| 1321 - 1330 |
Volumetric oxygen mass transfer coefficient in an upflow cocurrent packed-bed bioreactor
Deront M, Samb FM, Adler N, Peringer P |
| 1331 - 1348 |
Batch extractive distillation : the process and the operational policies
Lelkes Z, Lang P, Moszkowicz P, Benadda B, Otterbein M |
| 1349 - 1366 |
Analytical solution of the energy-minimization multi-scale model for gas-solid two-phase flow
Xu GW, Li JH |
| 1367 - 1374 |
Permeation of acetone and isopropanol vapours through a porous alumina membrane
Assabumrungrat S, White DA |
| 1375 - 1385 |
A new model of velocity distribution of a single-phase fluid flowing in packed beds
Subagyo, Standish N, Brooks GA |
| 1387 - 1395 |
Supercritical carbon dioxide extraction of essential oils : Modeling and simulation
Goodarznia I, Eikani MH |
| 1397 - 1404 |
An iterative procedure to obtain the concentration dependency of the diffusion coefficient from the space-averaged concentration vs time
van der Zanden AJJ |
| 1405 - 1434 |
Hardware composites : A new conceptual tool for the analysis and optimisation of steam turbine networks in chemical process industries - Part I : Principles and construction procedure
Mavromatis SP, Kokossis AC |
| 1435 - 1461 |
Hardware composites : a new conceptual tool for the analysis and optimisation Of steam turbine networks in chemical process industries - Part II : application to operation and design
Mavromatis SP, Kokossis AC |
| 1463 - 1464 |
Boundary conditions for flow with dispersion
Barber JA, Perkins JD, Sargent RWH |
| 1465 - 1467 |
Modelling equilibrium isotherms for styrene-divinylbenzene ion exchange resins
Bricio OJ, Coca J, Sastre H |
| 1469 - 1470 |
Comments on transport phenomena in multi-particle systems
Epstein N |
| 1470 - 1471 |
Comments on trasport phenomena in multi-particle systems - Authors' reply
Mauret E, Renaud M |
