2177 - 2181 |
Comparison of the hydrothermal decomposition reactivities of chitin and cellulose Sakanishi K, Ikeyama N, Sakaki T, Shibata M, Miki T |
2182 - 2202 |
Metal ion separations by supported liquid membranes de Gyves J, de San Miguel ER |
2203 - 2209 |
Evaluation of a commercial mass spectrometer for its potential to measure auto exhaust constituents in real time Dearth MA |
2210 - 2215 |
Selective catalytic reduction of NO by NH3 over a bulk sulfated CuO/gamma-Al2O3 catalyst Jeong SM, Jung SH, Yoo KS, Kim SD |
2216 - 2224 |
Product distribution from pyrolysis of wood and agricultural residues Di Blasi C, Signorelli G, Di Russo C, Rea G |
2225 - 2230 |
Oxyethylation and oxypropylation of low molecular alcohols Hreczuch W, Poskrobko H, Pyzalski K, Szymanowski J |
2231 - 2237 |
A kinetic study of methanol oxidation in supercritical water Anitescu G, Zhang ZH, Tavlarides LL |
2238 - 2244 |
A round-robin study of cellulose pyrolysis kinetics by thermogravimetry Gronli M, Antal MJ, Varhegyi G |
2245 - 2253 |
Kinetics of the n-butoxylation of p-chloronitrobenzene under liquid-liquid-liquid phase transfer catalysis Yadav GD, Reddy CA |
2254 - 2259 |
Base hydrolysis of HMX and HMX-based plastic-bonded explosives with sodium hydroxide between 100 and 155 degrees C Bishop RL, Flesner RL, Dell'Orco PC, Spontarelli T, Larson SA, Bell DA |
2260 - 2263 |
A study of the effect of quench design on the quality of experimental kinetic data Hawboldt KA, Monnery WD, Svrcek WY |
2264 - 2267 |
In situ hypochlorous acid generation for the treatment of distillery spentwash Vijayaraghavan K, Ramanujam TK, Balasubramanian N |
2268 - 2274 |
Inhibition and deactivation effects in catalytic wet oxidation of high-strength alcohol-distillery liquors Belkacemi K, Larachi F, Hamoudi S, Turcotte G, Sayari A |
2275 - 2282 |
Solarthermal and solar quasi-electrolytic processing and separations: Zinc from zinc oxide as an example Fletcher EA |
2283 - 2291 |
Influence of surface modifiers on the structure of precipitated calcium carbonate Agnihotri R, Mahuli SK, Chauk SS, Fan LS |
2292 - 2298 |
Cuprous-chloride-modified nanoporous alumina membranes for ethylene-ethane separation Lin YS, Ji W, Wang Y, Higgins RJ |
2299 - 2309 |
Silica decomposition using a transferred arc process Addona T, Munz RJ |
2310 - 2314 |
Steel corrosion protection by means of alkyd paints pigmented with calcium acid phosphate del Amo B, Romagnoli R, Vetere VF |
2315 - 2329 |
Inherent dynamic problems with on-demand control structures Luyben WL |
2330 - 2344 |
Aggregated models for integrated distillation systems Caballero JA, Grossmann IE |
2345 - 2349 |
A neural-network-based nonlinear controller using an extended Kalman filter Gao FR, Wang FL, Li MZ |
2350 - 2363 |
Dynamic optimization with equality path constraints Feehery WF, Barton PI |
2364 - 2374 |
Optimal simulation-based operations planning with quantitative safety constraints Asprey SP, Batres R, Fuchino T, Naka Y |
2375 - 2382 |
Robust multivariable inverse-eased controllers: Theory and application Semino D, Pannocchia G |
2383 - 2390 |
Improved regulatory control of industrial gas-phase ethylene polymerization reactors Ali EM, Abasaeed AE, Al-Zahrani SR |
2391 - 2399 |
A strategy for detection of gross errors in nonlinear processes Renganathan T, Narasimhan S |
2400 - 2410 |
Design of simulated moving bed units under nonideal conditions Migliorini C, Gentilini A, Mazzotti M, Morbidelli M |
2411 - 2417 |
Design retrofit targets of pump-around refluxes for better energy integration of a crude distillation column Sharma R, Jindal A, Mandawala D, Jana SK |
2418 - 2424 |
Phase separation of liquid mixtures in the presence of surfactants Gupta R, Mauri R, Shinnar R |
2425 - 2427 |
Plant-scale method for the preparation of deuterium-depleted water Kotai L, Lippart J, Gacs I, Kazinczy B, Vidra L |
2428 - 2433 |
New crystallization of fatty acids from aqueous ethanol solution combined with liquid-liquid extraction Maeda K, Nomura Y, Tai M, Ueno Y, Fukui K, Hirota S |
2434 - 2438 |
Multisite Langmuir model applied to the interpretation of sorption of n-paraffins in 5A zeolite Silva JAC, Rodrigues AE |
2439 - 2449 |
Equilibrium theory for pressure swing adsorption. 5. Separation and purification in multicomponent adsorption Pigorini G, LeVan MD |
2450 - 2459 |
An integrated process for the removal of Cd and U from wet phosphoric acid Ortiz I, Alonso AI, Urtiaga AM, Demircioglu M, Kocacik N, Kabay N |
2460 - 2468 |
Heterogeneous modeling of gas absorption in emulsions Mehra A |
2469 - 2473 |
Adsorption of eutectic LiCl-KCl into zeolite 4A using a mechanically fluidized vacuum system Simpson MF, Battisti TJ |
2474 - 2481 |
Separation of hydroxycitric acid lactone from fruit pectins and polyhydroxyphenols on polybenzimidazole weak-base resin. Chanda M, Rempel GL |
2482 - 2484 |
Composition profile of an azeotropic continuous distillation with feed composition on a ridge or in a valley Li YH, Chen HF, Liu JQ |
2485 - 2490 |
A method to predict equilibrium conditions of gas hydrate formation in porous media Clarke MA, Pooladi-Darvish M, Bishnoi PR |
2491 - 2496 |
Correlation on the particle entrainment rate in gas fluidized beds Choi JH, Chang IY, Shun DW, Yi CK, Son JE, Kim SD |
2497 - 2502 |
Jet fuel system icing inhibitors: Synthesis and characterization Mushrush GW, Beal EJ, Hardy DR, Hughes JM, Cummings JC |
2503 - 2504 |
Effect of turbulent Schmidt number on mass-transfer rates to falling Liquid films Dudukovic A, Pjanovic R |
2505 - 2509 |
Projection velocities of droplets in the spray regime of sieve tray operation Chen JM, Liu YY, Tan TN |
2510 - 2512 |
Comments on "Enhancement of the global convergence-of using iterative dynamic programming to solve optimal control problems" Luus R |
2513 - 2514 |
Reply to comments oil "Enhancement of the global convergence of using iterative dynamic programming to solve optimal control problems" Hwang CY, Lin JS |