2413 - 2413 |
Preface for the special issue on the capture of carbon dioxide from industrial sources: Technological developments and future opportunities Idem R, Tontiwachwuthikul P |
2414 - 2420 |
Pilot plant studies of the CO2 capture performance of aqueous MEA and mixed MEA/MDEA solvents at the University of Regina CO2 capture technology development plant and the Boundary Dam CO2 capture demonstration Idem R, Wilson M, Tontiwachwuthikul P, Chakma A, Veawab A, Aroonwilas A, Gelowitz D |
2421 - 2429 |
Identifying cost-effective CO2 control levels for amine-based CO2 capture systems Rao AB, Rubin ES |
2430 - 2436 |
Accelerated mass transfer of CO2 in reservoir brine due to density-driven natural convection at high pressures and elevated temperatures Yang CD, Gu YG |
2437 - 2451 |
Analysis of monoethanolamine and its oxidative degradation products during CO2 absorption from flue gases: A comparative study of GC-MS, HPLC-RID, and CE-DAD analytical techniques and possible optimum combinations Supap T, Idem R, Tontiwachwuthikul P, Saiwan C |
2452 - 2456 |
Effect of operational parameters on carbon dioxide storage capacity in a heterogeneous oil reservoir: A case study Asghari K, Al-Dliwe A, Mahinpey N |
2457 - 2464 |
Energy performance of stripper configurations for CO2 capture by aqueous amines Oyenekan BA, Rochelle GT |
2465 - 2472 |
Innovative absorber/stripper configurations for CO2 capture by aqueous monoethanolamine Jassim MS, Rochelle GT |
2473 - 2482 |
Absorption of CO2 in aqueous diglycolamine Al-Juaied M, Rochelle GT |
2483 - 2488 |
Life-cycle analysis of CO2 EOR on EOR and geological storage through economic optimization and sensitivity analysis using the Weyburn unit as a case study Suebsiri J, Wilson M, Tontiwachwuthikul P |
2489 - 2496 |
Study of a modified amine-based regeneration unit Tobiesen FA, Svendsen HF |
2497 - 2504 |
Study of the carbamate stability of amines using a initio methods and free-energy perturbations da Silva EF, Svendsen HF |
2505 - 2512 |
Experimental and modeling study of the solubility of carbon dioxide in aqueous 30 mass % 2-((2-aminoethyl)amino)ethanol solution Ma'mun S, Jakobsen JP, Svendsen HF, Juliussen O |
2513 - 2521 |
Oxidation inhibitors for copper and iron catalyzed degradation of monoethanolamine in CO2 capture processes Goff GS, Rochelle GT |
2522 - 2530 |
Hydrotalcite as CO2 sorbent for sorption-enhanced steam reforming of methane Reijers HTJ, Valster-Schiermeier SEA, Cobden PD, van den Brink RW |
2531 - 2545 |
Kinetics of carbon dioxide absorption into aqueous potassium carbonate and piperazine Cullinane JT, Rochelle GT |
2546 - 2552 |
Economics of CO2 and mixed gas geosequestration of flue gas using gas separation membranes Ho MT, Leamon G, Allinson GW, Wiley DE |
2553 - 2557 |
Rigorous model for predicting the behavior of CO2 absorption into AMP in packed-bed absorption columns Aboudheir A, Tontiwachwuthikul P, Idem R |
2558 - 2568 |
Photocatalytic process for CO2 emission reduction from industrial flue gas streams Usubharatana P, McMartin D, Veawab A, Tontiwachwuthikul P |
2569 - 2579 |
Comprehensive study of the kinetics of the oxidative degradation of CO2 loaded and concentrated aqueous monoethanolamine (MEA) with and without sodium metavanadate during CO2 absorption from flue gases Bello A, Idem RO |
2580 - 2585 |
Using a packed-column model to simulate the performance of a membrane absorber deMontigny D, Aboudheir A, Tontiwachwuthikul P, Chakma A |
2586 - 2593 |
Electrochemical investigation on the effect of heat-stable salts on corrosion in CO2 capture plants using aqueous solution of MEA Tanthapanichakoon W, Veawab A, McGarvey B |
2594 - 2600 |
Modelling the performance of a CO2 absorber containing structured packing deMontigny D, Aboudheir A, Tontiwachwuthikul P, Chakma A |
2601 - 2607 |
Kinetics of the oxidative degradation of CO2 loaded and concentrated aqueous MEA-MDEA blends during CO2 absorption from flue gas streams Lawal AO, Idem RO |
2608 - 2616 |
Kinetics of the absorption of CO2 into mixed aqueous loaded solutions of monoethanolamine and methyldiethanolamine Ramachandran N, Aboudheir A, Idem R, Tontiwachwuthikul P |
2617 - 2625 |
Nickel-copper oxygen carriers to reach zero CO and H-2 emissions in chemical-looping combustion Adanez J, Garcia-Labiano F, de Diego LF, Gayan P, Celaya J, Abad A |
2626 - 2633 |
Diethylenetriamine[propyl(silyl)]-functionalized (DT) mesoporous silicas as CO2 adsorbents Knowles GP, Delaney SW, Chaffee AL |
2634 - 2640 |
N-halamine-based antimicrobial additives for polymers: Preparation, characterization, and antimicrobial activity Chen ZB, Sun YY |
2641 - 2645 |
Synthesis of water-based polystyrene-nanoclay composite suspension via miniemulsion polymerization Tong ZH, Deng YL |
2646 - 2650 |
FCCSOx additives deactivation Roncolatto RE, Cardoso MJB, Lam YL, Schmal M |
2651 - 2660 |
Comparison between phenomenological and empirical models for gas-phase polymerization process control Neumann GA, Finkler TF, Cardozo NSM, Secchi AR |
2661 - 2671 |
The oxidative dehydrogenation of n-butane in a fixed-bed reactor and in an inert porous membrane reactor-maximizing the production of butenes and butadiene Milne D, Glasser D, Hildebrandt D, Hausberger B |
2672 - 2676 |
Melt transesterification of polycarbonate catalyzed by DMAP Hsu JP, Wong JJ |
2677 - 2688 |
NOx-mediated homogeneous pathways for the synthesis of formaldehyde from CH4-O-2 mixtures Zalc JM, Green WH, Iglesia E |
2689 - 2696 |
Chemical-looping combustion with NiO and Fe2O3 in a thermobalance and circulating fluidized bed reactor with double loops Son SR, Kim SD |
2697 - 2706 |
Yield improvements in membrane reactors for partial oxidation reactions O'Neill CM, Wolf EE |
2707 - 2714 |
Comparison of reactive distillation with process alternatives for the isobutene dimerization reaction Kamath RS, Qi ZW, Sundmacher K, Aghalayam P, Mahajani SM |
2715 - 2721 |
Ozone decomposition in water catalyzed by activated carbon: Influence of chemical and textural properties Faria PCC, Orfao JJM, Pereira MFR |
2722 - 2727 |
Static and dynamic mechanical properties of vinylester resin matrix composites reinforced with shellac-treated jute yarns Ray D, Sengupta SP, Rana AK, Bose NR |
2728 - 2733 |
Macroemulsions of liquid and supercritical CO2-in-water and water-in-liquid CO2 stabilized by fine particles Golomb D, Barry E, Ryan D, Swett P, Duan H |
2734 - 2740 |
Rheological comparison of chemical and physical blowing agents in a thermoplastic polyolefin Qin X, Thompson AR, Hrymak AN |
2741 - 2747 |
Method for proportional-integral controller tuning assessment Visioli A |
2748 - 2757 |
Optimal shutdown policy for maintenance of cracking furnaces in ethylene plants Schulz EP, Bandoni JA, Diaz MS |
2758 - 2768 |
Model-based controller design for unstable, non-minimum-phase, nonlinear processes Panjapornpon C, Soroush M, Seider WD |
2769 - 2776 |
Decentralized control system design for multivariable processes - A novel method based on effective relative gain array Xiong Q, Cai WJ, He MJ, He M |
2777 - 2786 |
Geometry of separation boundaries: Systems with reaction Taylor R, Miller A, Lucia A |
2787 - 2792 |
Optimization of biological nitrogen removal via nitrite in a SBR treating supernatant from the anaerobic digestion of municipal solid wastes Mace S, Dosta J, Gali A, Mata-Alvarez J |
2793 - 2807 |
Scaling rules and increasing feed rates in two-zone and four-zone simulated moving bed systems Jin WH, Wankat PC |
2808 - 2817 |
Mathematical simulation of hazardous ion retention from radioactive waste in a fixed bed reactor Othman SH, Sohsah MA, Ghoneim MM, El-Anadouli BE |
2818 - 2823 |
Experimental and theoretical investigation of the purification process of organic materials in a continuous inclined column crystallizer Chen LA, Li J, Matsuoka M |
2824 - 2829 |
Contribution of the surface reactions to the overall oxygen permeation of the mixed conducting membranes Chang XF, Zhang C, Wu ZT, Jin WQ, Xu NP |
2830 - 2839 |
Electrochemical degradation of pulp and paper mill wastewater. Part 1. COD and color removal Mahesh S, Prasad B, Mall ID, Mishra IM |
2840 - 2844 |
Precipitation kinetics of cellulose in the Lyocell spinning process Liu RG, Hu XC |
2845 - 2849 |
Feasibility study on the integration of adsorption/bioregeneration of pi-complexation adsorbent for desulfurization Li WL, Xing JM, Xiong XC, Huang JX, Liu HZ |
2850 - 2855 |
Removal of zinc(II) from aqueous solution by purified carbon nanotubes: Kinetics and equilibrium studies Lu CS, Chiu H, Liu CT |
2856 - 2861 |
Estimation of the normal boiling point of organic compounds Sanghvi R, Yalkowsky SH |
2862 - 2874 |
Simulation of flow distribution in radial flow reactors Kareeri AA, Zughbi HD, Al-Ali HH |
2875 - 2880 |
Design of task-specific ionic liquids for capturing CO2: A molecular orbital study Yu GR, Zhang SJ, Yao XQ, Zhang JM, Dong K, Dai WB, Mori R |
2881 - 2891 |
Modeling turbulent flows with free-surface in unbaffled agitated vessels Haque JN, Mahmud T, Roberts KJ, Rhodes D |
2892 - 2896 |
Cellular automata model of phase transition in binary mixtures Vannozzi C, Fiorentino D, D'Amore M, Rumshitzki DS, Dress A, Mauri R |
2897 - 2900 |
Degradation of phenol by simultaneous use of gas-phase corona discharge and catalyst-supported mesoporous carbon gels Sano N, Yamamoto T, Takemori I, Kim SI, Eiad-ua A, Yamamoto D, Nakaiwa M |