1 - 10 |
Interaction of bubbles rising inline in quiescent liquid Gumulya M, Utikar RP, Evans GM, Joshi JB, Pareek V |
1 - 10 |
Interaction of bubbles rising inline in quiescent liquid Gumulya M, Utikar RP, Evans GM, Joshi JB, Pareek V |
11 - 18 |
A combined CFD simulation of Plateau borders including films and transitional areas of liquid foams Anazadehsayed A, Naser J |
11 - 18 |
A combined CFD simulation of Plateau borders including films and transitional areas of liquid foams Anazadehsayed A, Naser J |
19 - 27 |
Film formation in a horizontal twin-shaft rotating disk reactor for polymer devolatilization Cheng WK, Wang JJ, Gu XP, Feng LF |
19 - 27 |
Film formation in a horizontal twin-shaft rotating disk reactor for polymer devolatilization Cheng WK, Wang JJ, Gu XP, Feng LF |
28 - 41 |
A coupled Volume of Fluid and Immersed Boundary Method for simulating 3D multiphase flows with contact line dynamics in complex geometries Patel HV, Das S, Kuipers JAM, Padding JT, Peters EAJF |
28 - 41 |
A coupled Volume of Fluid and Immersed Boundary Method for simulating 3D multiphase flows with contact line dynamics in complex geometries Patel HV, Das S, Kuipers JAM, Padding JT, Peters EAJF |
42 - 52 |
Modeling of the interfacial behaviors for the isobutane alkylation with C4 olefin using ionic liquid as catalyst Zheng WZ, Xie WX, Sun WZ, Zhao L |
42 - 52 |
Modeling of the interfacial behaviors for the isobutane alkylation with C4 olefin using ionic liquid as catalyst Zheng WZ, Xie WX, Sun WZ, Zhao L |
53 - 65 |
Developing breakage models relating morphological data to the milling behaviour of flame synthesised titania particles Lindberg C, Akroyd J, Kraft M |
53 - 65 |
Developing breakage models relating morphological data to the milling behaviour of flame synthesised titania particles Lindberg C, Akroyd J, Kraft M |
66 - 76 |
Highly selective hydrogenation of phenol to cyclohexanol over MOF-derived non-noble Co-Ni@NC catalysts Li AQ, Shen K, Chen JY, Li Z, Li YW |
66 - 76 |
Highly selective hydrogenation of phenol to cyclohexanol over MOF-derived non-noble Co-Ni@NC catalysts Li AQ, Shen K, Chen JY, Li Z, Li YW |
77 - 90 |
Hybrid model based expected improvement control for cyclical operation of membrane microfiltration processes Chan LLT, Chou CP, Chen JH |
77 - 90 |
Hybrid model based expected improvement control for cyclical operation of membrane microfiltration processes Chan LLT, Chou CP, Chen JH |
91 - 100 |
Preparation of thermally stable composite forward osmosis hollow fiber membranes based on copoly(phthalazinone biphenyl ether sulfone) substrates Zhang SH, Liu P, Chen YN, Jin JY, Hu LJ, Jian XG |
91 - 100 |
Preparation of thermally stable composite forward osmosis hollow fiber membranes based on copoly(phthalazinone biphenyl ether sulfone) substrates Zhang SH, Liu P, Chen YN, Jin JY, Hu LJ, Jian XG |
101 - 106 |
Catalytic effectiveness of porous particles: A continuum analytic model including internal and external surfaces Cohen D, Merchuk J, Zeiri Y, Sadot O |
101 - 106 |
Catalytic effectiveness of porous particles: A continuum analytic model including internal and external surfaces Cohen D, Merchuk J, Zeiri Y, Sadot O |
107 - 114 |
Flow velocity dependence of the pressure drop of oil mist filters Kolb HE, Meyer J, Kasper G |
107 - 114 |
Flow velocity dependence of the pressure drop of oil mist filters Kolb HE, Meyer J, Kasper G |
115 - 121 |
Methodology to estimate the yield stress applied to ultraconcentrated detergents as model systems Calero N, Santos J, Munoz J |
115 - 121 |
Methodology to estimate the yield stress applied to ultraconcentrated detergents as model systems Calero N, Santos J, Munoz J |
122 - 129 |
Printing particles: A high-throughput technique for the production of uniform, bioresorbable polymer microparticles and encapsulation of therapeutic peptides Palmer D, Bamsey K, Groves R, Patil P, Jones H, McAleer L, Seaman P |
122 - 129 |
Printing particles: A high-throughput technique for the production of uniform, bioresorbable polymer microparticles and encapsulation of therapeutic peptides Palmer D, Bamsey K, Groves R, Patil P, Jones H, McAleer L, Seaman P |
130 - 143 |
Subspace decomposition and critical phase selection based cumulative quality analysis for multiphase batch processes Qin Y, Zhao CH, Wang XZ, Gao FR |
130 - 143 |
Subspace decomposition and critical phase selection based cumulative quality analysis for multiphase batch processes Qin Y, Zhao CH, Wang XZ, Gao FR |
144 - 160 |
Optimized design and operation strategy of a Ca-Cu chemical looping process for hydrogen production Fernandez JR, Abanades JC |
144 - 160 |
Optimized design and operation strategy of a Ca-Cu chemical looping process for hydrogen production Fernandez JR, Abanades JC |
161 - 167 |
Rapid salinity measurements for fluid flow characterisation using minimal invasive sensors Severin TS, Plamauer S, Apel AC, Bruck T, Weuster-Botz D |
161 - 167 |
Rapid salinity measurements for fluid flow characterisation using minimal invasive sensors Severin TS, Plamauer S, Apel AC, Bruck T, Weuster-Botz D |
168 - 180 |
Experimental investigation of liquid distribution in a packed column with structured packing under permanent tilt and roll motions using electrical resistance tomography Son Y, Kim G, Lee S, Kim H, Min K, Lee KS |
168 - 180 |
Experimental investigation of liquid distribution in a packed column with structured packing under permanent tilt and roll motions using electrical resistance tomography Son Y, Kim G, Lee S, Kim H, Min K, Lee KS |
181 - 192 |
Life cycle cost analysis of MEG regeneration process incorporating a modified slip stream concept Kim H, Lim Y, Seo Y, Ko M |
181 - 192 |
Life cycle cost analysis of MEG regeneration process incorporating a modified slip stream concept Kim H, Lim Y, Seo Y, Ko M |
193 - 209 |
Reactive absorption of CO2 in NaOH: Detailed study of enhancement factor models Krauss M, Rzehak R |
193 - 209 |
Reactive absorption of CO2 in NaOH: Detailed study of enhancement factor models Krauss M, Rzehak R |
210 - 219 |
Explicit equation for the determination of the overall mass transfer coefficient in a hollow fiber membrane contactor Manrique YA, Ozdural AR, Trebouet D, Ribeiro AM, Loureiro JM |
210 - 219 |
Explicit equation for the determination of the overall mass transfer coefficient in a hollow fiber membrane contactor Manrique YA, Ozdural AR, Trebouet D, Ribeiro AM, Loureiro JM |
220 - 234 |
Stability analysis by means of information entropy: Assessment of a novel method against natural circulation experimental data Cammi A, Misale M, Devia F, Cauzzi MT, Pini A, Luzzi L |
220 - 234 |
Stability analysis by means of information entropy: Assessment of a novel method against natural circulation experimental data Cammi A, Misale M, Devia F, Cauzzi MT, Pini A, Luzzi L |
235 - 245 |
Contradictory concepts in tortuosity determination in porous media in electrochemical devices Tjaden B, Finegan DP, Lane J, Brett DJL, Shearing PR |
235 - 245 |
Contradictory concepts in tortuosity determination in porous media in electrochemical devices Tjaden B, Finegan DP, Lane J, Brett DJL, Shearing PR |
246 - 261 |
Rotary reverse flow reactor vs. adiabatic reactor with regenerative preheating - Design and comparison Luzi CD, Martinez OM, Barreto GF |
246 - 261 |
Rotary reverse flow reactor vs. adiabatic reactor with regenerative preheating - Design and comparison Luzi CD, Martinez OM, Barreto GF |
262 - 273 |
Tailoring product distribution during upgrading of palmitic acid over bi-functional metal/zeolite catalysts Shi YC, Xing EH, Cao YY, Liu MJ, Wu KJ, Yang MD, Wu YL |
262 - 273 |
Tailoring product distribution during upgrading of palmitic acid over bi-functional metal/zeolite catalysts Shi YC, Xing EH, Cao YY, Liu MJ, Wu KJ, Yang MD, Wu YL |
274 - 282 |
Heterogeneous catalysis in pulsed-flow reactors with nanoporous gold hollow spheres Falcucci G, Amati G, Krastev VK, Montessori A, Yablonsky GS, Succi S |
274 - 282 |
Heterogeneous catalysis in pulsed-flow reactors with nanoporous gold hollow spheres Falcucci G, Amati G, Krastev VK, Montessori A, Yablonsky GS, Succi S |
283 - 302 |
Analyzing the effects of turbulence and multiphase treatments on oxy-coal combustion process predictions using LES and RANS Sadiki A, Agrebi S, Chrigui M, Doost AS, Knappstein R, Di Mare F, Janicka J, Massmeyer A, Zabrodiec D, Hees J, Kneer R |
283 - 302 |
Analyzing the effects of turbulence and multiphase treatments on oxy-coal combustion process predictions using LES and RANS Sadiki A, Agrebi S, Chrigui M, Doost AS, Knappstein R, Di Mare F, Janicka J, Massmeyer A, Zabrodiec D, Hees J, Kneer R |
303 - 312 |
Numerical study of three-dimensional droplet impact on a flowing liquid film in annular two-phase flow Xie ZH, Hewitt GF, Pavlidis D, Salinas P, Pain CC, Matar OK |
303 - 312 |
Numerical study of three-dimensional droplet impact on a flowing liquid film in annular two-phase flow Xie ZH, Hewitt GF, Pavlidis D, Salinas P, Pain CC, Matar OK |
313 - 319 |
Molecular dynamics simulation of the influence of polyacrylamide on the stability of sodium dodecyl sulfate foam Wu G, Zhu QQ, Yuan CT, Wang HB, Li CL, Sun SQ, Hu SQ |
313 - 319 |
Molecular dynamics simulation of the influence of polyacrylamide on the stability of sodium dodecyl sulfate foam Wu G, Zhu QQ, Yuan CT, Wang HB, Li CL, Sun SQ, Hu SQ |
320 - 333 |
Analysis of light-off during oxidation of reactant mixtures on Pt/Al2O3 using micro-kinetic models Kota AS, Dadi RK, Luss D, Balakotaiah V |
320 - 333 |
Analysis of light-off during oxidation of reactant mixtures on Pt/Al2O3 using micro-kinetic models Kota AS, Dadi RK, Luss D, Balakotaiah V |
334 - 344 |
Interval enclosures for reachable sets of chemical kinetic flow systems. Part 1: Sparse transformation Tulsyan A, Barton PI |
334 - 344 |
Interval enclosures for reachable sets of chemical kinetic flow systems. Part 1: Sparse transformation Tulsyan A, Barton PI |
345 - 357 |
Interval enclosures for reachable sets of chemical kinetic flow systems. Part 2: Direct-bounding method Tulsyan A, Barton PI |
345 - 357 |
Interval enclosures for reachable sets of chemical kinetic flow systems. Part 2: Direct-bounding method Tulsyan A, Barton PI |
358 - 372 |
Interval enclosures for reachable sets of chemical kinetic flow systems. Part 3: Indirect-bounding method Tulsyan A, Barton PI |
358 - 372 |
Interval enclosures for reachable sets of chemical kinetic flow systems. Part 3: Indirect-bounding method Tulsyan A, Barton PI |
373 - 373 |
Effect of sintering on the reactivity of copper-based oxygen carriers synthesized by impregnation (vol 162, pg 131, 2017) Maya JC, Chejne F, Bhatia SK |
373 - 373 |
Effect of sintering on the reactivity of copper-based oxygen carriers synthesized by impregnation (vol 162, pg 131, 2017) Maya JC, Chejne F, Bhatia SK |