1 - 16 |
Membrane separation of chlorine gas Lindbrathen A, Hagg MB |
17 - 28 |
Flow-through catalytic membrane reactors-Principles and applications Westermann T, Melin T |
29 - 37 |
Pressure drop excess in the flow of viscoelastic liquids through fixed beds of particles Bendova H, Siska B, Machac I |
38 - 47 |
Kinetics and thermodynamics studies of chromium(VI) ions adsorption onto activated carbon from aqueous solutions Barkat M, Nibou D, Chearouche S, Mellah A |
48 - 58 |
Intensification of desorption processes by use of microwaves-An overview of possible applications and industrial perspectives Cherbanski R, Molga E |
59 - 67 |
Experiments in a large-scale venturi scrubber Part I: Pressure drop Silva AM, Teixeira JCF, Teixeira SFCF |
68 - 83 |
Ink drop motion in wide-format printers I. Drop flow from Drop-On-Demand (DOD) printing heads Link N, Semiat R |
84 - 91 |
Ink drop motion in wide-format printers II. Airflow investigation Link N, Lampert S, Gurka R, Liberzon A, Hetsroni G, Semiat R |
92 - 100 |
Recrystallization of pharmaceuticals using the batch supercritical anti-solvent process Su CS, Tang M, Chen YP |
101 - 110 |
Prediction of flow regimes transitions in bubble columns using passive acoustic measurements Ajbar A, Al-Masry W, Ali E |
111 - 119 |
Theoretical and experimental studies of membrane extraction of Cu2+ with D2EHPA through rectangular conduits Guo JJ, Ho CD |
120 - 125 |
The Gaussian spectral pressure distribution applied to a fluidized bed Parise MR, Kurka PRG, Taranto OP |
126 - 134 |
Experiment on particle mixing in flat-bottom spout-fluid bed Zhang Y, Jin BS, Zhong WQ |
135 - 144 |
Dynamic modeling and simulation of a CO2 absorber column for post-combustion CO2 capture Kvamsdal HM, Jakobsen JP, Hoff KA |
145 - 151 |
CFD simulation of hydrodynamics of valve tray Li XG, Liu DX, Xu SM, Li H |
152 - 164 |
Thermodynamic equilibrium calculations concerning the removal of heavy metals from sewage sludge ash by chlorination Fraissler G, Joller M, Mattenberger H, Brunner T, Obernberger I |
165 - 177 |
Effect of circulating fluidized bed reactor riser geometries on chemical reaction rates by using CFD simulations Chalermsinsuwan B, Kuchonthara P, Piumsomboon P |
178 - 186 |
Experimental analysis of bubble velocity in a rotating fluidized bed Nakamura H, Iwasaki T, Watano S |
187 - 194 |
Physical and chemical characteristics of waste activated sludge treated ultrasonically Feng X, Lei HY, Deng JC, Yu Q, Li HL |
195 - 202 |
Enhancement of tapioca starch separation with a hydrocyclone: effects of apex diameter, feed concentration, and pressure drop on tapioca starch separation with a hydrocyclone Saengchan K, Nopharatana A, Songkasiri W |
203 - 208 |
Extraction of solanesol from tobacco (Nicotiana tobaccum L.) leaves by bubble column Zhao CJ, Zu YG, Li CY |
209 - 216 |
Pressure drop characteristics of a multi-stage counter-current fluidized bed reactor for control of gaseous pollutants Mohanty CR, Meikap BC |
217 - 223 |
A new approach to the analysis of heat and mass transfer in drying and frying of food products Farid M, Kizilel R |
224 - 228 |
Stage efficiency of Hanson mixer-settler extraction column Torab-Mostaedi M, Safdari J, Moosavian MA, Maragheh MG |
229 - 238 |
Simplified design methods of reverse flow catalytic combustors for the treatment of lean hydrocarbon-air mixtures Marin P, Ordonez S, Diez FV |
239 - 249 |
Case-based reasoning and TRIZ: A coupling for innovative conception in Chemical Engineering Robles GC, Negny S, Le Lann JM |
250 - 258 |
Reactive dividing wall distillation columns: Simulation and implementation in a pilot plant Hernandez S, Sandoval-Vergara R, Barroso-Munoz FO, Murrieta-Duenas R, Hernandez-Escoto H, Segovia-Hernandez JG, Rico-Ramirez V |
259 - 267 |
Comparison of macroscopic flow properties obtained by three methods of operation in a liquid-solid circulating fluidized bed Shilapuram V, Krishnaiah K, Sai PST |
268 - 278 |
General systems modeling of multi-phase batch crystallization from solution Borissova A |
279 - 287 |
Hydrodynamics of a gas-liquid-solid fluidized bed with hollow cylindrical particles Jena HM, Roy GK, Meikap BC |
288 - 295 |
Experimental measurement and numerical simulation for liquid flow velocity and local phase hold-ups in the riser of a GLSCFB Cao CQ, Liu MY, Wen JP, Guo QJ |
296 - 305 |
Mathematical modeling of microwave-assisted inert medium fluidized bed drying of cylindrical carrot samples Souraki BA, Andres A, Mowla D |
306 - 310 |
Effect of light cycles (night/day) on CO2 fixation and biomass production by microalgae in photobioreactors Jacob-Lopes E, Scoparo CHG, Lacerda LMCF, Franco TT |
311 - 320 |
Simulation of an industrial-scale process for the SCR of NOx based on the loop reactor concept Marin P, Fissore D, Barresi AA, Ordonez S |
321 - 328 |
Closed cross flow structures-Improving the heat transfer in fixed bed reactors by enforcing radial convection Schildhauer TJ, Newson E, Wokaun A |
329 - 332 |
An industrial view of process intensification Becht S, Franke R, Geisselmann A, Hahn H |
333 - 338 |
Pyrolysis property of pulverized coal in an entrained flow reactor during coal reburning Lu P, Xu SR, Zhu XM |
339 - 347 |
Simulation and optimization of a six-effect evaporator in a desalination process Khademi MH, Rahimpour MR, Jahanmiri A |
348 - 355 |
Measurement of liquid particle concentrations in a free jet flow Terfous A, Helmaoui M, Hazzab A, Ghenaim A |
356 - 363 |
Selection of systems for catalyst recovery by micellar enhanced ultrafiltration Schwarze M, Rost A, Weigel T, Schomacker R |
364 - 369 |
Extraction, dealcoholization and concentration of anthocyanin from red radish Patil G, Madhusudhan MC, Babu BR, Raghavarao KSMS |
370 - 379 |
Competitive adsorption of cadmium(II) and nickel(II) metal ions from aqueous solution onto rice husk ash Srivastava VC, Mall ID, Mishra IM |
380 - 388 |
Influence of dry and humid gaseous atmosphere on the thermal decomposition of calcium chloride and its impact on the remove of heavy metals by chlorination Fraissler G, Joller M, Brunner T, Obernberger I |
389 - 395 |
Cold model test and industrial applications of high geometrical area packings for separation intensification Li QS, Chang QL, Tian YM, Liu H |
396 - 407 |
Novel multi-staged radially cross-flow fluidized bed ion-exchange column Verma R, Srivastava G, Verma N |
408 - 423 |
Monitoring of the primary drying of a lyophilization process in vials Barresi AA, Pisano R, Fissore D, Rasetto V, Velardi SA, Vallan A, Parvis M, Galan M |
424 - 431 |
Experiments in large scale venturi scrubber Part II. Droplet size Silva AM, Teixeira JCF, Teixeira SFCF |
432 - 437 |
Process intensification of hydrogenation reactions using cavitation: Modelling the effect of solvent and catalyst Sharma A, Bapat PS, Gogate PR, Gastgar SN, Pandit AB |
438 - 445 |
One-step preparation method of multiple emulsions entrapping reactive agent in the liquid-liquid Couette-Taylor flow Dluska E, Markowska A |
446 - 451 |
Modeling of temperature gradients in packed-bed solid-state bioreactors Fanaei MA, Vaziri BM |
452 - 463 |
Prediction of flow profiles and interfacial phenomena for two-phase flow in coiled tubes Vashisth S, Nigam KDP |
464 - 469 |
Development of a fermentation process for production of calcium-L-lactate Gao MT, Hirata M, Toorisaka E, Hano T |
470 - 475 |
Direct entropy minimization applied to the production of propylene glycol Manzi J, Vianna R, Bispo H |
476 - 484 |
Instability of the phase front in the soils freezing process Bronfenbrener L |
485 - 492 |
Increasing PVC suspension polymerization productivity-An industrial application Tacidelli AR, Alves JJN, Vasconcelos LGS, Brito RP |
493 - 506 |
Generic modelling, design and optimization of industrial phosphoric acid production processes Papadopoulos AI, Seferlisa P |
507 - 514 |
Thermal stress-induced fragmentation of quartzite particles in a hot fluidized bed Liu JG, Jiang XM, Zhou LS, Wang H, Han XX |
515 - 523 |
Regeneration of CO2 from CO2-rich alkanolamines solution by using reduced thickness and vacuum technology: Regeneration feasibility and characteristic of thin-layer solvent Yan SP, Fang MX, Luo ZY, Cen KF |
524 - 531 |
Microwave drying kinetics of tomato pomace: Effect of osmotic dehydration Al-Harahsheh M, Al-Muhtaseb AH, Magee TRA |
532 - 537 |
Modeling aqueous heterogeneous photocatalytic degradation of organic pollutants with immobilized TiO2 Goetz V, Cambon JP, Sacco D, Plantard G |
538 - 548 |
Following of polymerization process of polyurethane spinning solutions in dimethylformamide by means of the power consumption Masiuk S, Rakoczy R |
549 - 553 |
Process intensification by combining ionic liquids and supercritical carbon dioxide applied to the design of Levodopa production Damen MR, Brand RW, Bloem SC, Pingen E, Steur K, Peters CJ, Witkamp GJ, Kroon MC |
554 - 559 |
Effect of microchannel aspect ratio on residence time distributions and the axial dispersion coefficient Aubin J, Prat L, Xuereb C, Gourdon C |
560 - 568 |
Selective dehydration of high-pressure natural gas using supersonic nozzles Karimi A, Abdi MA |
569 - 575 |
Laboratory differential simulation design method of pressure absorbers for carbonization of phenolate solution by carbon dioxide in coal-tar processing Linek V, Sinkule J, Moucha T, Rejl JF |
576 - 580 |
Hydrolysis of milk/whey lactose by beta galactosidase: A comparative study of stirred batch process and packed bed reactor prepared with calcium alginate entrapped enzyme Haider T, Husain Q |
581 - 585 |
An expression for the power consumption of in-line rotor-stator devices Kowalski AJ |