer solution
Bekassy-Molnar E, Marki E, Majeed JG |
