495 - 501 |
Application of a fully thermally coupled distillation column for fractionation process in naphtha reforming plant Lee JY, Kim YH, Hwang KS |
503 - 509 |
Effects of liquid property on gas holdup and mass transfer in co-current downflow contacting column Akosman C, Orhan R, Dursun G |
511 - 522 |
Comparison of different models of cyclone prediction performance for various operating conditions using a general software Altmeyer S, Mathieu V, Jullemier S, Contal P, Midoux N, Rode S, Leclerc JP |
523 - 531 |
A new computational technique for the estimation of sterilization time in canned food Farid M, Ghani AGA |
533 - 539 |
Isobutene hydration in a countercurrent flow fixed bed reactor Zhang CM, Adesina AA, Wainwright MS |
541 - 545 |
Vapor-liquid phase behavior of the binary systems containing supercritical carbon dioxide Li ZY, Wang W, Zhang XD, Liu XW, Hu DP, Xia YJ |
547 - 553 |
Effect of surfactant on the characteristics of a droplet-laden jet Ariyapadi S, Balachandar R, Berruti F |
555 - 558 |
Long-term performance of an industrial water desalination plant Al-Bastaki N, Abbas A |
559 - 570 |
Hybrid neural network-prior knowledge model in temperature control of a semi-batch polymerization process Ng CW, Hussain MA |
571 - 573 |
The effect of vessel diameter on time dependent gas hold-up variations in highly viscous impeller agitated liquids Khare AS, Niranjan K |
575 - 579 |
Influence of scale on the volumetric mass transfer coefficients in bubble columns Vandu CO, Krishna R |