2879 - 2879 |
Ogunnaike selected as Associate Editor Paul DR |
2880 - 2887 |
Electrosynthesis of phthalocyanines: Influence of solvent Kharisov BI, Blanco LM, Torres-Martinez LM, Garcia-Luna A |
2888 - 2895 |
Glucose and fructose decomposition in subcritical and supercritical water: Detailed reaction pathway, mechanisms, and kinetics Kabyemela BM, Adschiri T, Malaluan RM, Arai K |
2896 - 2901 |
Kinetic model for skeletal isomerization of n-butene over ZSM-22 Byggningsbacka R, Kumar N, Lindfors LE |
2902 - 2910 |
Supercritical water oxidation of methylphosphonic acid Bianchetta S, Li LX, Gloyna EF |
2911 - 2918 |
Synthesis of 2-phenoxyisobutyric acid ethyl ester by tri-liquid-phase catalysis. 1. Analysis of factors affecting the formation of a third liquid phase Hsiao HC, Weng HS |
2919 - 2926 |
Model for random hydrolysis and end degradation of linear polysaccharides: Application to the thermal treatment of mannan in solution Nattorp A, Graf M, Spuhler C, Renken A |
2927 - 2931 |
Preparation and properties of biodiesel from Cynara cardunculus L. oil Encinar JM, Gonzalez JF, Sabio E, Ramiro MJ |
2932 - 2939 |
Dry desulfurization of simulated flue gas in a fluidized-bed reactor for a broad range of SO2 concentration and temperature: A comparison of models Suyadal Y, Oguz H |
2940 - 2946 |
Photocatalytic processes using solar radiation. Modeling of photodegradation of contaminants in polluted waters Martin CA, Sgalari G, Santarelli F |
2947 - 2953 |
High-porosity carbons prepared from bituminous coal with potassium hydroxide activation Teng HS, Hsu LY |
2954 - 2962 |
Removal of H2S by spray-calcined calcium acetate Nimmo W, Agnew J, Hampartsoumian E, Jones JM |
2963 - 2972 |
Comparison of oxygen permeability and stability of perovskite type La(0.2)A(0.8)Co(0.2)Fe(0.8)O(3-delta) (A = Sr, Ba, Ca) membranes Li SG, Jin WQ, Huang P, Xu NP, Shi J, Lin YS, Hu MZC, Payzant EA |
2973 - 2978 |
A novel cross-flow cascade packed column design and simulation Chen FR, Zhou RQ, Duan ZT, Liu YM |
2979 - 2983 |
Control of integrator processes with dominant time delay Tian YC, Gao FR |
2984 - 2994 |
Synthesis of plantwide control systems using optimization McAvoy TJ |
2995 - 3006 |
Nonlinear control of a simulated industrial evaporation system using a feedback linearization technique with a state observer Kam KM, Tade MO |
3007 - 3012 |
PID autotuner based on gain- and phase-margin specifications Wang YG, Shao HH |
3013 - 3026 |
Resource-constrained scheduling of tests in new product development Jain V, Grossmann IE |
3027 - 3035 |
A new structural algorithm for observability classification Ponzoni I, Sanchez MC, Brignole NB |
3036 - 3045 |
Effect of systematic and random errors in thermodynamic models on chemical process design and simulation: A Monte Carlo approach Vasquez VR, Whiting WB |
3046 - 3050 |
The driving force distribution for minimum lost work in chemical reactors close to and far from equilibrium. 1. Theory Kjelstrup S, Sauar E, Bedeaux D, van der Kooi H |
3051 - 3055 |
The driving force distribution for minimum lost work in a chemical reactor close to and far from equilibrium. 2. Oxidation of SO2 Kjelstrup S, Island TV |
3056 - 3068 |
Integration and computational issues in stochastic design and planning optimization problems Bernardo FP, Pistikopoulos EN, Saraiva PM |
3069 - 3075 |
Supercritical fractional extraction of fennel seed oil and essential oil: Experiments and mathematical modeling Reverchon E, Daghero J, Marrone C, Mattea M, Poletto M |
3076 - 3082 |
Selective adsorption of sterically hindered phenols through a single-point binding mechanism Koehler JA, Wallace KK, Smith PJ, Payne GF |
3083 - 3095 |
New method for quaternary systems liquid-liquid extraction tray to tray design Marcilla A, Gomez A, Reyes JA, Olaya MM |
3096 - 3104 |
A novel process for diethanolamine recovery from partially degraded solutions. 1. Process description and phase equilibria of the DEA-BHEP-THEED-hexadecane system Abdi MA, Meisen A |
3105 - 3114 |
A novel process for diethanolamine recovery from partially degraded solutions. 2. Process analysis Abdi MA, Meisen A |
3115 - 3120 |
Fluidization of scrap-wood materials: The influence of the degree of thermal decomposition on the hydrodynamic properties Reina J, Velo E, Puigjaner K |
3121 - 3130 |
Molecular weight and specific gravity distributions for athabasca and cold lake bitumens and their saturate, aromatic, resin, and asphaltene fractions Peramanu S, Pruden BB, Rahimi P |
3131 - 3143 |
Relation between flow pattern and blending in stirred tanks Patwardhan AW, Joshi JB |
3144 - 3161 |
Solubility of hydrocarbons and CO2 mixtures in water under high pressure Dhima A, de Hemptinne JC, Jose J |
3162 - 3171 |
From the correlation of binary systems involving supercritical CO2 and fatty acid esters to the prediction of (CO2-fish oils) phase behavior Jaubert JN, Coniglio L, Denet F |
3172 - 3175 |
Diffusion of aromatic hydrocarbon in ZSM-5 studied by the improved zero length column method Han MH, Yin XY, Jin Y, Chen S |
3176 - 3185 |
Volatile organic compound emission rates from mechanical surface aerators: Mass-transfer modeling Chern JM, Chou SR |
3186 - 3187 |
Comments on "Distillation columns containing structured packings: A comprehensive model for their performance. 1. Hydraulic models" Qiu JH |
3188 - 3189 |
Rebuttal to the comments of Dr. Jun-Hong Qiu on "Distillation columns containing structured packings: A comprehensive model for their performance. 1. Hydraulic models" Rocha JA, Bravo JL, Fair JR |
3190 - 3190 |
A mathematical programming model for water usage and treatment network design. (vol 38, pg 2679, 1999) Huang CH, Chang CT, Ling HC, Chang CC |