605 - 606 |
Gas-to-liquids processes: Preface Patience GS, Boffito DC |
607 - 612 |
Synthesis gas technology large-scale applications Dybkjaer I, Aasberg-Petersen K |
613 - 622 |
Micro-syngas technology options for GtL Trevisanut C, Jazayeri SM, Bonkane S, Neagoe C, Mohamadalizadeh A, Boffito DC, Bianchi CL, Pirola C, Visconti CG, Lietti L, Abatzoglou N, Frost L, Lerou J, Green W, Patience GS |
623 - 635 |
The engine reformer: Syngas production in an engine for compact gas-to-liquids synthesis Lim EG, Dames EE, Cedrone KD, Acocella AJ, Needham TR, Arce A, Cohn DR, Bromberg L, Cheng WK, Green WH |
636 - 641 |
Production of synthetic fuels by high-temperature co-electrolysis of carbon dioxide and steam with Fischer-Tropsch synthesis Frost L, Elangovan E, Hartvigsen J |
642 - 649 |
Partial oxidation of methane to syngas over Pt/Rh/MgO catalyst supported on FeCralloy woven fibre Ma ZN, Ouzilleau P, Trevisanut C, Neagoe C, Lotfi S, Boffito DC, Patience GS |
650 - 654 |
H2S poisoning of NiAl2O4/Al2O3-YSZ catalyst during methane dry reforming Blanchard J, Achouri I, Abatzoglou N |
655 - 661 |
Stability of a Cs-promoted Co-Mo/Al2O3 catalyst during synthesis gas conversion Ardakani SJ, Alyani M, Smith KJ |
662 - 677 |
New concepts in low-temperature catalytic hydrogenation and their implications for process intensification Fernandez C, Karelovic A, Gaigneaux EM, Ruiz P |
678 - 684 |
Fischer-Tropsch synthesis: Effect of solvent on the H-2-D-2 isotopic exchange rate over an activated cobalt catalyst Pendyala VRR, Shafer WD, Jacobs G, Davis BH |
685 - 695 |
Kinetics of low-temperature Fischer-Tropsch synthesis on cobalt catalysts: Are both slurry autoclave and tubular packed-bed reactors adequate to collect relevant data at lab-scale? Visconti CG, Lietti L, Tronconi E, Rossini S |
696 - 702 |
High-loaded Fe-supported catalyst for the thermochemical BtL-FT process: Experimental results and modelling Comazzi A, Pirola C, Bianchi CL, Galli F, Longhi M, Manenti F |
703 - 712 |
Chemical looping syngas from CO2 and H2O over manganese oxide minerals Perreault P, Patience GS |
713 - 715 |
How do you write and present research well? 6Tell it in the title Patience GS, Boffito DC, Patience PA |
716 - 724 |
Ethanol production from sweet potato: The effect of ripening, comparison of two heating methods, and cost analysis Schweinberger CM, Putti TR, Susin GB, Trierweiler JO, Trierweiler LF |
725 - 732 |
Groundwater nitrate contamination: Assessment and treatment using Moringa oleifera Lam. seed extract and activated carbon filtration Rezende D, Nishi L, Coldebella PF, Silva MF, Vieira MF, Vieira AMS, Bergamasco R, Fagundes-Klen MR |
733 - 737 |
Drop forming as a basis for scaling up of the in situ coating process Abouzeid A, Petersen S, Ulrich J |
738 - 744 |
Determination of adsorption and kinetic parameters for methyl oleate (biodiesel) esterification reaction catalyzed by Amberlyst 15 resin Ray NM, Ray AK |
745 - 751 |
Methanol carboxylation over zirconium dioxide: Effect of catalyst phase composition on its acid-base spectrum and direction of catalytic transformations Kochkin YN, Vlasenko NV, Struzhko VL, Puziy AM, Strizhak PE |
752 - 760 |
Steam reforming of ethanol over mesoporous Rh/CeZrO2: Mechanistic evaluation using in situ DRIFT spectroscopy Sharma PK, Saxena N, Bind VK, Roy PK, Bhatt A |
761 - 770 |
Techno-economic assessment of CO2 capture from aluminum smelter emissions using PZ activated AMP solutions Lassagne O, Iliuta MC, Gosselin L, Desilets M |
771 - 778 |
Gas-phase mass transfer characteristics in a counter airflow shear rotating packed bed Liu YZ, Zhang FF, Gu DY, Qi GS, Jiao WZ, Chen XY |
779 - 791 |
Heavy oil recovery using ASP flooding: A pore-level experimental study in fractured five-spot micromodels Sedaghat M, Mohammadzadeh O, Kord S, Chatzis I |
792 - 802 |
A new model based on coupling of MEP/CFD/ILIA for prediction of primary atomization Hosseinalipour SM, Karimaei H |