4269 - 4276 |
Investigation of the chemical basis for inefficient lignin removal in softwood kraft pulp during oxygen delignification Fu SY, Lucia LA |
4277 - 4282 |
Gasification of alkylphenols with supported noble metal catalysts in supercritical water Sato T, Osada M, Watanabe M, Shirai M, Arai K |
4283 - 4289 |
Alkylation of isobutane with C3-C5 olefins to produce high-quality gasolines: Physicochemical sequence of events Albright LF |
4290 - 4295 |
Decomposition and oxidation of pyrite in a fixed-bed reactor Hansen JP, Jensen LS, Wedel S, Dam-Johansen K |
4296 - 4302 |
Poly(methacrylic acid) grafted with poly(ethylene glycol) and n-dodecane as pH-sensitive surfactants for water-in-oil fermentations Restrepo AS, Ju LK |
4303 - 4310 |
Bath-substrate-flow method for evaluating the detersive and dispersant performance of hard-surface detergents Alameda EJ, Rodriguez VB, Moreno RB, Olea JN, Vaz DA |
4311 - 4318 |
Emulsion catastrophic inversion from abnormal to normal morphology. 3. Conditions for triggering the dynamic inversion and application to industrial processes Tyrode E, Mira I, Zambrano N, Marquez L, Rondon-Gonzalez M, Salager JL |
4319 - 4328 |
Rigorous graphical targeting for resource conservation via material recycle/reuse networks El-Halwagi MM, Gabriel F, Harell D |
4329 - 4339 |
Synthesis of heat-integrated thermally coupled distillation systems for multicomponent separations Rong BG, Kraslawski A, Turunen I |
4340 - 4347 |
Design for operability: A singular-value optimization approach within a multiple-objective framework Blanco AM, Bandoni JA |
4348 - 4365 |
Effects of process design on recycle dynamics and its implication to control structure selection Cheng YC, Yu CC |
4366 - 4375 |
Optimal sensor placement and maintenance strategies for mass-flow networks Lai CA, Chang CT, Ko CL, Chen CL |
4376 - 4381 |
High-temperature oxygen sorption in a fixed bed packed with perovskite-type ceramic sorbents Yang ZH, Lin YS |
4382 - 4388 |
Thermodynamics of mixtures containing organic carbonates. 14. Excess molar Gibbs energies for 1-hexanol plus dimethyl or diethyl carbonate systems at 353.15 and 363.15 K. Comparison with ERAS results Sporzynski A, Szurgocinska M, Domanska U, Gonzalez JA |
4389 - 4397 |
Analysis of the Stefan tube at supercritical conditions and diffusion coefficient measurements Ozguler EI, Sunol SG, Sunol AK |
4398 - 4405 |
Sorption thermodynamics and mutual diffusivity of carbon dioxide in molten polycaprolactone Cotugno S, Di Maio E, Ciardiello C, Iannace S, Mensitieri G, Nicolais L |
4406 - 4413 |
Ideal multicomponent liquid solution as a mixed solvent Ruckenstein E, Shulgin I |
4414 - 4421 |
Prediction of the pK(a) values of amines using ab initio methods and free-energy perturbations da Silva EF, Svendsen HF |
4422 - 4422 |
New general continuous-time state-task network formulation for short-term scheduling of multipurpose batch plants. (vol 42, pg 3073, 2003) Maravelias CT, Grossmann IE |