| 273 - 277 |
Difficulties in trying to model and scale-up the bubbling fluidized bed (BFB) reactor
Levenspiel O |
| 278 - 283 |
Surface decontamination of radioactive metal wastes using acid-in-supercritical CO2 emulsions
Koh M, Yoo J, Ju M, Joo B, Park K, Kim H, Kim H, Fournel B |
| 284 - 294 |
Experimental design to optimize the oxidation of Orange II dye solution using a clay-based Fenton-like catalyst
Herney-Ramirez J, Lampinen M, Vicente MA, Costa CA, Madeira LM |
| 295 - 302 |
Synthesis of zeolite from thermally treated sediment
Wu DY, Lu YK, Kong HN, Ye C, Jin XC |
| 303 - 310 |
Deactivation of modified iron oxide materials in the cyclic water gas shift process for CO-free hydrogen production
Galvita V, Hempel T, Lorenz H, Rihko-Struckmann LK, Sundmacher K |
| 311 - 322 |
Global kinetics for a commercial diesel oxidation catalyst with two exhaust hydrocarbons
Sampara CS, Bissett EJ, Chmielewski M |
| 323 - 331 |
Optimal design of synthesis gas production process with recycled carbon dioxide utilization
Choi S, Park J, Han C, Yoon ES |
| 332 - 343 |
Detection of unmeasured disturbances in model predictive control (MPC) plant test data
Dong HB, Riggs JB |
| 344 - 368 |
A comparative study of recent/popular PID tuning rules for stable, first-order plus dead time, single-input single-output processes
Lin MG, Lakshminarayanan S, Rangaiah GP |
| 369 - 379 |
Impact of multiple storage in wastewater minimization for multicontaminant batch plants: Toward zero effluent
Gouws JF, Majozi T |
| 380 - 393 |
Parameter estimation in continuous-time dynamic models in the presence of unmeasured states and nonstationary disturbances
Varziri MS, McAuley KB, McLellan PJ |
| 394 - 404 |
Improving agility of cryogenic air separation plants
Miller J, Luyben WL, Belanger P, Blouin S, Megan L |
| 405 - 411 |
Exponentially weighted moving average (EWMA) control charts for monitoring an analytical process
Carson PK, Yeh AB |
| 412 - 418 |
Enhancement of the CO2 retention capacity of Y zeolites by Na and Cs treatments: Effect of adsorption temperature and water treatment
Diaz E, Munoz E, Vega A, Ordonez S |
| 419 - 427 |
Variable MWPCA for adaptive process monitoring
Bin He X, Yang YP |
| 428 - 433 |
Recovery of molybdate from dilute aqueous solutions by complexation with cationic surfactants and extraction with isobutanol
Sameer N, Markwei M, Ramarao BV, Francis RC |
| 434 - 442 |
Compositional effects of nanocrystalline lithium zirconate on its CO2 capture properties
Ochoa-Fernandez E, Ronning M, Yu XF, Grande T, Chen D |
| 443 - 450 |
Liquid-liquid equilibria of the methyl oleate-glycerol-hexane-methanol system
Tizvar R, McLean DD, Kates M, Dube MA |
| 451 - 458 |
Semiempirical method for determining water content of methane-rich hydrocarbon gas in equilibrium with gas hydrates
Mohammadi AH, Richon D |
| 459 - 469 |
Phase equilibrium in two-phase, water-rich-liquid, hydrate systems: Experiment and theory
Zhang Y, Holder GD, Warzinski RP |
| 470 - 480 |
Computational investigation of horizontal slug flow in pneumatic conveying
Kuang SB, Chu KW, Yu AB, Zou ZS, Feng YQ |
| 481 - 485 |
Master curve for the discrete-element method
Lim EWC |
| 486 - 490 |
Neural network modeling and simulation of the solid/liquid activated carbon adsorption process
Kumar KV, Porkodi K, Rondon RLA, Rocha F |
