4469 - 4475 |
In honor of Gerhart Eigenberger Stankiewicz A, Kolios G |
4476 - 4482 |
Catalytic bubble model: Bubble growth with an interfacial chemical reaction Favelukis M, Yablonsky GS |
4483 - 4493 |
Eulerian simulation strategy for scaling up a bubble column slurry reactor for Fischer-Tropsch synthesis van Baten JM, Krishna R |
4494 - 4502 |
Novel analytical solution for a simulated moving bed in the presence of mass-transfer resistance Silva VMT, Minceva M, Rodrigues AE |
4503 - 4510 |
Modeling of three-way-catalyst monolith converters with microkinetics and diffusion in the washcoat Koci P, Kubicek M, Marek M |
4511 - 4521 |
Hydrodynamics of pulsing flow in three-phase fixed-bed reactor operating at an elevated pressure Burghardt A, Bartelmus G, Szlemp A |
4522 - 4534 |
Kinetic study of lean NOx storage over the Pt-Ba/Al2O3 system Scotti A, Nova I, Tronconi E, Castoldi L, Lietti L, Forzatti P |
4535 - 4539 |
Enhancement of heterogeneous autocatalytic reactions accompanied by mass and heat transfer phenomena Grzesik M, Kulawska MT, Skrzypek J, Ptaszek A |
4540 - 4550 |
Advanced kinetic concepts and experimental methods for catalytic three-phase processes Salmi T, Murzin DY, Mikkola JP, Warna J, Maki-Arvela P, Toukoniitty E, Toppinen S |
4551 - 4558 |
Feasibility of an electrochemical membrane reactor for the partial oxidation of n-butane to maleic anhydride Ye YM, Rihko-Struckmann L, Munder B, Rau H, Sundmacher K |
4559 - 4570 |
Thermal evolution of the structure of a Mg-Al-CO3 layered double hydroxide: Sorption reversibility aspects Kim Y, Yang WS, Liu PKT, Sahimi M, Tsotsis TT |
4571 - 4579 |
Improvement of properties of poly(ether ketone) ionomer membranes by blending and cross-linking Kerres J, Tang CM, Graf C |
4580 - 4584 |
A high-throughput screening technique for conversion in hot compressed water Potic B, Kersten SRA, Prins W, van Swaaij WPM |
4585 - 4594 |
No more runaways in fine chemical reactors Westerterp KR, Molga EJ |
4595 - 4601 |
Synthesis of dimethyl oxalate from CO and CH3ONO on carbon nanofiber supported palladium catalysts Zhao TJ, Chen D, Dai YC, Yuan WK, Holmen A |
4602 - 4611 |
Monolithic catalysts for the chemical industry Boger T, Heibel AK, Sorensen CM |
4612 - 4623 |
Computational analysis and optimization of a chemical vapor deposition reactor with large-scale computing Salinger AG, Pawlowski RP, Shadid JN, Van Bloemen Waanders BG |
4624 - 4634 |
Concept and design of a novel compact reactor for autothermal steam reforming with integrated evaporation and CO cleanup Morillo A, Freund A, Merten C |
4635 - 4646 |
Effect of clustering on gas-solid drag in dilute two-phase flow Heynderickx GJ, Das AK, De Wilde J, Marin GB |
4647 - 4656 |
Dynamic behavior of microbial populations in stirred bioreactors simulated with Euler-Lagrange methods: Traveling along the lifelines of single cells Lapin A, Muller D, Reuss M |
4657 - 4667 |
Some considerations on the design and operation of high-temperature catalytic reverse-flow reactors Neumann D, Gepert V, Veser G |
4668 - 4690 |
Light-off and cumulative emissions in catalytic monoliths with nonuniform catalyst loading Ramanathan K, West DH, Balakotaiah V |
4691 - 4702 |
Analysis of heterogeneously catalyzed ester hydrolysis performed in a chromatographic reactor and in a reaction calorimeter Mai PT, Vu TD, Mai KX, Seidel-Morgenstern A |
4703 - 4708 |
Model analysis of thermal lance combustion Wang HR, Hlavacek V, Pranda P |
4709 - 4720 |
Adsorption, diffusion, and reaction phenomena on FCC catalysts in the CREC riser simulator Atias JA, de Lasa H |
4721 - 4731 |
Compact radial reactor with a structured porous metal catalyst for the conversion of natural gas to synthesis gas: Experiment and modeling Kirillov VA, Bobrin AS, Kuzin NA, Kuzmin VA, Shigarov AB, Skomorokhov VB, Smirnov EI, Sobyanin VA |
4732 - 4739 |
Synthesis of high-surface-area SiC through a modified Sol-Gel route: Control of the pore structure Gupta P, Wang W, Fan LS |
4740 - 4752 |
Precursor aggregate distributions for particulate gels Bonanomi E, Sandkuhler P, Sefcik J, Morari M, Morbidelli M |
4753 - 4760 |
Oxygen distribution in packed-bed membrane reactors for partial oxidations: Effect of the radial porosity profiles on the product selectivity Kurten U, van Sint Annaland M, Kuipers JAM |
4761 - 4767 |
Modeling of axial dispersion in a rotating-bucket contactor Dente M, Bozzano G |
4768 - 4772 |
High-flux palladium membranes based on microsystem technology Keurentjes JTF, Gielens FC, Tong HD, van Rijn CJM, Vorstman MAG |
4773 - 4779 |
Intensification of regenerative heat exchange in chemical reactors using desorptive cooling Grunewald M, Agar DW |
4780 - 4788 |
Modeling of a three-way catalytic converter with respect to fast transients lambda-sensor relevant exhaust gas components Auckenthaler TS, Onder CH, Geering HP, Frauhammer J |
4789 - 4795 |
Impact of initiation and deactivation on melting during gas-phase olefin polymerization Song H, Luss D |
4796 - 4808 |
Novel reactor concepts for thermally efficient methane steam reforming: Modeling and simulation Kolios G, Gritsch A, Glockler B, Sorescu G, Frauhammer J |
4809 - 4814 |
1-butene plus isobutane reactions on solid acid catalysts in dense CO2-based reaction media: Experiments and modeling Lyon CJ, Sarsani VSR, Subramaniam B |
4815 - 4821 |
Kinetics of cyanate decomposition in alkaline solutions of high ionic strength: The catalytic effect of bicarbonate DeMartini N, Murzin DY, Forssen M, Hupa M |
4822 - 4826 |
H-1-NMR, UV-visible, and FT-HR spectral analyses for the conflicting impacts of proton mobility and H-bonding association on the mesomeric structure in azopyrogallol, catechol, resorcinol, quinol, and phenol derivatives of melamine Sayed MB |
4827 - 4832 |
C02-induced miscibility of fluorous and organic solvents for recycling homogeneous catalysts West KN, Hallett JP, Jones RS, Bush D, Liotta CL, Eckert CA |
4833 - 4840 |
Fabrication of single-channel catalytic microburners: Effect of confinement on the oxidation of hydrogen/air mixtures Norton DG, Wetzel ED, Vlachos DG |
4841 - 4847 |
Potential explanations for the inhibition and acceleration of phenol SCWO by water Henrikson JT, Savage PE |
4848 - 4855 |
Improving flooding performance for countercurrent monolith reactors Heibel AK, Jamison JA, Woehl P, Kapteijn F, Moulijn JA |
4856 - 4863 |
Decomposition of urea into NH3 for the SCR process Yim SD, Kim SJ, Baik JH, Nam IS, Mok YS, Lee JH, Cho BK, Oh SH |
4864 - 4870 |
Kinetic studies on catalytic decomposition of methane to hydrogen and carbon over Ni/TiO2 catalyst Zein SHS, Mohamed AR, Sai PST |
4871 - 4875 |
Improving the stereoselectivity of asymmetric reduction of 3-oxo ester to 3-hydroxy ester with pretreatments on bakers'yeast Yang ZH, Yao SJ, Lin DQ |
4876 - 4882 |
Calcium bisulfite oxidation in the flue gas desulfurization process catalyzed by iron and manganese ions Karatza D, Prisciandaro M, Lancia A, Musmarra D |
4883 - 4888 |
Chopped industrial hemp fiber reinforced cellulosic plastic biocomposites: Thermomechanical and morphological properties Wibowo AC, Mohanty AK, Misra M, Drzal LT |
4889 - 4902 |
On the design of optimally informative experiments for dynamic crystallization process modeling Chen BH, Bermingham S, Neumann AH, Kramer HJM, Asprey SP |
4903 - 4907 |
Scale-up of the solid-liquid extraction using characteristic function technique Simeonov E, Seikova I, Pentchev I, Mintchev A |
4908 - 4921 |
Modeling and experimental study of carbon dioxide absorption in aqueous alkanolamine solutions using a membrane contactor Hoff KA, Juliussen O, Falk-Pedersen O, Svendsen HF |
4922 - 4934 |
Removal of selenate by Fe and NiFe nanosized particles Mondal K, Jegadeesan G, Lalvani SB |
4935 - 4943 |
Mass transport modeling in a gas antisolvent process Elvassore N, Cozzi F, Bertucco A |
4944 - 4946 |
Recycled soybean cooking oils as blending stocks for diesel fuels Mushrush GW, Wynne JH, Willauer HD, Lloyd CT, Hughes JM, Beal- EJ |
4947 - 4956 |
In situ ultrasonic spectroscopy study of the nucleation and growth of copper sulfate pentahydrate batch crystallized from supersaturated aqueous solutions Lyall E, Mougin P, Wilkinson D, Roberts KJ |
4957 - 4963 |
Rationalization of the industrial nickel hydroxide synthetic process in view of optimizing its electrochemical performances Casas-Cabanas M, Hernandez JC, Gil V, Soria GL, Palacin MR |
4964 - 4966 |
Clathrate hydrate formed with methane and 2-Propanol: Confirmation of structure II hydrate formation Ohmura R, Takeya S, Uchida T, Ebinuma T |
4967 - 4972 |
Calculation of Hansen solubility parameter values for a range of pressure and temperature conditions, including the supercritical fluid region Williams LL, Rubin JB, Edwards HW |