1 - 11 |
Fabrication and characterization of novel hollow fiber catalytic packing of PFSA-PES-ZrO2 (shell)-TiO2 (core) solid superacid via wet-spinning method Ji CH, Xue SM, Xu ZL, Ma XH |
12 - 20 |
Coupled gel spreading and diffusive transport models describing microbicidal drug delivery Funke C, MacMillan K, Ham AS, Szeri AJ, Katz DF |
21 - 25 |
Sensitivity of chemical-looping combustion to particle reaction kinetics Schnellmann MA, Scott SA, Williams G, Dennis JS |
26 - 34 |
Mixing performance evaluation of additive manufactured milli-scale reactors Woldemariam M, Filimonov R, Purtonen T, Sorvari J, Koiranen T, Eskelinen H |
35 - 44 |
In-situ grown molybdenum sulfide on TiO2 for dye-sensitized solar photocatalytic hydrogen generation Malekshoar G, Ray AK |
45 - 54 |
Prediction of conductive heating time scales of particles in a rotary drum Emady HN, Anderson KV, Borghard WG, Muzzio FJ, Glasser BJ, Cuitino A |
55 - 64 |
Investigation of the influence of viscoelastic behaviour on the agitation of non-Newtonian fluid flow Reviol T, Kluck S, Genuit F, Reim V, Bohle M |
65 - 83 |
Segregation and dispersion of binary solids in liquid fluidised beds: A CFD-DEM study Peng ZB, Joshi JB, Moghtaderi B, Khan MS, Evans GM, Doroodchi E |
84 - 94 |
Bubble swarm rise velocity in fluidized beds Puncochar M, Ruzicka MC, Simcik M |
95 - 108 |
PAT-based design of agrochemical co-crystallization processes: A case-study for the selective crystallization of 1:1 and 3:2 co-crystals of p-toluenesulfonamideitriphenylphosphine oxide Powell KA, Croker DM, Rielly CD, Nagy ZK |
109 - 115 |
Mass transfer into a spherical bubble Saboni A, Alexandrova S, Karsheva M, Gourdon C |
116 - 126 |
Online in situ viscosity determination in stirred tank reactors by measurement of the heat transfer capacity Wunderlich M, Trampnau PP, Lopes EF, Buchs J, Regestein L |
127 - 139 |
Insights into the hydrodynamic properties of slurry flow in a tubular photocatalytic reactor by PIV combined with LSIA Geng JF, Wang YC, Hu XW, Jing DW |
140 - 150 |
A new turbulence-induced theoretical breakage kernel in the context of the population balance equation Das SK |
151 - 162 |
Influence of orifice type and wetting properties on bubble formation at bubble column reactors Huber M, Dobesch D, Kunz P, Hirschler M, Nielsen U |
163 - 171 |
The flow inside shaking flasks and its implication for mycelial cultures Palacios-Morales C, Aguayo-Vallejo JP, Trujillo-Roldan MA, Zenit R, Ascanio G, Cordova-Aguilar MS |
172 - 185 |
Numerical simulation of 3D hollow-fiber vacuum membrane distillation by computational fluid dynamics Zhang YG, Peng YL, Ji SL, Wang SB |
186 - 198 |
The shape and behaviour of a granular bed in a rotating drum using Eulerian flow fields obtained from PEPT Morrison AJ, Govender I, Mainza AN, Parker DJ |
199 - 212 |
Development of a gas-solid drag law for clustered particles using particle-resolved direct numerical simulation Mehrabadi M, Murphy E, Subramaniam S |
213 - 226 |
An integrated two-step Fr 13 synthesis - demonstrated with membrane fouling in combined ultrafiltration-osmotic distillation (UF-OD) for concentrated juice Zou W, Davey KR |
227 - 238 |
Numerical analysis of gasification and emission characteristics of a two-stage entrained flow gasifier Zhang B, Ren ZY, Shi SP, Yan S, Fang F |
239 - 247 |
Using microchannels to visually investigate the formation and dissolution of acrylonitrile droplets in a bio-hydration system Li JH, Chen Y, Guo MZ, Wang YJ, Xu JH, Luo GS, Yu HM |
248 - 254 |
First investigation of modified poly(2-vinyl-4,4-dimethylazlactone)s as kinetic hydrate inhibitors Ree LHS, Kelland MA, Roth PJ, Batchelor R |
255 - 266 |
Implementation of an improved bubble breakup model for TFM-PBM simulations of gas-liquid flows in bubble columns Guo XF, Zhou Q, Li J, Chen CX |
267 - 279 |
Experimental study on drag reduction performance of surfactant flow in longitudinal grooved channels Huang CH, Liu DJ, Wei JJ |
280 - 292 |
Vacuum powder feeding and dispersion analysis for a solar thermochemical drop-tube reactor Brkic M, Koepf E, Alxneit I, Meier A |
293 - 300 |
Controlled formation and coalescence of paramagnetic ionic liquid droplets under magnetic field in coaxial microfluidic devices Huang JP, Ge XH, Xu JH, Luo GS |
301 - 310 |
Modeling a production scale milk drying process: parameter estimation, uncertainty and sensitivity analysis Ferrari A, Gutierrez S, Sin G |
311 - 322 |
Forced convective transport of alumina-water nanofluid in micro-channels subject to constant heat flux Yang C, Peng KL, Nakayama A, Qiu T |
323 - 342 |
A heuristic approach based on a single-temperature-peak design principle for simultaneous optimization of water and energy in fixed flowrate systems Xie WN, Hou YL, Wang YX, Wang JT |
343 - 350 |
Prediction of vapor-liquid equilibria for mixtures of low boiling point compounds using Wong-Sandler mixing rule and EOS/G(E) model Espanani R, Miller A, Jacoby W |
351 - 369 |
An improved Front-Tracking technique for the simulation of mass transfer in dense bubbly flows Roghair I, Annaland MV, Kuipers JAM |
370 - 380 |
Overproduction of squalene synergistically downregulates ethanol production in Saccharomyces cerevisiae Rasool A, Ahmed MS, Li C |
381 - 391 |
Investigation of bubble swarm drag at elevated pressure in a contaminated system Lane CD, Parisien V, Macchi A, Donaldson AA |
392 - 402 |
The optimal diffusion experiment Wolff L, Koss HJ, Bardow A |
403 - 412 |
Effects of harvesting cell density, medium depth and environmental factors on biomass and lipid productivities of Chlorella vulgaris grown in swine wastewater Amini H, Wang LJ, Shahbazi A |
413 - 425 |
Numerical modelling of flow and coupled mass and heat transfer in an adsorption process Cheng D, Peters EAJF, Kuipers JAM |
426 - 435 |
DQMOM approach for poly-dispersed soot formation processes in a turbulent non-premixed ethylene/air flame Kim T, Kim Y |
436 - 442 |
Flame aerosol synthesis of WO3/CeO2 from aqueous solution: Two distinct pathways and structure design Wang SH, Huang Y |
443 - 456 |
Filtered sub-grid constitutive models for fluidized gas-particle flows constructed from 3-D simulations Sarkar A, Milioli FE, Ozarkar S, Li TW, Sun X, Sundaresan S |
457 - 467 |
Engineering of the terpenoid pathway in Saccharomyces cerevisiae co-overproduces squalene and the non-terpenoid compound oleic acid Rasool A, Zhang GL, Li Z, Li C |
468 - 477 |
Electrochemical reduction of CO2 to methanol over MWCNTs impregnated with Cu2O Malik MI, Malaibari ZO, Atieh M, Abussaud B |
478 - 487 |
Liquid mixing dynamics in slurry stirred tanks based on electrical resistance tomography Carletti C, Montante G, De Blasio C, Paglianti A |
488 - 496 |
Model-based evaluation on simultaneous nitrate and arsenite removal in a membrane biofilm reactor Chen XM, Ni BJ |
497 - 506 |
Effects of the orifice to pipe diameter ratio on orifice flows Shan F, Liu ZC, Liu W, Tsuji Y |
507 - 515 |
Simulation and optimization of a 6-step dual-reflux VSA cycle for post-combustion CO2 capture Khurana M, Farooq S |
516 - 527 |
Experimental investigation on the breakup dynamics for bubble formation in viscous liquids in a flow-focusing device Lu YT, Fu TT, Zhu CY, Ma YG, Li HZ |
528 - 546 |
A PIV investigation of the effect of disperse phase fraction on the turbulence characteristics of liquid-liquid mixing in a stirred tank Liu NN, Wang W, Han JC, Zhang M, Angeli P, Wu CC, Gong J |
547 - 567 |
Unified Design of chromatographic processes with timed events: Separation of ternary mixtures Sainio T |
568 - 578 |
Flow pattern construction-based tubular heat transfer intensification using calculus of variations Guo K, Liu BT, Li X, Liu H, Liu CJ |
579 - 585 |
An analytical relation for the void fraction distribution in a fully developed bubbly flow in a vertical pipe Marfaing O, Guingo M, Lavieville J, Bois G, Mechitoua N, Merigoux N, Mimouni S |
586 - 590 |
Application of a new model based on oxygen balance to determine the oxygen uptake rate in mammalian cell chemostat cultures Rigual-Gonzalez Y, Gomez L, Nunez J, Vergara M, Diaz-Barrera A, Berrios J, Altamirano C |
591 - 605 |
Premixed combustion of methane-air mixture stabilized over porous medium: A 2D numerical study Giovannoni V, Sharma RN, Raine RR |
606 - 623 |
Flow in the thin film created by a coherent turbulent water jet impinging on a vertical wall Bhagat RK, Wilson DI |
624 - 635 |
Modeling and simulation of catalytic coal gasification in a pressurized jetting fluidized bed with embedded high-speed air jets Xia ZH, Chen CX, Bi JC, Li KZ, Jin YD |
636 - 648 |
Local gas holdup simulation and validation of industrial-scale aerated bioreactors Witz C, Treffer D, Hardiman T, Khinast J |
649 - 662 |
Integration of simulated moving bed chromatography and enzymatic racemization for the production of single enantiomers Fuereder M, Femmer C, Storti G, Panke S, Bechtold M |
663 - 673 |
Structure-transport relationships in disordered solids using integrated rate of gas sorption and mercury porosimetry Nepryahin A, Holt EM, Fletcher RS, Rigby SP |
674 - 677 |
Influence of solids concentration on diffusion behavior in sewage sludge and its digestate Zhang YY, Li H, Cheng YC, Liu C |
678 - 688 |
Butanol production by Clostridium acetobutylicum in a series of packed bed biofilm reactors Raganati F, Procentese A, Olivieri G, Russo ME, Gotz P, Salatino P, Marzocchella A |
689 - 698 |
Effects of particle size distribution on drying characteristics in a drum by XDEM: A case study Mohseni M, Peters B |
699 - 708 |
Flow regime and liquid solid mass transfer investigation in a designed porous structure using electrochemical micro-probes Altheimer M, Becker D, D'Aleo FP, von Rohr PR |
709 - 716 |
Evolution of sorptive and textural properties of CaO-based sorbents during repetitive sorption/regeneration cycles Bazaikin YV, Malkovich EG, Derevschikov VS, Lysikov AI, Okunev AG |
717 - 723 |
Ammoximation of cyclohexanone to cyclohexanone oxime using ammonium chloride as nitrogen source Xu YY, Yang QS, Li ZH, Gao LY, Zhang DS, Wang SF, Zhao XQ, Wang YJ |
724 - 735 |
Mechanistic modelling of water partitioning behaviour in hydrocyclone Banerjee C, Climent E, Majumder AK |
736 - 745 |
Influence of the carbon chain length of a sulfate-based surfactant on the formation of CO2, CH4 and CO2-CH4 gas hydrates Dicharry C, Diaz J, Torre JP, Ricaurte M |
746 - 753 |
Can cyclopentane hydrate formation be used to screen the performance of surfactants as LDHI anti-agglomerants at atmospheric pressure? Abojaladi N, Kelland MA |
754 - 766 |
The role of the Boudouard and water gas shift reactions in the methanation of CO or CO2 over Ni/gamma-Al2O3 catalyst Lim JY, McGregor J, Sederman AJ, Dennis JS |
767 - 782 |
Modification of kinetic theory of granular flow for frictional spheres, Part I: Two-fluid model derivation and numerical implementation Yang L, Padding JT, Kuipers JAM |
783 - 794 |
Modification of kinetic theory of granular flow for frictional spheres, part II: Model validation Yang L, Padding JT, Kuipers JAM |
795 - 795 |
The application of the parametric continuation method for determining steady state diagrams in chemical enginnering (vol 65, pg 5411, 2010) Berezowski M |