575 - 575 |
Roy Jackson Sundaresan S |
576 - 589 |
Multiscale structure of uniformity in mixtures Wei J |
590 - 595 |
Pumping slurries forming highly compactible cakes Tiller FM, Cleveland T, Lu R |
596 - 600 |
Prediction of stress distribution in a two-dimensional bunker using the fixed principal axes method Nedderman RM |
601 - 609 |
Novel optical methodologies in studying mechanical signal transduction in mammalian cells Stamatas GN, McIntire LV |
610 - 620 |
Two-dimensional voidage waves in fluidized beds Chen Z, Gibilaro LG, Foscolo PU |
621 - 630 |
Electrical capacitance tomography measurements of gravity-driven granular flows Hua JS, Wang CH |
631 - 638 |
Bipolar coagulation process for the production of powders Camelot D, Marijnissen JCM, Scarlett B |
639 - 651 |
Choosing optimal control policies using the attainable region approach Godorr S, Hildebrandt D, Glasser D, McGregor C |
652 - 659 |
The attainable region and Pontryagin's maximum principle McGregor C, Glasser D, Hildebrandt D |
660 - 666 |
On the optimal design and control of a biodegradation process with substrate inhibition kinetics Villadsen J |
667 - 682 |
A new design of reverse-flow reactors with enhanced thermal dispersion Keith JM, Leighton DT, Chang HC |
683 - 691 |
Removal rates of major and trace components of an organic film using aqueous nonionic surfactant solutions Kabin JA, Saez AE, Grant CS, Carbonell RG |
692 - 704 |
Anonymous class in declarative process modeling Allan BA, Westerberg AW |
705 - 713 |
Measurement of particle phase stresses in fast fluidized beds Polashenski W, Chen JC |
714 - 722 |
A novel distillate policy for batch reactive distillation with application to the production of butyl acetate Venimadhavan G, Malone MF, Doherty MF |
723 - 730 |
Molecular dynamics simulations of diffusion in mesoporous glass Fernandes NE, Gavalas GR |
731 - 743 |
Particulate stresses in dense disperse flow Buyevich YA |
744 - 766 |
Optimization framework for the synthesis of chemical reactor networks Schweiger CA, Floudas CA |
767 - 777 |
Analytical criteria for validity of pseudohomogeneous models of packed-bed catalytic reactors Dommeti SMS, Balakotaiah V, West DH |
778 - 786 |
Flow mechanisms, relative permeabilities, and coupling effects in steady-state two-phase flow through porous media, the case of strong wettability Avraam DG, Payatakes AC |
787 - 792 |
Computation of circulating fluidized-bed riser flow for the fluidization VIII benchmark test Sun B, Gidaspow D |
793 - 798 |
Kinetics of rapid high-temperature reactions: Titanium-nitrogen system Pelekh AE, Mukasyan AS, Varma A |
799 - 802 |
Wavy instability in liquid-fluidized beds Nicolas M, Hinch J, Guazzelli E |
803 - 811 |
Characteristics of gas-fluidized beds in different flow regimes Bai D, Issangya AS, Grace JR |
812 - 819 |
Sorbent/ash reactivation for enhanced SO2 capture using a novel carbonation technique Agnihotri R, Chauk SS, Mahuli SK, Fan LS |
820 - 822 |
Granular dilatancy and the plasticity of glassy lubricants Goddard JD |
823 - 832 |
Improving product recovery in fractional crystallization processes: Retrofit of an adipic acid plant Cesar MAB, Ng KM |
833 - 844 |
Dissolution of an immobile phase during flow in porous media Quintard M, Whitaker S |
845 - 850 |
The beauty of self-adjoint symmetry Ramkrishna D, Asis R |
851 - 854 |
Dispersion in flows with streamwise variations of mean velocity: Radial flow Stone HA, Brenner H |
855 - 864 |
Subcritical solvent effects on a parallel Diels-Alder reaction network Reaves JT, Roberts CB |
865 - 872 |
Rolled stationary phases: Dimensionally structured textile adsorbents for rapid liquid chromatography of proteins Hamaker K, Rau SL, Hendrickson R, Liu J, Ladisch CM, Ladisch MR |
873 - 878 |
Selective catalytic reduction of nitric oxide with ethylene on copper ion-exchanged Al-MCM-41 catalyst Long RQ, Yang RT |
879 - 883 |
Chemical processing in high-pressure aqueous environments. 6. Demonstration of catalytic gasification for chemical manufacturing wastewater cleanup in industrial plants Elliott DC, Neuenschwander GG, Phelps MR, Hart TR, Zacher AH, Silva LJ |
884 - 891 |
Direct epoxidation of propene using gold dispersed on TS-1 and other titanium-containing supports Nijhuis TA, Huizinga BJ, Makkee M, Moulijn JA |
892 - 896 |
Investigation of the effects of controlled periodic illumination on the oxidation of gaseous trichloroethylene using a thin film of TiO2 Buechler KJ, Noble RD, Koval CA, Jacoby WA |
897 - 905 |
Experimental analysis of the combustion of mixtures of C-1-C-2 hydrocarbons Rota R, Fiandaca R, Morbidelli M, Carra S |
906 - 915 |
Hydrogenation of 2,4-dinitrotoluene using a supported Ni catalyst: Reaction kinetics and semibatch slurry reactor modeling Malyala RV, Chaudhari RV |
916 - 927 |
Performance of ZSM-5 as a fluid catalytic cracking catalyst additive: Effect of the total number of acid sites and particle size Triantafillidis CS, Evmiridis NP, Nalbandian L, Vasalos IA |
928 - 937 |
Effect of operating variables on the gas holdup in a large-scale slurry bubble column reactor operating with an organic liquid mixture Inga JR, Morsi BI |
938 - 943 |
Upgrading of a petroleum residue. Kinetics of Conradson carbon residue conversion Trasobares S, Callejas MA, Benito AM, Martinez MT, Severin D, Brouwer L |
944 - 949 |
Holdup and liquid circulation velocity in a rectangular air-lift bioreactor Atenas M, Clark M, Lazarova V |
950 - 957 |
Pore structure modification of alumina support by SiC-Si3N4 nanoparticles prepared by the particle precipitation aided chemical vapor deposition Hong LS, Lai HT |
958 - 963 |
Modification of ZnO-TiO2 high-temperature desulfurization sorbent by ZrO2 addition Sasaoka E, Sada N, Manabe A, Uddin MA, Sakata Y |
964 - 972 |
Studies on asphaltenes through analysis of polar fractions Nalwaya V, Tangtayakom V, Piumsomboon P, Fogler S |
973 - 977 |
Conversion of fly ash into mesoporous aluminosilicate Chang HL, Chun CM, Aksay IA, Shih WH |
978 - 987 |
A neural PPD controller for the pH neutralization process Yeo YK, Kwon TI |
988 - 998 |
Multiple-fault diagnosis under uncertain conditions by the quantification of qualitative relations Lee GB, Lee BW, Yoon ES, Han CH |
999 - 1006 |
A quantitative controllability index Zheng A, Mahajanam RV |
1007 - 1023 |
Control schemes for an industrial rotary calciner with a heat shield around the combustion zone Ciftci S, Kim NK |
1024 - 1031 |
Shortcut procedure for multicomponent batch distillation with distillate receiver Kim JK, Ju DP |
1032 - 1039 |
Separation and recovery of gallium and indium from simulated zinc refinery residue by liquid-liquid extraction Nishihama S, Hirai T, Komasawa I |
1040 - 1056 |
Computational strategies for sizing liquid-liquid extractors Kumar A, Hartland S |
1057 - 1064 |
Development of a corresponding-state "association enthalpy" function for use in the prediction of coal liquid enthalpies Sharma R, Baid A, Jayaram IS |
1065 - 1068 |
Effect of oxide acidity upon the heats of decomposition of metal oxysalts Ibanez JG, Silva MA, Bravo MA |
1069 - 1074 |
Simulation of the direct production of synthesis gas from sour natural gas by noncatalytic partial oxidation (NCPO): Thermodynamics and stoichiometry Abdel-Aal HK, Shalabi MA, Al-Harbi DK, Hakeem T |
1075 - 1082 |
Characterization of mixing in micromixers by a test reaction: Single mixing units and mixer arrays Ehrfeld W, Golbig K, Hessel V, Lowe H, Richter T |
1083 - 1093 |
Countercurrent gas-pseudoplastic liquid two-phase flow Welsh SA, Ghiaaisaan SM, Abdel-Khalik SI |
1094 - 1098 |
Flow patterns in liquid-liquid Taylor-Couette-Poiseuille flow Campero RJ, Vigil RD |
1099 - 1106 |
Prediction of pressure losses in pipe flow of aqueous foams Gardiner BS, Dlugogorski BZ, Jameson GJ |
1107 - 1113 |
Phase-boundary calculations in systems involving more than two phases, with application to hydrocarbon mixtures Lindeloff N, Andersen SI, Stenby EH, Heidemann RA |
1114 - 1124 |
Binary adsorption isotherms from chromatographic retention times Buffham BA, Mason G, Heslop MJ |
1125 - 1132 |
Investigation of urea release from a coated sphere into a quiescent liquid Doan HD, Trass O, Fayed ME |
1133 - 1139 |
Surface tension model for concentrated electrolyte aqueous solutions by the Pitzer equation Li ZB, Li YG, Lu JF |
1140 - 1148 |
Simplified hole theory equation of state for liquid-liquid equilibria of polymer solutions and blends Feng W, Wang WC |
1149 - 1158 |
Solubility of sulfur dioxide in aqueous solutions of acetic acid, sodium acetate, and ammonium acetate in the temperature range from 313 to 393 K at pressures up to 3.3 MPa: Experimental results and comparison with correlations/predictions Xia JZ, Rumpf B, Maurer G |
1159 - 1162 |
Development and application of an on-line fouling gauge for brown coal power stations Chadwick BL |
1163 - 1165 |
A way to higher hydrocarbons from methane with sizable yield and good selectivity Pareja P, Mercy M, Gachon JC, Amariglio A, Amariglio H |
1166 - 1168 |
Comments on "Production of activated carbon from coconut shell char in a fluidized bed reactor" Martin-Gullon I, Conesa JA, Linares-Solano A |
1169 - 1171 |
Rebuttal to comments on "Production of activated carbon from coconut shell char in a fluidized bed reactor" Sai PMS, Ahmed J, Krishnaiah K |
1172 - 1173 |
Comments on the paper "Empirical method to correlate and to predict the vapor-liquid equilibrium and liquid-liquid equilibrium of binary amorphous polymer solutions" Imre A, Van Hook WA |
1174 - 1175 |
Reply to the comments of A. Imre and W. Alexander Van Hook on "Empirical methods to correlate and to predict the vapor-liquid equilibrium of binary amorphous polymer solutions" Vetere A |
1176 - 1176 |
Shortcut procedure for multicomponent batch distillation with distillate receiver (vol 38, pg 1024, 1998) Kim JK, Ju DP |