Year |
Citation |
Score |
2010 |
Biegler LT, Grossmann IE, Westerberg AW. Issues and trends in the teaching of process and product design Aiche Journal. 56: 1120-1125. DOI: 10.1002/Aic.12256 |
0.516 |
|
2005 |
Davis JG, Subrahmanian E, Westerberg AW. The "global" and the "local" in knowledge management Journal of Knowledge Management. 9: 101-112. DOI: 10.1108/13673270510582992 |
0.378 |
|
2005 |
Cheng L, Subrahmanian E, Westerberg AW. Multiobjective decision processes under uncertainty : Applications, problem formulations, and solution strategies Industrial & Engineering Chemistry Research. 44: 2405-2415. DOI: 10.1021/Ie049622+ |
0.68 |
|
2004 |
Cheng L, Subrahmanian E, Westerberg AW. Multi-objective Decisions on Capacity Planning and Production−Inventory Control under Uncertainty Industrial & Engineering Chemistry Research. 43: 2192-2208. DOI: 10.1021/Ie0303404 |
0.673 |
|
2004 |
Cheng L, Subrahmanian E, Westerberg AW. A comparison of optimal control and stochastic programming from a formulation and computation perspective Computers & Chemical Engineering. 29: 149-164. DOI: 10.1016/J.Compchemeng.2004.07.030 |
0.693 |
|
2004 |
Siirola JD, Hauan S, Westerberg AW. Computing Pareto fronts using distributed agents Computers & Chemical Engineering. 29: 113-126. DOI: 10.1016/J.Compchemeng.2004.07.012 |
0.787 |
|
2004 |
Westerberg AW. A retrospective on design and process synthesis Computers & Chemical Engineering. 28: 447-458. DOI: 10.1016/J.Compchemeng.2003.09.029 |
0.434 |
|
2003 |
Herder PM, Turk AL, Subrahmanian E, Westerberg AW. Collaborative learning in a cross-Atlantic design course J. of Design Research. 3: 0. DOI: 10.1504/Jdr.2003.009831 |
0.353 |
|
2003 |
Cheng L, Subrahmanian E, Westerberg AW. Multi-objective decision processes under uncertainty: Applications, problem formulations and solutions Computer-Aided Chemical Engineering. 15: 433-438. DOI: 10.1016/S1570-7946(03)80583-7 |
0.668 |
|
2003 |
Siirola JD, Hauan S, Westerberg AW. Toward agent-based process systems engineering: proposed framework and application to non-convex optimization Computers & Chemical Engineering. 27: 1801-1811. DOI: 10.1016/S0098-1354(03)00152-2 |
0.779 |
|
2003 |
Cheng L, Subrahmanian E, Westerberg A. Design and planning under uncertainty: issues on problem formulation and solution Computers & Chemical Engineering. 27: 781-801. DOI: 10.1016/S0098-1354(02)00264-8 |
0.68 |
|
2002 |
Herder PM, Subrahmanian E, Talukdar S, Turk AL, Westerberg AW. The use of video-taped lectures and web-based communications in teaching: A distance-teaching and cross-Atlantic collaboration experiment European Journal of Engineering Education. 27: 39-48. DOI: 10.1080/03043790110100209 |
0.351 |
|
2002 |
Rico-Ramı́rez V, Westerberg AW. Interior point methods for the solution of conditional models Computers & Chemical Engineering. 26: 375-383. DOI: 10.1016/S0098-1354(01)00769-4 |
0.506 |
|
2002 |
Rico-Ramirez V, Westerberg AW. Structural analysis of conditional models Computers & Chemical Engineering. 26: 359-373. DOI: 10.1016/S0098-1354(01)00768-2 |
0.423 |
|
2001 |
Davis JG, Subrahmanian E, Konda S, Granger H, Collins M, Westerberg AW. Creating Shared Information Spaces to Support Collaborative Design Work Information Systems Frontiers. 3: 377-392. DOI: 10.1023/A:1011469727367 |
0.405 |
|
2001 |
Lee JW, Hauan S, Westerberg AW. Feasibility of a reactive distillation column with ternary mixtures Industrial & Engineering Chemistry Research. 40: 2714-2728. DOI: 10.1021/Ie0005194 |
0.374 |
|
2001 |
Tyner KH, Westerberg AW. Multiperiod design of azeotropic separation systems II: Approximate models Computers and Chemical Engineering. 25: 1569-1583. DOI: 10.1016/S0098-1354(01)00722-0 |
0.459 |
|
2001 |
Tyner KH, Westerberg AW. Multiperiod design of azeotropic separation systems. I. An agent based solution Computers and Chemical Engineering. 25: 1267-1284. DOI: 10.1016/S0098-1354(01)00703-7 |
0.509 |
|
2001 |
Lee JW, Westerberg AW. Graphical design applied to MTBE and methyl acetate reactive distillation processes Aiche Journal. 47: 1333-1345. DOI: 10.1002/Aic.690470611 |
0.384 |
|
2000 |
Lee JW, Hauan S, Lien KM, Westerberg AW. A graphical method for designing reactive distillation columns. II. The McCabe-Thiele method Proceedings of the Royal Society a: Mathematical, Physical and Engineering Sciences. 456: 1965-1978. DOI: 10.1098/Rspa.2000.0597 |
0.383 |
|
2000 |
Lee JW, Hauan S, Lien KM, Westerberg AW. A graphical method for designing reactive distillation columns. I. The Ponchon-Savarit method Proceedings of the Royal Society a: Mathematical, Physical and Engineering Sciences. 456: 1953-1964. DOI: 10.1098/Rspa.2000.0596 |
0.404 |
|
2000 |
Lee JW, Hauan S, Westerberg AW. Circumventing an azeotrope in reactive distillation Industrial & Engineering Chemistry Research. 39: 1061-1063. DOI: 10.1021/Ie990447K |
0.367 |
|
2000 |
Westerberg AW, Lee JW, Hauan S. Synthesis of distillation-based processes for non-ideal mixtures Computers & Chemical Engineering. 24: 2043-2054. DOI: 10.1016/S0098-1354(00)00575-5 |
0.401 |
|
2000 |
Lee JW, Westerberg AW. Visualization of stage calculations in ternary reacting mixtures Computers & Chemical Engineering. 24: 639-644. DOI: 10.1016/S0098-1354(00)00366-5 |
0.356 |
|
2000 |
Lee JW, Hauan S, Lien KM, Westerberg AW. Difference points in extractive and reactive cascades. II - Generating design alternatives by the lever rule for reactive systems Chemical Engineering Science. 55: 3161-3174. DOI: 10.1016/S0009-2509(99)00590-4 |
0.425 |
|
2000 |
Hauan S, Westerberg AW, Lien KM. Phenomena-based analysis of fixed points in reactive separation systems Chemical Engineering Science. 55: 1053-1075. DOI: 10.1016/S0009-2509(99)00392-9 |
0.418 |
|
2000 |
Lee JW, Hauan S, Westerberg AW. Extreme conditions in binary reactive distillation Aiche Journal. 46: 2225-2236. DOI: 10.1002/Aic.690461114 |
0.393 |
|
2000 |
Grossmann IE, Westerberg AW. Research challenges in process systems engineering Aiche Journal. 46: 1700-1703. DOI: 10.1002/Aic.690460902 |
0.504 |
|
2000 |
Lee JW, Hauan S, Westerberg AW. Graphical methods for reaction distribution in a reactive distillation column Aiche Journal. 46: 1218-1233. DOI: 10.1002/Aic.690460614 |
0.352 |
|
1999 |
Allan BA, Westerberg AW. Anonymous class in declarative process modeling Industrial & Engineering Chemistry Research. 38: 692-704. DOI: 10.1021/Ie980297Y |
0.446 |
|
1999 |
Rico-Ramirez V, Allan BA, Westerberg AW. Conditional Modeling. 1. Requirements for an Equation-Based Environment Industrial & Engineering Chemistry Research. 38: 519-530. DOI: 10.1021/Ie9800593 |
0.43 |
|
1999 |
Reich Y, Konda S, Subrahmanian E, Cunningham D, Dutoit A, Patrick R, Thomas M, Westerberg AW. Building Agility for Developing Agile Design Information Systems Research in Engineering Design. 11: 67-83. DOI: 10.1007/Pl00003884 |
0.397 |
|
1999 |
Davis JG, Subrahmanian E, Westerberg AW. SCOPE: a blackboard model-based decision support system for crude-oil trading International Journal of Intelligent Systems in Accounting, Finance & Management. 8: 89-104. DOI: 10.1002/(Sici)1099-1174(199906)8:2<89::Aid-Isaf166>3.0.Co;2-G |
0.406 |
|
1997 |
Safrit BT, Westerberg AW. Synthesis of Azeotropic Batch Distillation Separation Systems Industrial & Engineering Chemistry Research. 36: 1841-1854. DOI: 10.1021/Ie960345J |
0.43 |
|
1997 |
Safrit BT, Westerberg AW. Algorithm for Generating the Distillation Regions for Azeotropic Multicomponent Mixtures Industrial & Engineering Chemistry Research. 36: 1827-1840. DOI: 10.1021/Ie960344R |
0.412 |
|
1997 |
Safrit BT, Westerberg AW. Improved Operational Policies for Batch Extractive Distillation Columns Industrial & Engineering Chemistry Research. 36: 436-443. DOI: 10.1021/Ie960343Z |
0.376 |
|
1997 |
Westerberg AW, Subrahmainan E, Reich Y, Konda S. Designing the process design process Computers & Chemical Engineering. 21. DOI: 10.1016/S0098-1354(97)87470-4 |
0.424 |
|
1997 |
Abbott KA, Allan BA, Westerberg AW. Global preordering for Newton equations using model hierarchy Aiche Journal. 43: 3193-3204. DOI: 10.1002/Aic.690431207 |
0.497 |
|
1996 |
Huss RS, Westerberg AW. Collocation Methods for Distillation Design. 2. Applications for Distillation Industrial & Engineering Chemistry Research. 35: 1611-1623. DOI: 10.1021/Ie9503508 |
0.502 |
|
1996 |
Huss RS, Westerberg AW. Collocation Methods for Distillation Design. 1. Model Description and Testing Industrial & Engineering Chemistry Research. 35: 1603-1610. DOI: 10.1021/Ie9503499 |
0.425 |
|
1996 |
Westerberg AW, Wahnschafft O. Synthesis of Distillation-Based Separation Systems Advances in Chemical Engineering. 23. DOI: 10.1016/S0065-2377(08)60202-1 |
0.386 |
|
1995 |
Safrit BT, Westerberg AW, Diwekar U, Wahnschafft OM. Extending Continuous Conventional and Extractive Distillation Feasibility Insights to Batch Distillation Industrial & Engineering Chemistry Research. 34: 3257-3264. DOI: 10.1021/Ie00037A012 |
0.392 |
|
1995 |
Modi AK, Newell A, Steier DM, Westerberg AW. Building a chemical process design system within soar—2. Learning issues Computers & Chemical Engineering. 19: 345-361. DOI: 10.1016/0098-1354(94)00056-T |
0.436 |
|
1994 |
Wahnschafft OM, Köhler JW, Westerberg AW. Homogeneous azeotropic distillation: Analysis of separation feasibility and consequences for entrainer selection and column design Computers & Chemical Engineering. 18. DOI: 10.1016/0098-1354(94)80006-5 |
0.416 |
|
1993 |
Westerberg AW, Westerberg KM, Westerberg KW, Chung Y, Safrit B. Why standard integration packages fail on a near index problem Industrial & Engineering Chemistry Research. 32: 1798-1799. DOI: 10.1021/Ie00020A039 |
0.724 |
|
1993 |
Wahnschafft OM, Rudulier JPL, Westerberg AW. A problem decomposition approach for the synthesis of complex separation processes with recycles Industrial & Engineering Chemistry Research. 32: 1121-1141. DOI: 10.1021/Ie00018A019 |
0.472 |
|
1993 |
Wahnschafft OM, Westerberg AW. The product composition regions of azeotropic distillation columns. 2. Separability in two-feed columns and entrainer selection Industrial & Engineering Chemistry Research. 32: 1108-1120. DOI: 10.1021/Ie00018A018 |
0.409 |
|
1993 |
Subrahmanian E, Konda SL, Levy SN, Reich Y, Westerberg AW, Monarch I. Equations aren't enough: informal modeling in design Ai Edam Artificial Intelligence For Engineering Design, Analysis and Manufacturing. 7: 257-274. DOI: 10.1017/S0890060400000354 |
0.428 |
|
1992 |
Piela P, McKelvey R, Westerberg A. An introduction to the ASCEND modeling system: its language and interactive environment Journal of Management Information Systems. 9: 91-121. DOI: 10.1080/07421222.1992.11517969 |
0.401 |
|
1992 |
Chung Y, Westerberg AW. Solving a class of near index problems as perturbations of index problems Industrial & Engineering Chemistry Research. 31: 2593-2603. DOI: 10.1021/Ie00011A026 |
0.713 |
|
1992 |
Smith OJ, Westerberg AW. Acceleration of cyclic steady state convergence for pressure swing adsorption models Industrial & Engineering Chemistry Research. 31: 1569-1573. DOI: 10.1021/Ie00006A021 |
0.383 |
|
1992 |
Modi AK, Westerberg AW. Distillation column sequencing using marginal price Industrial & Engineering Chemistry Research. 31: 839-848. DOI: 10.1021/Ie00003A028 |
0.44 |
|
1992 |
Wahnschafft OM, Rudulier JPL, Blania P, Westerberg AW. Split: II. Authomated synthesis of hybrid liquid separation systems Computers & Chemical Engineering. 16. DOI: 10.1016/S0098-1354(09)80036-7 |
0.432 |
|
1992 |
Smith OJ, Westerberg AW. The optimal design of pressure swing adsorption systems—II Chemical Engineering Science. 47: 4213-4217. DOI: 10.1016/0009-2509(92)85170-G |
0.462 |
|
1991 |
Westerberg AW. 23 Process Engineering Advances in Chemical Engineering. 16: 499-523. DOI: 10.1016/S0065-2377(08)60171-4 |
0.4 |
|
1991 |
Piela PC, Epperly TG, Westerberg KM, Westerberg AW. ASCEND: an object-oriented computer environment for modeling and analysis: The modeling language Computers & Chemical Engineering. 15: 53-72. DOI: 10.1016/0098-1354(91)87006-U |
0.427 |
|
1991 |
Wahnschafft OM, Jurain TP, Westerberg AW. SPLIT : a separation process designer Computers & Chemical Engineering. 15: 565-581. DOI: 10.1016/0098-1354(91)80012-K |
0.533 |
|
1991 |
Smith OJ, Westerberg AW. The optimal design of pressure swing adsorption systems Chemical Engineering Science. 46: 2967-2976. DOI: 10.1016/0009-2509(91)85001-E |
0.408 |
|
1990 |
Chung Y, Westerberg AW. A proposed numerical algorithm for solving nonlinear index problems Industrial & Engineering Chemistry Research. 29: 1234-1239. DOI: 10.1021/Ie00103A023 |
0.719 |
|
1990 |
Westerberg A, Grossmann I, Talukdar S, Prinz F, Fenves S, Maher ML. Applications of AI in design research at Carnegie Mellon University's EDRC Artificial Intelligence in Engineering. 5: 110-124. DOI: 10.1016/0954-1810(90)90005-O |
0.516 |
|
1990 |
Clark PA, Westerberg AW. Bilevel programming for steady-state chemical process design—I. Fundamentals and algorithms Computers & Chemical Engineering. 14: 87-97. DOI: 10.1016/0098-1354(90)87007-C |
0.516 |
|
1990 |
Wehe RR, Westerberg AW. A bounding procedure for the minimum number of columns in nonsharp distillation sequences Chemical Engineering Science. 45: 1-11. DOI: 10.1016/0009-2509(90)87075-4 |
0.42 |
|
1990 |
Smith OJ, Westerberg AW. Mixed-integer programming for pressure swing adsorption cycle scheduling Chemical Engineering Science. 45: 2833-2842. DOI: 10.1016/0009-2509(90)80176-F |
0.451 |
|
1989 |
Carlberg NA, Westerberg AW. Temperature-heat diagrams for complex columns. 3. Underwood's method for the Petlyuk configuration Industrial & Engineering Chemistry Research. 28: 1386-1397. DOI: 10.1021/Ie00093A018 |
0.353 |
|
1989 |
Carlberg NA, Westerberg AW. Temperature-heat diagrams for complex columns. 2. Underwood's method for side strippers and enrichers Industrial & Engineering Chemistry Research. 28: 1379-1386. DOI: 10.1021/Ie00093A017 |
0.387 |
|
1989 |
Terranova BE, Westerberg AW. Temperature-heat diagrams for complex columns. 1. Intercooled/interheated distillation columns Industrial & Engineering Chemistry Research. 28: 1374-1379. DOI: 10.1021/Ie00093A016 |
0.351 |
|
1989 |
Westerberg AW. Synthesis in engineering design Computers & Chemical Engineering. 13: 365-376. DOI: 10.1016/0098-1354(89)85016-1 |
0.393 |
|
1988 |
Banãres-Alcántara R, Ko EI, Westerberg AW, Rychener MD. DECADE-a hybrid expert system for catalyst selection-II. Final architecture and results Computers and Chemical Engineering. 12: 923-938. DOI: 10.1016/0098-1354(88)87018-2 |
0.383 |
|
1988 |
Westerberg AW, Hillenbrand JB. The synthesis of multiple-effect evaporator systems using minimum utility insights—II. liquid flowpattern selection Computers & Chemical Engineering. 12: 625-636. DOI: 10.1016/0098-1354(88)80004-8 |
0.381 |
|
1988 |
Hillenbrand JB, Westerberg AW. The synthesis of multiple-effect evaporator systems using minimum utility insights—I. A cascaded heat representation Computers & Chemical Engineering. 12: 611-624. DOI: 10.1016/0098-1354(88)80003-6 |
0.407 |
|
1987 |
Vaselenak JA, Grossmann IE, Westerberg AW. Optimal retrofit design of multiproduct batch plants Industrial & Engineering Chemistry Research. 26: 718-726. DOI: 10.1021/Ie00064A016 |
0.518 |
|
1987 |
Vaselenak JA, Grossmann IE, Westerberg AW. An embedding formulation for the optimal scheduling and design of multipurpose batch plants Industrial & Engineering Chemistry Research. 26: 139-148. DOI: 10.1021/Ie00061A027 |
0.599 |
|
1987 |
Wehe RR, Westerberg AW. An algorithmic procedure for the synthesis of distillation sequences with bypass Computers & Chemical Engineering. 11: 619-627. DOI: 10.1016/0098-1354(87)87007-2 |
0.491 |
|
1987 |
Bañares-Alcántara R, Westerberg AW, Ko EI, Rychener MD. Decade-A hybrid expert system for catalyst selection-I. Expert system consideration Computers and Chemical Engineering. 11: 265-277. DOI: 10.1016/0098-1354(87)85008-1 |
0.456 |
|
1987 |
Lien K, Suzuki G, Westerberg AW. The role of expert systems technology in design Chemical Engineering Science. 42: 1049-1071. DOI: 10.1016/0009-2509(87)80056-8 |
0.512 |
|
1986 |
Vaselenak JA, Grossmann IE, Westerberg AW. Heat integration in batch processing Industrial & Engineering Chemistry Process Design and Development. 25: 357-366. DOI: 10.1021/I200033A004 |
0.495 |
|
1986 |
Hrymak AN, McRae GJ, Westerberg AW. An implementation of a moving finite element method Journal of Computational Physics. 63: 168-190. DOI: 10.1016/0021-9991(86)90090-2 |
0.414 |
|
1986 |
Westerberg AW, Bingzhen C. Structural flexibility for heat integrated distillation columns—II. Synthesis Chemical Engineering Science. 41: 355-363. DOI: 10.1016/0009-2509(86)87016-6 |
0.484 |
|
1986 |
Hrymak AN, Westerberg AW. Computational considerations for moving finite element methods Chemical Engineering Science. 41: 1673-1680. DOI: 10.1016/0009-2509(86)85245-9 |
0.424 |
|
1985 |
Hrymak AN, McRae GJ, Westerberg AW. Combined Analysis and Optimization of Extended Heat Transfer Surfaces Journal of Heat Transfer. 107: 527-532. DOI: 10.1115/1.3247456 |
0.482 |
|
1985 |
Biegler L, Grossmann I, Westerberg A. A note on approximation techniques used for process optimization Computers & Chemical Engineering. 9: 201-206. DOI: 10.1016/0098-1354(85)85010-9 |
0.598 |
|
1985 |
Kuru S, Westerberg AW. A Newton-Raphson based strategy for exploiting latency in dynamic simulation Computers & Chemical Engineering. 9: 175-182. DOI: 10.1016/0098-1354(85)85007-9 |
0.432 |
|
1985 |
Bañares-Alcántara R, Westerberg AW, Rychener MD. Development of an expert system for physical property predictions Computers & Chemical Engineering. 9: 127-142. DOI: 10.1016/0098-1354(85)85003-1 |
0.432 |
|
1985 |
Westerberg AW, Benjamin DRja. Thoughts on a future equation-oriented flowsheeting system☆ Computers & Chemical Engineering. 9: 517-526. DOI: 10.1016/0098-1354(85)80026-0 |
0.417 |
|
1985 |
Westerberg AW. The synthesis of distillation-based separation systems Computers & Chemical Engineering. 9: 421-429. DOI: 10.1016/0098-1354(85)80020-X |
0.45 |
|
1985 |
Westerberg AW, Andrecovich MJ. Utility bounds for nonconstant QΔT for heat‐integrated distillation sequence synthesis Aiche Journal. 31: 1475-1479. DOI: 10.1002/Aic.690310909 |
0.423 |
|
1985 |
Andrecovich MJ, Westerberg AW. An MILP formulation for heat‐integrated distillation sequence synthesis Aiche Journal. 31: 1461-1474. DOI: 10.1002/Aic.690310908 |
0.519 |
|
1985 |
Andrecovich MJ, Westerberg AW. A Simple Synthesis Method Based on Utility Bounding for Heat‐Integrated Distillation Sequences Aiche Journal. 31: 363-375. DOI: 10.1002/Aic.690310303 |
0.492 |
|
1983 |
Locke MH, Westerberg AW. The ASCEND-II system ― a flowsheeting application of a successive quadratic programming methodology Computers & Chemical Engineering. 7: 615-630. DOI: 10.1016/0098-1354(83)80007-6 |
0.499 |
|
1983 |
Cerda J, Westerberg AW, Mason D, Linnhoff B. Minimum utility usage in heat exchanger network synthesis : a transportation problem Chemical Engineering Science. 38: 373-387. DOI: 10.1016/0009-2509(83)80156-0 |
0.458 |
|
1982 |
Grimes LE, Rychener MD, Westerberg AW. The synthesis and evolution of networks of heat exchange that feature the minimum number of units Chemical Engineering Communications. 14: 339-360. DOI: 10.1080/00986448208911053 |
0.415 |
|
1981 |
Cerda J, Westerberg AW. Shortcut methods for complex distillation columns. 1. Minimum reflux Industrial & Engineering Chemistry Process Design and Development. 20: 546-557. DOI: 10.1021/I200014A028 |
0.447 |
|
1981 |
Motard RL, Westerberg AW. Exclusive tear sets for flowsheets Aiche Journal. 27: 725-732. DOI: 10.1002/Aic.690270504 |
0.366 |
|
1981 |
Nishida N, Stephanopoulos G, Westerberg AW. A review of process synthesis Aiche Journal. 27: 321-351. DOI: 10.1002/Aic.690270302 |
0.661 |
|
1980 |
Berna TJ, Locke MH, Westerberg AW. A new approach to optimization of chemical processes Aiche Journal. 26: 37-43. DOI: 10.1002/Aic.690260107 |
0.482 |
|
1978 |
Westerberg AW, Shah JV. Assuring a global optimum by the use of an upper bound on the lower (dual) bound Computers and Chemical Engineering. 2: 83-92. DOI: 10.1016/0098-1354(78)80012-X |
0.455 |
|
1978 |
Westerberg AW, Director SW. A modified least squares algorithm for solving sparse n × n sets of nonlinear equations Computers and Chemical Engineering. 2: 77-81. DOI: 10.1016/0098-1354(78)80011-8 |
0.414 |
|
1978 |
Westerberg AW, Berna TJ. Decomposition of very large-scale Newton-Raphson based flowsheeting problems Computers & Chemical Engineering. 2: 61-63. DOI: 10.1016/0098-1354(78)80008-8 |
0.485 |
|
1977 |
Seader JD, Westerberg AW. A combined heuristic and evolutionary strategy for synthesis of simple separation sequences Aiche Journal. 23: 951-954. DOI: 10.1002/Aic.690230628 |
0.376 |
|
1977 |
Shah JV, Westerberg AW. Process synthesis using structural parameters: A problem with inequality constraints Aiche Journal. 23: 378-380. DOI: 10.1002/Aic.690230323 |
0.45 |
|
1976 |
Stephanopoulos G, Westerberg AW. Studies in process synthesis—II: Evolutionary synthesis of optimal process flowsheets☆ Chemical Engineering Science. 31: 195-204. DOI: 10.1016/0009-2509(76)85057-9 |
0.646 |
|
1976 |
Allen GL, Westerberg AW. Solution procedures for indexed equation sets: Structural considerations Aiche Journal. 22: 549-558. DOI: 10.1002/Aic.690220319 |
0.417 |
|
1975 |
Westerberg AW, Stephanopoulos G. Studies in process synthesis—I: Branch and bound strategy with list techniques for the synthesis of separation schemes Chemical Engineering Science. 30: 963-972. DOI: 10.1016/0009-2509(75)80063-7 |
0.655 |
|
1975 |
Stephanopoulos G, Westerberg AW. The use of Hestenes' method of multipliers to resolve dual gaps in engineering system optimization Journal of Optimization Theory and Applications. 15: 285-309. DOI: 10.1007/Bf00933339 |
0.681 |
|
1975 |
Stephanopoulos G, Westerberg AW. Synthesis of optimal process flowsheets by an infeasible decomposition technique in the presence of functional non‐convexities Canadian Journal of Chemical Engineering. 53: 551-555. DOI: 10.1002/Cjce.5450530515 |
0.628 |
|
1974 |
Westerberg AW, Stephanopoulos G. A Stronger Version of the Discrete Minimum Principle Industrial & Engineering Chemistry Fundamentals. 13: 231-237. DOI: 10.1021/I160051A013 |
0.606 |
|
1974 |
Gupta PK, Westerberg AW, Hendry JE, Hughes RR. Assigning output variables to equations using linear programming Aiche Journal. 20: 397-399. DOI: 10.1002/Aic.690200231 |
0.364 |
|
1973 |
Stephanopoulos G, Westerberg AW. Overcoming deficiencies of the two-level method for systems optimization Aiche Journal. 19: 1269-1271. DOI: 10.1002/Aic.690190634 |
0.6 |
|
1973 |
Westerberg AW, Debrosse CJ. An optimization algorithm for structured design systems Aiche Journal. 19: 335-343. DOI: 10.1002/Aic.690190219 |
0.502 |
|
1973 |
Debrosse CJ, Westerberg AW. A feasible‐point algorithm for structured design systems in chemical engineering Aiche Journal. 19: 251-258. DOI: 10.1002/Aic.690190208 |
0.456 |
|
1972 |
McGalliard RL, Westerberg AW. Structural sensitivity analysis in design synthesis Chemical Engineering Journal. 4: 127-138. DOI: 10.1016/0300-9467(72)80005-4 |
0.462 |
|
1971 |
Westerberg AW, Edie FC. Computer-Aided Design, Part 2 An approach to convergence and tearing in the solution of sparse equation sets Chemical Engineering Journal. 2: 17-25. DOI: 10.1016/0300-9467(71)87003-X |
0.42 |
|
1971 |
Westerberg AW, Edie FC. Computer-aided design, Part 1 enhancing convergence properties by the choice of output variable assignments in the solution of Sparse equation sets Chemical Engineering Journal. 2: 9-16. DOI: 10.1016/0300-9467(71)87002-8 |
0.459 |
|
1971 |
Edie FC, Westerberg AW. Computer-aided design: Part 3 decision variable selection to avoid hidden singularities in resulting recycle calculations Chemical Engineering Journal. 2: 114-124. DOI: 10.1016/0300-9467(71)80005-9 |
0.442 |
|
Show low-probability matches. |