| 4369 - 4376 |
Practical and direct expressions of the heat of vaporization for mixtures
Akasaka R, Yamaguchi T, Ito T |
| 4377 - 4395 |
Conceptual design of single-feed hybrid reactive distillation columns
Dragomir RM, Jobson M |
| 4397 - 4407 |
Separation of carbon dioxide and methane in continuous countercurrent gas centrifuges
van Wissen R, Golombok M, Brouwers JJH |
| 4409 - 4421 |
An improved dynamic combined model for evaluating the mass transfer performances in extraction columns
Tang XJ, Luo GS, Wang JD |
| 4423 - 4430 |
Heat transfer phenomena in a solid oxide fuel cell: An analytical approach
Couteheris FA, Douvartzides SL, Tsiakaras PE |
| 4431 - 4451 |
A systematic approach to the synthesis and design of flexible site utility systems
Shang ZG, Kokossis A |
| 4453 - 4467 |
Numerical simulation of enhancement of mass transfer in the cathode electrode of a PEM fuel cell by magnet particles deposited in the cathode-side catalyst layer
Wang LB, Wakayama NI, Okada T |
| 4469 - 4484 |
Three-dimensional modeling of a circulating fluidized bed gasifier for sewage sludge
Petersen I, Werther J |
| 4485 - 4492 |
Three dimensional iron flow and heat transfer in the hearth of a blast furnace during tapping process
Cheng WT, Huang CN, Du SW |
| 4493 - 4507 |
Stability analysis of bubble columns: Predictions for regime transition
Bhole MR, Joshi JB |
| 4509 - 4523 |
Influence of operation parameters on the separation of mixtures by pervaporation and vapor permeation with inorganic membranes. Part 1: Dehydration of solvents
Sommer S, Melin T |
| 4525 - 4533 |
Influence of operation parameters on the separation of mixtures by pervaporation and vapor permeation with inorganic membranes. Part 2: Purely organic systems
Sommer S, Melin T |
| 4535 - 4556 |
Optimal design and steady-state operation of micro power generation employing fuel cells
Chachuat B, Mitsos A, Barton PI |
| 4557 - 4565 |
Nanomilling in stirred media mills
Stenger F, Mende S, Schwedes J, Peukert W |
| 4567 - 4580 |
The effects of particle and gas properties on the fluidization of Geldart A particles
Ye M, van der Hoef MA, Kuipers JAM |
| 4581 - 4592 |
Self- and mutual diffusion coefficient equation for pure fluids, liquid mixtures and polymeric solutions
Reis RA, Nobrega R, Oliveira JV, Tavares FW |
| 4593 - 4608 |
Macropore diffusion dusty-gas coefficient for pelletised zeolites from breakthrough experiments in the O-2/N-2 system
Todd RS, Webley PA |
| 4609 - 4622 |
Modelling of a rotary kiln for the pyrolysis of aluminium waste
Marias F, Roustan H, Pichat A |
| 4623 - 4633 |
A new technique for the determination of contact time distribution (CTD) from tracers experiments in heterogeneous systems
Tayakout-Fayolle M, Othman S, Jallut C |
| 4635 - 4645 |
Dynamic simulation of pressure swing adsorption system with the electrical network
Guan JY, Zeng R, Long CX, Hu XJ |
| 4647 - 4653 |
A new device for coating single particles under controlled conditions
Strom D, Karlsson S, Folestad S, Bjorn IN, Laurell T, Nilsson J, Rasmuson A |
| 4655 - 4657 |
Comments on the free rise of gas bubbles in non-Newtonian liquids
Karamanev D, Dewsbury K, Margaritis A |
| 4659 - 4660 |
A conceptually simple derivation of the Kelvin equation
Galvin KP |
