| 233 - 244 |
Kinetics of protein deposition and replacement from a shear flow
Mandrusov E, Yang JD, Pfeiffer N, Vroman L, Puszkin E, Leonard EF |
| 245 - 254 |
Blowdown of pipelines carrying flashing liquids
Fairuzov YV |
| 255 - 262 |
Flow and axial dispersion simulation for traveling axisymmetric Taylor vortices
Howes T, Rudman M |
| 263 - 270 |
Influence of buoyancy forces on the flow of gases through packed beds at elevated pressures
Benneker AH, Kronberg AE, Westerterp KR |
| 271 - 278 |
Quantitative characterization of mixing of dry powders in V-blenders
Brone D, Alexander A, Muzzio FJ |
| 279 - 293 |
Equation of state and radial distribution functions of FCC particles in a CFB
Gidaspow D, Huilin L |
| 294 - 309 |
Numerical simulation of intense reaction propagation in multiphase systems
Pape R, Gidaspow D |
| 310 - 322 |
Defect-free palladium membranes on porous stainless-steel support
Mardilovich PP, She Y, Ma YH, Rei MH |
| 323 - 331 |
Electrochemical membrane flue-gas desulfurization : K2SO4/V2O5 electrolyte
Schmidt DS, Winnick J |
| 332 - 340 |
Complete separation conditions for a local equilibrium TCC adsorption unit
Chiang AST |
| 341 - 360 |
Wavelet-based modulation in control-relevant process identification
Carrier JF, Stephanopoulos G |
| 361 - 371 |
Safety verification using a hybrid knowledge-based mathematical programming framework
Srinivasan R, Dimitriadis VD, Shah N, Venkatasubramanian V |
| 372 - 387 |
Continuously stirred decanting reactor : Operability and stability considerations
Khinast J, Luss D, Harold MP, Ostermaier JJ, McGill R |
| 388 - 393 |
Detrimental influence of excessive fractionation on reactive distillation
Sneesby MG, Tade MO, Datta R, Smith TN |
| 394 - 404 |
Runaway limits for adiabatic packed-bed catalytic reactors
Christoforatou EL, Balakotaiah V, West DH |
| 405 - 415 |
Role of water in formic acid decomposition
Akiya N, Savage PE |
| 416 - 426 |
Miscibilization of reactive polymers during early-stage spinodal decomposition
Yashin VV, Spontak RJ |
| 427 - 441 |
Mathematical model of a continuous industrial high-impact polystyrene process
Estenoz DA, Meira GR, Gomez N, Oliva HM |
| 442 - 451 |
Morphology development in shear flows of straight and folded molten fibers
Zhang DF, Zumbrunnen DA, Liu YH |
| 452 - 464 |
Compositional variation in hydrocarbon reservoirs with natural convection and diffusion
Riley MF, Firoozabadi A |
| 465 - 473 |
Comparison of converging and diverging radial flow for measuring cell adhesion
Goldstein AS, DiMilla PA |
| 474 - 476 |
Quick analysis of enantioselectivity by a chromatographic reactor
Wu JY |
| 477 - 483 |
Novel photocatalytic reactor for water purification
Ray AK, Beenackers AACM |
| 484 - 490 |
Measured and modeled superficial flow profiles in packed beds with liquid flow
Giese M, Rottschafer K, Vortmeyer D |
| 491 - 494 |
Effect of gas adsorption on defluidization after switching fluidizing gases
Kai T, Kamei T, Takahashi T |
| 495 - 498 |
Structural ratio for predicting the voidage of binary particle mixtures
Finkers HJ, Hoffmann AC |
| 499 - 500 |
Untitled
Epstein N, Grace JR, Zhang JP |
| 500 - 501 |
Untitled - Reply
Briens LA, Briens CL, Hay J, Margaritis A |
