1 - 11 |
MILP reformulations for the design of biotechnological multi-product batch plants using continuous equipment sizes and discrete host selection Sandoval G, Espinoza D, Figueroa N, Asenjo JA |
12 - 27 |
Timed-automata based method for synthesizing diagnostic tests in batch processes Hsieh WC, Chang CT |
28 - 35 |
Comparison of Monte Carlo and quasi-Monte Carlo technique in structure and relaxing dynamics of polymer in dilute solution Mukherjee R, Diwekar UM |
36 - 42 |
In situ adaptive tabulation (ISAT) to accelerate transient computational fluid dynamics with complex heterogeneous chemical kinetics Blasi JM, Kee RJ |
43 - 48 |
CFD modelling of a mixing chamber for the realisation of functionally graded scaffolds Mattei G, Vozzi G |
49 - 62 |
A new model and a reformulation for the crude distillation unit charging problem with oil blends and sequence-dependent changeover costs Cortez LCS, Pessoa AA |
63 - 82 |
Optimal design of integrated agricultural water networks Rubio-Castro E, Ponce-Ortega JM, Cervantes-Gaxiola ME, Hernandez-Calderon OM, Ortiz-del-Castillo JR, Milan-Carrillo J, Hernandez-Martinez JF, Meza-Contreras JA |
83 - 95 |
Optimal strategies for transitions in simulated moving bed chromatography Vignesh SV, Hariprasad K, Athawale P, Siram V, Bhartiya S |
96 - 103 |
Modeling and simulation of VMD desalination process by ANN Cao WS, Liu Q, Wang YQ, Mujtaba IM |
104 - 116 |
Fault diagnosis of chemical processes with incomplete observations: A comparative study Askarian M, Escudero G, Graells M, Zarghami R, Jalali-Farahani F, Mostoufi N |
117 - 131 |
Operational optimization of networks of compressors considering condition-based maintenance Xenos DP, Kopanos GM, Cicciotti M, Thornhill NF |
132 - 150 |
Population balance discretization for growth, attrition, aggregation, breakage and nucleation Bertin D, Cotabarren I, Pina J, Bucala V |
151 - 161 |
Spatio-temporal frequency response analysis of forced slip velocity effect on solute concentration oscillations in a reverse osmosis membrane channel Ratnayake P, Setiawan R, Bao J, Fimbres-Weihs G, Wiley DE |
162 - 170 |
Model predictive control with non-uniformly spaced optimization horizon for multi-timescale processes Tan CK, Tippett MJ, Bao J |
171 - 179 |
Numerical simulations of gas-liquid flow in thermal sorption processes Weber A, Herzog N, Bergmann T |
180 - 198 |
Fleet sizing in chemical supply chains using agent-based simulation Sha M, Srinivasan R |
199 - 207 |
Optimal design for flexible operation of the post-combustion CO2 capture plant with uncertain economic factors Zaman M, Jang H, Rizwan M, Lee JH |
208 - 216 |
Price model of electrical energy for PSE applications Manca D |
217 - 225 |
Numerical simulation of gas-diffusion-electrodes with moving gas-liquid interface: A study on pulse-current operation and electrode flooding Schroder D, Laue V, Krewer U |
226 - 236 |
Optimization of naphtha purchase price using a price prediction model Kwon H, Lyu B, Tak K, Lee J, Cho JH, Moon I |
237 - 254 |
Global optimization of multiphase flow networks using spline surrogate models Grimstad B, Foss B, Heddle R, Woodman M |
255 - 280 |
Human immunomodulation and initial HIV spread Joly M, Odloak D, Rondo PHC |
281 - 289 |
Comprehensive Fischer-Tropsch reactor model with non-ideal plug flow and detailed reaction kinetics Haarlemmer G, Bensabath T |
290 - 301 |
Techno-economic assessment of CO2 bio-fixation using microalgae in connection with three different state-of-the-art power plants Rezvani S, Moheimani NR, Bahri PA |
302 - 312 |
Polygeneration of hydrogen and power based on coal gasification integrated with a dual chemical looping process: Thermodynamic investigation Zhu L, Zhang Z, Fan JM, Jiang P |
313 - 325 |
Integration of wind, solar and biomass over a year for the constant production of CH4 from CO2 and water Martin M, Davis W |
326 - 337 |
Reconstruction of a distribution from a finite number of its moments: A comparative study in the case of depolymerization process Lebaz N, Cockx A, Sperandio M, Morchain J |
338 - 349 |
GMM and optimal principal components-based Bayesian method for multimode fault diagnosis Jiang QC, Huang B, Yan XF |
350 - 362 |
Fast arbitrary order moments and arbitrary precision solution of the general rate model of column liquid chromatography with linear isotherm Leweke S, von Lieres E |
363 - 370 |
Hybrid optimization technique for cyclic steam stimulation by horizontal wells in heavy oil reservoir Hou J, Zhou K, Zhao H, Kang XD, Wang ST, Zhang XS |
371 - 381 |
A toolbox using the stochastic optimization algorithm MIPT and ChemCAD for the systematic process retrofit of complex chemical processes Otte D, Lorenz HM, Repke JU |
382 - 393 |
A discrete-time scheduling model for continuous power-intensive process networks with various power contracts Zhang Q, Sundaramoorthy A, Grossmanna IE, Pinto JM |
394 - 408 |
Definition and validation of a patient-individualized physiologically-based pharmacokinetic model Abbiati RA, Lamberti G, Grassi M, Trotta F, Manca D |
409 - 421 |
Flexibility analysis of process supply chain networks Wang H, Mastragostino R, Swartz CLE |
422 - 433 |
Medium-term maintenance turnaround planning under uncertainty for integrated chemical sites Amaran S, Zhang T, Sahinidis NV, Sharda B, Bury SJ |
434 - 445 |
A comparative simulation study of power generation plants involving chemical looping combustion systems Petriz-Prieto MA, Rico-Ramirez V, Gonzalez-Alatorre G, Gomez-Castro FI, Diwekar UM |
446 - 457 |
A synchronous cellular automaton model of mass transport in porous media Gurikov A, Kolnoochenko A, Golubchikov M, Menshutina N, Smirnova I |
458 - 481 |
Bifurcation control of high-dimensional nonlinear chemical processes using an extended washout-filter algorithm Zhang N, Seider WD, Chen BZ |
482 - 492 |
Synthesis and design of new hybrid configurations for biobutanol purification Errico M, Sanchez-Ramirez E, Quiroz-Ramirez JJ, Segovia-Hernandez JG, Rong BG |
493 - 506 |
Efficient multi-product multi-BOM batch scheduling for a petrochemical blending plant with a shared pipeline network Hill A, Cornelissens T, Sorensen K |
507 - 515 |
A reactive optimization strategy for the simultaneous planning, scheduling and control of short-period continuous reactors Gutierrez-Limon MA, Flores-Tlacuahuac A, Grossmann IE |
516 - 535 |
Preprocessing and tightening methods for time-indexed MIP chemical production scheduling models Merchan AF, Maravelias CT |
536 - 545 |
Optimal design of batch mass exchange networks with multipurpose exchange units Zhou RJ, Li LJ, Dong HG |
546 - 557 |
A decomposition methodology for dynamic modeling of cold box in offshore natural gas liquefaction process Lee CJ, Song K, Lee Y, Han C |
558 - 567 |
First-principles models and sensitivity analysis for the lignocellulosic biomass-to-methanol conversion process Manenti F, Adani F, Rossi F, Bozzano G, Pirola C |
568 - 598 |
New a priori and a posteriori probabilistic bounds for robust counterpart optimization: I. Unknown probability distributions Guzman YA, Matthews LR, Floudas CA |
599 - 610 |
Optimal scenario reduction framework based on distance of uncertainty distribution and output performance: II. Sequential reduction Li ZK, Floudas CA |
611 - 626 |
Inventory pinch gasoline blend scheduling algorithm combining discrete-and continuous-time models Castillo-Castillo PA, Mahalec V |
627 - 646 |
Improved continuous-time model for gasoline blend scheduling Castillo-Castillo PA, Mahalec V |