| Year |
Citation |
Score |
| 2020 |
Reyes-Lúa A, Skogestad S. Systematic design of active constraint switching using classical advanced control structures Industrial & Engineering Chemistry Research. 59: 2229-2241. DOI: 10.1021/Acs.Iecr.9B04511 |
0.499 |
|
| 2020 |
Reyes-Lúa A, Skogestad S. Correction to “Systematic Design of Active Constraint Switching Using Classical Advanced Control Structures” Industrial & Engineering Chemistry Research. 59: 9342-9342. DOI: 10.1021/Acs.Iecr.0C01977 |
0.386 |
|
| 2020 |
Reyes-Lúa A, Skogestad S. Multi-input single-output control for extending the operating range: Generalized split range control using the baton strategy Journal of Process Control. 91: 1-11. DOI: 10.1016/J.Jprocont.2020.05.001 |
0.517 |
|
| 2020 |
Zotică C, Nord LO, Kovács J, Skogestad S. Optimal Operation and Control of Heat to Power Cycles: a New Perspective from a Systematic Plantwide Control Approach Computers & Chemical Engineering. 141: 106995. DOI: 10.1016/J.Compchemeng.2020.106995 |
0.429 |
|
| 2020 |
Jahanshahi E, Krishnamoorthy D, Codas A, Foss B, Skogestad S. Plantwide control of an oil production network Computers & Chemical Engineering. 136: 106765. DOI: 10.1016/J.Compchemeng.2020.106765 |
0.46 |
|
| 2019 |
Krishnamoorthy D, Skogestad S. Online Process Optimization with Active Constraint Set Changes using Simple Control Structures Industrial & Engineering Chemistry Research. 58: 13555-13567. DOI: 10.1021/Acs.Iecr.9B00308 |
0.446 |
|
| 2019 |
Krishnamoorthy D, Jahanshahi E, Skogestad S. Feedback Real-Time Optimization Strategy Using a Novel Steady-state Gradient Estimate and Transient Measurements Industrial & Engineering Chemistry Research. 58: 207-216. DOI: 10.1021/Acs.Iecr.8B03137 |
0.462 |
|
| 2019 |
Krishnamoorthy D, Foss BA, Skogestad S. A Primal decomposition algorithm for distributed multistage scenario model predictive control Journal of Process Control. 81: 162-171. DOI: 10.1016/J.Jprocont.2019.02.003 |
0.364 |
|
| 2019 |
Straus J, Krishnamoorthy D, Skogestad S. On combining self-optimizing control and extremum-seeking control – Applied to an ammonia reactor case study Journal of Process Control. 78: 78-87. DOI: 10.1016/J.Jprocont.2019.01.012 |
0.467 |
|
| 2019 |
Reyes-Lúa A, Zotică C, Forsman K, Skogestad S. Systematic Design of Split Range Controllers Ifac-Papersonline. 52: 898-903. DOI: 10.1016/J.Ifacol.2019.06.176 |
0.484 |
|
| 2019 |
Krishnamoorthy D, Ryu J, Skogestad S. A Dynamic Extremum Seeking Scheme Applied to Gas Lift Optimization Ifac-Papersonline. 52: 802-807. DOI: 10.1016/J.Ifacol.2019.06.160 |
0.355 |
|
| 2019 |
Krishnamoorthy D, Fjalestad K, Skogestad S. Optimal operation of oil and gas production using simple feedback control structures Control Engineering Practice. 91: 104107. DOI: 10.1016/J.Conengprac.2019.104107 |
0.431 |
|
| 2019 |
Straus J, Skogestad S. A new termination criterion for sampling for surrogate model generation using partial least squares regression Computers & Chemical Engineering. 121: 75-85. DOI: 10.1016/J.Compchemeng.2018.10.008 |
0.331 |
|
| 2019 |
Torgashov A, Skogestad S. The use of first principles model for evaluation of adaptive soft sensor for multicomponent distillation unit Chemical Engineering Research & Design. 151: 70-78. DOI: 10.1016/J.Cherd.2019.08.017 |
0.317 |
|
| 2019 |
Halvorsen IJ, Dejanović I, Olujić Ž, Skogestad S. Thermal coupling opportunities for floating natural gas liquefaction plants Chemical Engineering Research & Design. 147: 346-353. DOI: 10.1016/J.Cherd.2019.05.013 |
0.305 |
|
| 2018 |
Torgashov A, Skogestad S, An D. A Rigorous Model for Evaluating Moving Window Soft Sensors for Industrial Distillation Processes Chemical Engineering Transactions. 69: 487-492. DOI: 10.3303/Cet1869082 |
0.336 |
|
| 2018 |
Sun B, Skogestad S, Lu J, Zhang W. Dual SIMC-PI Controller Design for Cascade Implement of Input Resetting Control with Application Industrial & Engineering Chemistry Research. 57: 6947-6955. DOI: 10.1021/Acs.Iecr.7B05047 |
0.491 |
|
| 2018 |
Backi CJ, Grimes BA, Skogestad S. A Control- and Estimation-Oriented Gravity Separator Model for Oil and Gas Applications Based upon First-Principles Industrial & Engineering Chemistry Research. 57: 7201-7217. DOI: 10.1021/Acs.Iecr.7B04297 |
0.333 |
|
| 2018 |
Grimholt C, Skogestad S. Optimization of fixed-order controllers using exact gradients Journal of Process Control. 71: 130-138. DOI: 10.1016/J.Jprocont.2018.09.001 |
0.488 |
|
| 2018 |
Grimholt C, Skogestad S. Optimal PI and PID control of first-order plus delay processes and evaluation of the original and improved SIMC rules Journal of Process Control. 70: 36-46. DOI: 10.1016/J.Jprocont.2018.06.011 |
0.455 |
|
| 2018 |
Krishnamoorthy D, Thombre M, Skogestad S, Jäschke J. Data-driven Scenario Selection for Multistage Robust Model Predictive Control Ifac-Papersonline. 51: 462-468. DOI: 10.1016/J.Ifacol.2018.11.046 |
0.383 |
|
| 2018 |
Straus J, Skogestad S. Self-Optimizing Control in Chemical Recycle Processes Ifac-Papersonline. 51: 536-541. DOI: 10.1016/J.Ifacol.2018.09.369 |
0.479 |
|
| 2018 |
Reyes-Lúa A, Zotică C, Skogestad S. Optimal Operation with Changing Active Constraint Regions using Classical Advanced Control Ifac-Papersonline. 51: 440-445. DOI: 10.1016/J.Ifacol.2018.09.340 |
0.519 |
|
| 2018 |
Krishnamoorthy D, Foss BA, Skogestad S. A Distributed Algorithm for Scenario-based Model Predictive Control using Primal Decomposition Ifac-Papersonline. 51: 351-356. DOI: 10.1016/J.Ifacol.2018.09.325 |
0.42 |
|
| 2018 |
Backi CJ, Gravdahl JT, Skogestad S. Simple method for parameter identification of a nonlinear Greitzer compressor model Ifac-Papersonline. 51: 198-203. DOI: 10.1016/J.Ifacol.2018.07.277 |
0.311 |
|
| 2018 |
Backi CJ, Krishnamoorthy D, Skogestad S. Slug handling with a virtual harp based on nonlinear predictive control for a gravity separator Ifac-Papersonline. 51: 120-125. DOI: 10.1016/J.Ifacol.2018.06.365 |
0.387 |
|
| 2018 |
Krishnamoorthy D, Jahanshahi E, Skogestad S. Gas-lift Optimization by Controlling Marginal Gas-Oil Ratio using Transient Measurements Ifac-Papersonline. 51: 19-24. DOI: 10.1016/J.Ifacol.2018.06.349 |
0.439 |
|
| 2018 |
Reyes-Lúa A, Backi CJ, Skogestad S. Improved PI control for a surge tank satisfying level constraints Ifac-Papersonline. 51: 835-840. DOI: 10.1016/J.Ifacol.2018.06.125 |
0.439 |
|
| 2018 |
Straus J, Skogestad S. Surrogate model generation using self-optimizing variables Computers & Chemical Engineering. 119: 143-151. DOI: 10.1016/J.Compchemeng.2018.08.031 |
0.34 |
|
| 2018 |
Ye L, Skogestad S. Dynamic self-optimizing control for unconstrained batch processes Computers & Chemical Engineering. 117: 451-468. DOI: 10.1016/J.Compchemeng.2018.06.024 |
0.445 |
|
| 2018 |
Daoutidis P, Lee JH, Harjunkoski I, Skogestad S, Baldea M, Georgakis C. Integrating operations and control: A perspective and roadmap for future research Computers & Chemical Engineering. 115: 179-184. DOI: 10.1016/J.Compchemeng.2018.04.011 |
0.515 |
|
| 2018 |
Krishnamoorthy D, Foss B, Skogestad S. Steady-state real-time optimization using transient measurements Computers & Chemical Engineering. 115: 34-45. DOI: 10.1016/J.Compchemeng.2018.03.021 |
0.382 |
|
| 2017 |
Pedersen S, Jahanshahi E, Yang Z, Skogestad S. Comparison of Model-Based Control Solutions for Severe Riser-Induced Slugs Energies. 10: 2014. DOI: 10.3390/En10122014 |
0.457 |
|
| 2017 |
Srinophakun TR, Prajimtis N, Upienpong T, Skogestad S. Passive Controller Design of Mass Exchanger Network King Mongkut’S University of Technology North Bangkok International Journal of Applied Science and Technology. 10. DOI: 10.14416/J.Ijast.2017.01.001 |
0.439 |
|
| 2017 |
Soltesz K, Grimholt C, Skogestad S. Simultaneous design of proportional–integral–derivative controller and measurement filter by optimisation Iet Control Theory and Applications. 11: 341-348. DOI: 10.1049/Iet-Cta.2016.0297 |
0.42 |
|
| 2017 |
Jahanshahi E, Skogestad S. Nonlinear control solutions to prevent slugging flow in offshore oil production Journal of Process Control. 54: 138-151. DOI: 10.1016/J.Jprocont.2017.03.014 |
0.492 |
|
| 2017 |
Ye L, Cao Y, Skogestad S. Global Self-Optimizing Control for Uncertain Constrained Process Systems Ifac-Papersonline. 50: 4672-4677. DOI: 10.1016/J.Ifacol.2017.08.691 |
0.441 |
|
| 2017 |
Jahanshahi E, Backi CJ, Skogestad S. Anti-slug control based on a virtual flow measurement Flow Measurement and Instrumentation. 53: 299-307. DOI: 10.1016/J.Flowmeasinst.2017.01.008 |
0.421 |
|
| 2017 |
Jienkulsawad P, Skogestad S, Arpornwichanop A. Control structure design of a solid oxide fuel cell and a molten carbonate fuel cell integrated system: Top-down analysis Energy Conversion and Management. 152: 88-98. DOI: 10.1016/J.Enconman.2017.09.033 |
0.394 |
|
| 2017 |
Šulc J, Skogestad S. A systematic approach for airflow velocity control design in road tunnels Control Engineering Practice. 69: 61-72. DOI: 10.1016/J.Conengprac.2017.09.005 |
0.452 |
|
| 2017 |
Bisgaard T, Skogestad S, Abildskov J, Huusom JK. Optimal operation and stabilising control of the concentric heat-integrated distillation column (HIDiC) Computers & Chemical Engineering. 96: 196-211. DOI: 10.1016/J.Compchemeng.2016.09.020 |
0.506 |
|
| 2017 |
Jia S, Qian X, Yuan X, Skogestad S. Control structure comparison for three-product Petlyuk column Chinese Journal of Chemical Engineering. 26: 1621-1630. DOI: 10.1016/J.Cjche.2017.10.018 |
0.463 |
|
| 2017 |
Straus J, Skogestad S. Use of Latent Variables to Reduce the Dimension of Surrogate Models Computer-Aided Chemical Engineering. 40: 445-450. DOI: 10.1016/B978-0-444-63965-3.50076-3 |
0.33 |
|
| 2016 |
Regalado-Méndez A, Skogestad S, Natividad R, Romero R. Biodiesel production by reactive flash: A numerical simulation International Journal of Chemical Engineering. 2016: 7843081. DOI: 10.1155/2016/7843081 |
0.301 |
|
| 2016 |
Qian X, Jia S, Skogestad S, Yuan X, Luo Y. Model Predictive Control of Reactive Dividing Wall Column for the Selective Hydrogenation and Separation of a C3 Stream in an Ethylene Plant Industrial and Engineering Chemistry Research. 55: 9738-9748. DOI: 10.1021/Acs.Iecr.6B02112 |
0.49 |
|
| 2016 |
Roux JDl, Skogestad S, Craig IK. Plant-wide control of grinding mill circuits: Top-down analysis Ifac-Papersonline. 49: 72-77. DOI: 10.1016/J.Ifacol.2016.10.099 |
0.404 |
|
| 2016 |
Oliveira Vd, Jäschke J, Skogestad S. Null-space method for optimal operation of transient processes Ifac-Papersonline. 49: 418-423. DOI: 10.1016/J.Ifacol.2016.07.378 |
0.449 |
|
| 2016 |
Torgashov A, Skogestad S, Kozlov A. Comparative Study of Multicomponent Distillation Static Estimators Based on Industrial and Rigorous Model Datasets Ifac-Papersonline. 49: 1187-1192. DOI: 10.1016/J.Ifacol.2016.07.369 |
0.334 |
|
| 2016 |
Bisgaard T, Skogestad S, Huusom JK, Abildskov J. Optimal Operation and Stabilising Control of the Concentric Heat-Integrated Distillation Column Ifac-Papersonline. 49: 747-752. DOI: 10.1016/J.Ifacol.2016.07.275 |
0.491 |
|
| 2016 |
Qian X, Jia S, Skogestad S, Yuan X. Comparison of stabilizing control structures for dividing wall columns Ifac-Papersonline. 49: 729-734. DOI: 10.1016/J.Ifacol.2016.07.271 |
0.447 |
|
| 2016 |
Grimholt C, Skogestad S. Optimal PID control of double integrating processes Ifac-Papersonline. 49: 127-132. DOI: 10.1016/J.Ifacol.2016.07.228 |
0.471 |
|
| 2016 |
Oliveira Vd, Jäschke J, Skogestad S. Optimal operation of energy storage in buildings: Use of the hot water system Journal of Energy Storage. 5: 102-112. DOI: 10.1016/J.Est.2015.11.009 |
0.323 |
|
| 2016 |
Qian X, Jia S, Skogestad S, Yuan X. Control structure selection for four-product Kaibel column Computers and Chemical Engineering. 93: 372-381. DOI: 10.1016/J.Compchemeng.2016.07.019 |
0.469 |
|
| 2016 |
Reyes-Lúa A, Solvik M, Skogestad S. Inclusion of thermodynamic equations for efficient steadystate process optimization Computer-Aided Chemical Engineering. 38: 613-618. DOI: 10.1016/B978-0-444-63428-3.50107-7 |
0.335 |
|
| 2016 |
Qian X, Jia S, Skogestad S, Yuan X. Design and control of azeotropic dividing wall column for separating furfural-water mixture Computer-Aided Chemical Engineering. 38: 409-414. DOI: 10.1016/B978-0-444-63428-3.50073-4 |
0.439 |
|
| 2016 |
Straus J, Skogestad S. Minimizing the complexity of surrogate models for optimization Computer-Aided Chemical Engineering. 38: 289-294. DOI: 10.1016/B978-0-444-63428-3.50053-9 |
0.388 |
|
| 2015 |
Bar NS, Skogestad S, Marçal JM, Ulanovsky N, Yovel Y. A sensory-motor control model of animal flight explains why bats fly differently in light versus dark. Plos Biology. 13: e1002046. PMID 25629809 DOI: 10.1371/Journal.Pbio.1002046 |
0.316 |
|
| 2015 |
Jahanshahi E, Skogestad S. Anti-slug control solutions based on identified model Journal of Process Control. 30: 58-68. DOI: 10.1016/J.Jprocont.2014.12.007 |
0.499 |
|
| 2015 |
Oliveira Vd, Jaschke J, Skogestad S. Neighbouring-Extremal Control for Steady-State Optimization Using Noisy Measurements Ifac-Papersonline. 48: 698-703. DOI: 10.1016/J.Ifacol.2015.09.050 |
0.506 |
|
| 2015 |
Oliveira Vd, Jäschke J, Skogestad S. An autonomous approach for driving systems towards their limit: an intelligent adaptive anti-slug control system for production maximization Ifac-Papersonline. 48: 104-111. DOI: 10.1016/J.Ifacol.2015.08.017 |
0.472 |
|
| 2015 |
Grimholt C, Skogestad S. Optimization of Oil Field Production Under Gas Coning Conditions Using the Optimal Closed-Loop Estimator Ifac-Papersonline. 48: 39-44. DOI: 10.1016/J.Ifacol.2015.08.007 |
0.325 |
|
| 2015 |
Francisco M, Skogestad S, Vega P. Model predictive control for the self-optimized operation in wastewater treatment plants: Analysis of dynamic issues Computers & Chemical Engineering. 82: 259-272. DOI: 10.1016/J.Compchemeng.2015.07.003 |
0.513 |
|
| 2015 |
Chatrattanawet N, Skogestad S, Arpornwichanop A. Control structure design and dynamic modeling for a solid oxide fuel cell with direct internal reforming of methane Chemical Engineering Research & Design. 98: 202-211. DOI: 10.1016/J.Cherd.2015.04.029 |
0.518 |
|
| 2015 |
Minasidis V, Skogestad S, Kaistha N. Simple Rules for Economic Plantwide Control Computer-Aided Chemical Engineering. 37: 101-108. DOI: 10.1016/B978-0-444-63578-5.50013-X |
0.499 |
|
| 2015 |
Grimholt C, Skogestad S. Improved Optimization-based Design of PID Controllers Using Exact Gradients Computer-Aided Chemical Engineering. 37: 1751-1756. DOI: 10.1016/B978-0-444-63577-8.50137-6 |
0.418 |
|
| 2015 |
Francisco M, Skogestad S, Vega P. Model Predictive Control for the Self-optimized Operation in Wastewater Treatment Plants Computer-Aided Chemical Engineering. 37: 1703-1708. DOI: 10.1016/B978-0-444-63577-8.50129-7 |
0.471 |
|
| 2014 |
Jahanshahi E, Oliveira VD, Grimholt C, Skogestad S. A comparison between Internal Model Control, optimal PIDF and robust controllers for unstable flow in risers Ifac Proceedings Volumes. 47: 5752-5759. DOI: 10.3182/20140824-6-Za-1003.02381 |
0.525 |
|
| 2014 |
Jahanshahi E, Skogestad S. Simplified Dynamic Models for Control of Riser Slugging in Offshore Oil Production Oil and Gas Facilities. 3: 80-88. DOI: 10.2118/172998-Pa |
0.377 |
|
| 2014 |
Nabil M, Narasimhan S, Skogestad S. Profitable and dynamically feasible operating point selection for constrained processes Journal of Process Control. 24: 531-541. DOI: 10.1016/J.Jprocont.2014.02.010 |
0.404 |
|
| 2014 |
Kim KKK, Skogestad S, Morari M, Braatz RD. Necessary and sufficient conditions for robust reliable control in the presence of model uncertainties and system component failures Computers and Chemical Engineering. 70: 67-77. DOI: 10.1016/J.Compchemeng.2014.07.023 |
0.681 |
|
| 2014 |
Jäschke J, Skogestad S. Optimal operation of heat exchanger networks with stream split: Only temperature measurements are required Computers & Chemical Engineering. 70: 35-49. DOI: 10.1016/J.Compchemeng.2014.03.020 |
0.344 |
|
| 2014 |
Dejanović I, Halvorsen IJ, Skogestad S, Jansen H, Olujić Ž. Hydraulic design, technical challenges and comparison of alternative configurations of a four-product dividing wall column Chemical Engineering and Processing. 84: 71-81. DOI: 10.1016/J.Cep.2014.03.009 |
0.327 |
|
| 2014 |
Khanam A, Shamsuzzoha M, Skogestad S. Optimal Operation and Control of Divided Wall Column Computer-Aided Chemical Engineering. 33: 673-678. DOI: 10.1016/B978-0-444-63456-6.50113-7 |
0.403 |
|
| 2014 |
Jäschke J, Skogestad S. A Self-Optimizing Strategy for Optimal Operation of a Preheating Train for a Crude Oil Unit Computer-Aided Chemical Engineering. 33: 607-612. DOI: 10.1016/B978-0-444-63456-6.50102-2 |
0.364 |
|
| 2014 |
Dutra JCS, Feital TdS, Skogestad S, Lima EL, Pinto JC. Control of Bulk Propylene Polymerizations Operated with Multiple Catalysts through Controller Reconfiguration Macromolecular Reaction Engineering. 8: 201-216. DOI: 10.1002/Mren.201300139 |
0.392 |
|
| 2013 |
Minasidis V, Jäschke J, Skogestad S. Economic plantwide control: Automated controlled variable selection for a reactor-separator-recycle process Ifac Proceedings Volumes. 46: 87-92. DOI: 10.3182/20131218-3-In-2045.00182 |
0.511 |
|
| 2013 |
Grimholt C, Skogestad S. Optimal PID-Control on First Order Plus Time Delay Systems & Verification of the SIMC Rules Ifac Proceedings Volumes. 46: 265-270. DOI: 10.3182/20131218-3-In-2045.00122 |
0.434 |
|
| 2013 |
Jäschke J, Skogestad S. Using Process Data for Finding Self-optimizing Controlled Variables ⋆ Ifac Proceedings Volumes. 46: 451-456. DOI: 10.3182/20131218-3-In-2045.00108 |
0.456 |
|
| 2013 |
Oliveira Vd, Jäschke J, Skogestad S. Dynamic online optimization of a house heating system in a fluctuating energy price scenario Ifac Proceedings Volumes. 46: 463-468. DOI: 10.3182/20131218-3-In-2045.00070 |
0.407 |
|
| 2013 |
Jahanshahi E, Skogestad S. Closed-Loop Model Identification and PID/PI Tuning for Robust Anti-Slug Control Ifac Proceedings Volumes. 46: 233-240. DOI: 10.3182/20131218-3-In-2045.00009 |
0.496 |
|
| 2013 |
Jahanshahi E, Skogestad S, Grøtli EI. Nonlinear model-based control of two-phase flow in risers by feedback linearization Ifac Proceedings Volumes. 46: 301-306. DOI: 10.3182/20130904-3-Fr-2041.00041 |
0.45 |
|
| 2013 |
De Araujo ACB, Gallani S, Mulas M, Skogestad S. Sensitivity analysis of optimal operation of an activated sludge process model for economic controlled variable selection Industrial and Engineering Chemistry Research. 52: 9908-9921. DOI: 10.1021/Ie4006673 |
0.473 |
|
| 2013 |
Ghadrdan M, Grimholt C, Skogestad S. A New Class of Model-Based Static Estimators Industrial & Engineering Chemistry Research. 52: 12451-12462. DOI: 10.1021/Ie400542N |
0.313 |
|
| 2013 |
Gera V, Panahi M, Skogestad S, Kaistha N. Economic plantwide control of the cumene process Industrial and Engineering Chemistry Research. 52: 830-846. DOI: 10.1021/Ie301386H |
0.526 |
|
| 2013 |
Yelchuru R, Skogestad S. Quantitative methods for Regulatory control layer selection Journal of Process Control. 23: 58-69. DOI: 10.1016/J.Jprocont.2012.10.006 |
0.444 |
|
| 2013 |
Jacobsen MG, Skogestad S. Active constraint regions for a natural gas liquefaction process Journal of Natural Gas Science and Engineering. 10: 8-13. DOI: 10.1016/J.Jngse.2012.10.002 |
0.428 |
|
| 2013 |
Halvorsen IJ, Dejanović I, Skogestad S, Olujić Ž. Internal configurations for a multi-product dividing wall column Chemical Engineering Research & Design. 91: 1954-1965. DOI: 10.1016/J.Cherd.2013.07.005 |
0.32 |
|
| 2013 |
Ghadrdan M, Halvorsen IJ, Skogestad S. Manipulation of vapour split in Kaibel distillation arrangements Chemical Engineering and Processing. 72: 10-23. DOI: 10.1016/J.Cep.2013.06.014 |
0.345 |
|
| 2013 |
Dwivedi D, Halvorsen IJ, Skogestad S. Control structure selection for three-product Petlyuk (dividing-wall) column Chemical Engineering and Processing: Process Intensification. 64: 57-67. DOI: 10.1016/J.Cep.2012.11.006 |
0.405 |
|
| 2013 |
Dwivedi D, Halvorsen IJ, Skogestad S. Control structure selection for four-product Petlyuk column Chemical Engineering and Processing: Process Intensification. 67: 49-59. DOI: 10.1016/J.Cep.2012.07.013 |
0.457 |
|
| 2013 |
Khanam A, Shamsuzzoha M, Skogestad S. Operation of energy efficient divided wall column Computer-Aided Chemical Engineering. 32: 235-240. DOI: 10.1016/B978-0-444-63234-0.50040-3 |
0.367 |
|
| 2013 |
Jagtap R, Kaistha N, Skogestad S. Economic Plantwide Control Over a Wide Throughput Range: A Systematic Design Procedure Aiche Journal. 59: 2407-2426. DOI: 10.1002/Aic.14028 |
0.503 |
|
| 2012 |
Yelchuru R, Skogestad S. Quantitative methods for optimal regulatory layer selection Ifac Proceedings Volumes. 45: 798-803. DOI: 10.3182/20120710-4-Sg-2026.00148 |
0.432 |
|
| 2012 |
Nabil M, Narasimhan S, Skogestad S. Economic back-off selection based on optimal multivariable controller Ifac Proceedings Volumes. 45: 792-797. DOI: 10.3182/20120710-4-Sg-2026.00140 |
0.428 |
|
| 2012 |
Ghadrdan M, Skogestad S, Halvorsen IJ. Economically Optimal Control of Kaibel Distillation Column: Fixed boilup rate Ifac Proceedings Volumes. 45: 744-749. DOI: 10.3182/20120710-4-Sg-2026.00126 |
0.519 |
|
| 2012 |
Jahanshahi E, Skogestad S, Hansen H. Control structure design for stabilizing unstable gas-lift oil wells Ifac Proceedings Volumes. 45: 93-100. DOI: 10.3182/20120710-4-Sg-2026.00110 |
0.473 |
|
| 2012 |
Jäschke J, Skogestad S. Economically Optimal Controlled Variables for Parallel Units – Application to Chemical Reactors1 Ifac Proceedings Volumes. 45: 768-773. DOI: 10.3182/20120710-4-Sg-2026.00096 |
0.433 |
|
| 2012 |
Jahanshahi E, Skogestad S, Helgesen AH. Controllability analysis of severe slugging in well-pipeline-riser systems Ifac Proceedings Volumes (Ifac-Papersonline). 1: 101-108. DOI: 10.3182/20120531-2-No-4020.00014 |
0.526 |
|
| 2012 |
Alcántara S, Vilanova R, Pedret C, Skogestad S. A look into robustness/performance and servo/regulation issues in PI tuning Ifac Proceedings Volumes. 45: 181-186. DOI: 10.3182/20120328-3-It-3014.00031 |
0.404 |
|
| 2012 |
Grimholt C, Skogestad S. Optimal PI-Control and Verification of the SIMC Tuning Rule Ifac Proceedings Volumes. 45: 11-22. DOI: 10.3182/20120328-3-It-3014.00003 |
0.417 |
|
| 2012 |
Dwivedi D, Strandberg JP, Halvorsen IJ, Skogestad S. Steady state and dynamic operation of four-product dividing-wall (Kaibel) columns: Experimental verification Industrial and Engineering Chemistry Research. 51: 15696-15706. DOI: 10.1021/Ie301432Z |
0.429 |
|
| 2012 |
Panahi M, Skogestad S. Selection of controlled variables for a natural gas to liquids process Industrial and Engineering Chemistry Research. 51: 10179-10190. DOI: 10.1021/Ie202678H |
0.368 |
|
| 2012 |
Panahi M, Rafiee A, Skogestad S, Hillestad M. A natural gas to liquids process model for optimal operation Industrial and Engineering Chemistry Research. 51: 425-433. DOI: 10.1021/Ie2014058 |
0.329 |
|
| 2012 |
Jacobsen MG, Skogestad S. Active Constraint Regions for Optimal Operation of Distillation Columns Industrial & Engineering Chemistry Research. 51: 2963-2973. DOI: 10.1021/Ie201220M |
0.382 |
|
| 2012 |
Yelchuru R, Skogestad S. Convex formulations for optimal selection of controlled variables and measurements using Mixed Integer Quadratic Programming Journal of Process Control. 22: 995-1007. DOI: 10.1016/J.Jprocont.2012.04.013 |
0.448 |
|
| 2012 |
Manum H, Skogestad S. Self-optimizing control with active set changes Journal of Process Control. 22: 873-883. DOI: 10.1016/J.Jprocont.2012.02.015 |
0.438 |
|
| 2012 |
Jäschke J, Skogestad S. Optimal controlled variables for polynomial systems Journal of Process Control. 22: 167-179. DOI: 10.1016/J.Jprocont.2011.09.005 |
0.461 |
|
| 2012 |
Petlyuk F, Danilov R, Skouras S, Skogestad S. Identification and analysis of possible splits for azeotropic mixtures. 2. Method for simple columns Chemical Engineering Science. 69: 159-169. DOI: 10.1016/J.Ces.2011.10.017 |
0.321 |
|
| 2012 |
Panahi M, Skogestad S. Economically efficient operation of CO 2 capturing process. Part II. Design of control layer Chemical Engineering and Processing: Process Intensification. 52: 112-124. DOI: 10.1016/J.Cep.2011.11.004 |
0.503 |
|
| 2012 |
Dwivedi D, Halvorsen IJ, Skogestad S. Dynamic behaviour and control of extended Petlyuk distillation arrangements Computer Aided Chemical Engineering. 30: 777-781. DOI: 10.1016/B978-0-444-59520-1.50014-2 |
0.474 |
|
| 2012 |
Sayalero EG, Skogestad S, Prada Cd, Sola JM, González R. Self-optimizing control for hydrogen optimization in a diesel hydrodesulfurization plant Computer-Aided Chemical Engineering. 31: 1647-1651. DOI: 10.1016/B978-0-444-59506-5.50160-7 |
0.466 |
|
| 2011 |
Halvorsen IJ, Skogestad S, Dejanovic I, Matijasevic L, Olujic Z. Multi-Product Dividing Wall Columns: A Simple and Effective Assessment and Conceptual Design Procedure Chemical Engineering Transactions. 25: 611-616. DOI: 10.3303/Cet1125102 |
0.328 |
|
| 2011 |
Yelchuru R, Skogestad S. Optimal Controlled Variable Selection with Structural Constraints Using MIQP Formulations Ifac Proceedings Volumes. 44: 4977-4982. DOI: 10.3182/20110828-6-It-1002.03038 |
0.467 |
|
| 2011 |
Jäschke J, Skogestad S. Optimal Operation by Controlling the Gradient to Zero Ifac Proceedings Volumes. 44: 6073-6078. DOI: 10.3182/20110828-6-It-1002.02486 |
0.447 |
|
| 2011 |
Jahanshahi E, Skogestad S. Simplified Dynamical Models for Control of Severe Slugging in Multiphase Risers Ifac Proceedings Volumes. 44: 1634-1639. DOI: 10.3182/20110828-6-It-1002.00981 |
0.385 |
|
| 2011 |
Jacobsen MG, Skogestad S. Active Constraint Regions for Optimal Operation of Chemical Processes Industrial & Engineering Chemistry Research. 50: 11226-11236. DOI: 10.1021/Ie2012196 |
0.414 |
|
| 2011 |
Alcantara S, Pedret C, Vilanova R, Skogestad S. Generalized Internal Model Control for Balancing Input/Output Disturbance Response Industrial & Engineering Chemistry Research. 50: 11170-11180. DOI: 10.1021/Ie200717Z |
0.398 |
|
| 2011 |
Dones I, Skogestad S, Preisig HA. Application of Balanced Truncation to Nonlinear Systems Industrial & Engineering Chemistry Research. 50: 10093-10101. DOI: 10.1021/Ie200706D |
0.308 |
|
| 2011 |
Jagtap R, Kaistha N, Skogestad S. Plantwide Control for Economic Optimum Operation of a Recycle Process with Side Reaction Industrial & Engineering Chemistry Research. 50: 8571-8584. DOI: 10.1021/Ie1024358 |
0.485 |
|
| 2011 |
Jäschke J, Skogestad S. NCO tracking and self-optimizing control in the context of real-time optimization Journal of Process Control. 21: 1407-1416. DOI: 10.1016/J.Jprocont.2011.07.001 |
0.445 |
|
| 2011 |
Alcántara S, Zhang WD, Pedret C, Vilanova R, Skogestad S. IMC-like analytical H∞ design with S/SP mixed sensitivity consideration: Utility in PID tuning guidance Journal of Process Control. 21: 976-985. DOI: 10.1016/J.Jprocont.2011.04.007 |
0.42 |
|
| 2011 |
Ghadrdan M, Halvorsen IJ, Skogestad S. Optimal operation of Kaibel distillation columns Chemical Engineering Research & Design. 89: 1382-1391. DOI: 10.1016/J.Cherd.2011.02.007 |
0.35 |
|
| 2011 |
Panahi M, Skogestad S. Economically efficient operation of CO 2 capturing process part I: Self-optimizing procedure for selecting the best controlled variables Chemical Engineering and Processing: Process Intensification. 50: 247-253. DOI: 10.1016/J.Cep.2011.02.005 |
0.418 |
|
| 2011 |
Jacobsen MG, Skogestad S. Optimization of LNG plants – challenges and strategies Computer-Aided Chemical Engineering. 29: 1854-1858. DOI: 10.1016/B978-0-444-54298-4.50149-5 |
0.351 |
|
| 2011 |
Jäschke J, Skogestad S. Controlled Variables from Optimal Operation Data Computer-Aided Chemical Engineering. 29: 753-757. DOI: 10.1016/B978-0-444-53711-9.50151-6 |
0.424 |
|
| 2011 |
Gera V, Kaistha N, Panahi M, Skogestad S. Plantwide Control of a Cumene Manufacture Process Computer Aided Chemical Engineering. 29: 522-526. DOI: 10.1016/B978-0-444-53711-9.50105-X |
0.466 |
|
| 2011 |
Ghadrdan M, Halvorsen IJ, Skogestad S. A Shortcut Design for Kaibel Columns Based on Minimum Energy Diagrams Computer-Aided Chemical Engineering. 29: 356-360. DOI: 10.1016/B978-0-444-53711-9.50072-9 |
0.325 |
|
| 2010 |
Mulas M, Araùjo ACBd, Baratti R, Skogestad S. Optimized Control Structure for a Wastewater Treatment Benchmark Ifac Proceedings Volumes. 43: 661-666. DOI: 10.3182/20100705-3-Be-2011.00110 |
0.475 |
|
| 2010 |
Jäschke J, Skogestad S. Self-Optimizing Control and NCO Tracking in the Context of Real-Time Optimization Ifac Proceedings Volumes. 43: 607-612. DOI: 10.3182/20100705-3-Be-2011.00101 |
0.456 |
|
| 2010 |
Bakke M, Johansen TA, Skogestad S. Effect of Varying Controller Parameters in Closed-Loop Subspace Identification Ifac Proceedings Volumes. 43: 595-600. DOI: 10.3182/20100705-3-Be-2011.00099 |
0.433 |
|
| 2010 |
Kvernland MK, Halvorsen IJ, Skogestad S. Model Predictive Control of a Kaibel Distillation Column Ifac Proceedings Volumes. 43: 553-558. DOI: 10.3182/20100705-3-Be-2011.00092 |
0.499 |
|
| 2010 |
Shamsuzzoha M, Skogestad S, Halvorsen IJ. On-Line PI Controller tuning Using Closed-Loop Setpoint Response Ifac Proceedings Volumes. 43: 511-516. DOI: 10.3182/20100705-3-Be-2011.00085 |
0.451 |
|
| 2010 |
Yelchuru R, Skogestad S, Manum H. MIQP formulation for Controlled Variable Selection in Self Optimizing Control Ifac Proceedings Volumes. 43: 61-66. DOI: 10.3182/20100705-3-Be-2011.00011 |
0.472 |
|
| 2010 |
Shamsuzzoha M, Skogestad S, Halvorsen IJ. A simple approach for on-line PI controller tuning using closed-loop setpoint responses Computer-Aided Chemical Engineering. 28: 619-624. DOI: 10.1016/S1570-7946(10)28104-X |
0.404 |
|
| 2010 |
Jagtap R, Kaistha N, Skogestad S. Plantwide Control for Economic Operation of a Recycle Process Computer-Aided Chemical Engineering. 28: 499-504. DOI: 10.1016/S1570-7946(10)28084-7 |
0.447 |
|
| 2010 |
Shamsuzzoha M, Skogestad S. The setpoint overshoot method: A simple and fast closed-loop approach for PID tuning Journal of Process Control. 20: 1220-1234. DOI: 10.1016/J.Jprocont.2010.08.003 |
0.462 |
|
| 2010 |
Sivertsen H, Storkaas E, Skogestad S. Small-scale experiments on stabilizing riser slug flow Chemical Engineering Research & Design. 88: 213-228. DOI: 10.1016/J.Cherd.2009.08.007 |
0.349 |
|
| 2010 |
Linhart A, Skogestad S. Reduced distillation models via stage aggregation Chemical Engineering Science. 65: 3439-3456. DOI: 10.1016/J.Ces.2010.02.032 |
0.309 |
|
| 2009 |
Jäschke JEP, Skogestad S. Optimally Invariant Variable Combinations for Nonlinear Systems Ifac Proceedings Volumes. 42: 530-535. DOI: 10.3182/20090712-4-Tr-2008.00085 |
0.413 |
|
| 2009 |
Downs JJ, Skogestad S. An industrial and academic perspective on plantwide control Ifac Proceedings Volumes. 42: 117-128. DOI: 10.3182/20090712-4-Tr-2008.00017 |
0.46 |
|
| 2009 |
Sivertsen H, Alstad V, Skogestad S. Medium-Scale Experiments on Stabilizing Riser-Slug Flow Spe Projects Facilities & Construction. 4: 156-170. DOI: 10.2118/120040-Pa |
0.392 |
|
| 2009 |
Dobos L, Jäschke J, Abonyi J, Skogestad S. Dynamic Model And Control Of Heat Exchanger Networks For District Heating Hungarian Journal of Industrial Chemistry. 37. DOI: 10.1515/220 |
0.304 |
|
| 2009 |
Aske EMB, Skogestad S. Consistent Inventory Control Industrial & Engineering Chemistry Research. 48: 10892-10902. DOI: 10.1021/Ie801603J |
0.438 |
|
| 2009 |
Gruetzmann S, Fieg G, Skogestad S. Experimental and Theoretical Studies on the Start-Up Operation of a Multivessel Batch Distillation Column Industrial & Engineering Chemistry Research. 48: 5336-5343. DOI: 10.1021/Ie800962B |
0.403 |
|
| 2009 |
Jensen JB, Skogestad S. Steady-State Operational Degrees of Freedom with Application to Refrigeration Cycles Industrial & Engineering Chemistry Research. 48: 6652-6659. DOI: 10.1021/Ie800565Z |
0.377 |
|
| 2009 |
Aske EMB, Skogestad S. Dynamic Degrees of Freedom for Tighter Bottleneck Control Computer-Aided Chemical Engineering. 27: 1275-1280. DOI: 10.1016/S1570-7946(09)70603-0 |
0.443 |
|
| 2009 |
Zenith F, Skogestad S. Control of the mass and energy dynamics of polybenzimidazole-membrane fuel cells Journal of Process Control. 19: 415-432. DOI: 10.1016/J.Jprocont.2008.06.019 |
0.34 |
|
| 2009 |
Alstad V, Skogestad S, Hori ES. Optimal measurement combinations as controlled variables Journal of Process Control. 19: 138-148. DOI: 10.1016/J.Jprocont.2008.01.002 |
0.434 |
|
| 2009 |
Linhart A, Skogestad S. Computational performance of aggregated distillation models Computers & Chemical Engineering. 33: 296-308. DOI: 10.1016/J.Compchemeng.2008.09.014 |
0.376 |
|
| 2008 |
Manum H, Narasimhan S, Skogestad S. Explicit MPC with output feedback using self-optimizing control Ifac Proceedings Volumes. 41: 6956-6961. DOI: 10.3182/20080706-5-Kr-1001.01179 |
0.474 |
|
| 2008 |
Jensen JB, Skogestad S. Problems with Specifying ¢Tmin in the Design of Processes with Heat Exchangers Industrial & Engineering Chemistry Research. 47: 3071-3075. DOI: 10.1021/Ie071335T |
0.316 |
|
| 2008 |
Hori ES, Skogestad S. Selection of Controlled Variables: Maximum Gain Rule and Combination of Measurements Industrial & Engineering Chemistry Research. 47: 9465-9471. DOI: 10.1021/Ie0711978 |
0.467 |
|
| 2008 |
Lid T, Skogestad S. Data reconciliation and optimal operation of a catalytic naphtha reformer Journal of Process Control. 18: 320-331. DOI: 10.1016/J.Jprocont.2007.09.002 |
0.392 |
|
| 2008 |
Araújo A, Skogestad S. Control structure design for the ammonia synthesis process Computers & Chemical Engineering. 32: 2920-2932. DOI: 10.1016/J.Compchemeng.2008.03.001 |
0.428 |
|
| 2008 |
Aske EMB, Strand S, Skogestad S. Coordinator MPC for maximizing plant throughput Computers & Chemical Engineering. 32: 195-204. DOI: 10.1016/J.Compchemeng.2007.05.012 |
0.373 |
|
| 2008 |
Lid T, Skogestad S. Scaled steady state models for effective on-line applications Computers & Chemical Engineering. 32: 990-999. DOI: 10.1016/J.Compchemeng.2007.04.003 |
0.352 |
|
| 2008 |
Baldea M, Araujo A, Skogestad S, Daoutidis P. Dynamic considerations in the synthesis of self-optimizing control structures Aiche Journal. 54: 1830-1841. DOI: 10.1002/Aic.11470 |
0.517 |
|
| 2008 |
Lersbamrungsuk V, Srinophakun T, Narasimhan S, Skogestad S. Control structure design for optimal operation of heat exchanger networks Aiche Journal. 54: 150-162. DOI: 10.1002/Aic.11366 |
0.487 |
|
| 2007 |
Narasimhan S, Skogestad S. Implementation Of Optimal Operation Using Off-Line Computations Ifac Proceedings Volumes. 40: 119-124. DOI: 10.3182/20070606-3-Mx-2915.00138 |
0.329 |
|
| 2007 |
Mulas M, Baratti R, Skogestad S. Controlled Variables Selection For A Biological Wastewater Treatment Process Ifac Proceedings Volumes. 40: 141-146. DOI: 10.3182/20070606-3-Mx-2915.00071 |
0.464 |
|
| 2007 |
Hori ES, Skogestad S. Maximum Gain Rule For Selecting Controlled Variables Ifac Proceedings Volumes. 40: 129-134. DOI: 10.3182/20070606-3-Mx-2915.00069 |
0.498 |
|
| 2007 |
Aske EMB, Skogestad S, Strand S. Throughput Maximization By Improved Bottleneck Control Ifac Proceedings Volumes. 40: 63-68. DOI: 10.3182/20070606-3-Mx-2915.00009 |
0.505 |
|
| 2007 |
Kariwala V, Forbes JF, Skogestad S. µ-Interaction measure for unstable systems International Journal of Automation and Control. 1: 295-313. DOI: 10.1504/Ijaac.2007.015845 |
0.399 |
|
| 2007 |
Skogestad S. The Dos and Don’ts of Distillation Column Control Chemical Engineering Research & Design. 85: 13-23. DOI: 10.1205/Cherd06133 |
0.477 |
|
| 2007 |
Hori ES, Skogestad S. Selection of Control Structure and Temperature Location for Two-Product Distillation Columns Chemical Engineering Research & Design. 85: 293-306. DOI: 10.1205/Cherd06115 |
0.391 |
|
| 2007 |
Araujo ACBD, Hori ES, Skogestad S. Application of Plantwide Control to the HDA Process. IIRegulatory Control Industrial & Engineering Chemistry Research. 46: 5159-5174. DOI: 10.1021/Ie061393Z |
0.509 |
|
| 2007 |
Alstad V, Skogestad S. Null Space Method For Selecting Optimal Measurement Combinations As Controlled Variables Industrial & Engineering Chemistry Research. 46: 846-853. DOI: 10.1021/Ie060285+ |
0.472 |
|
| 2007 |
Kariwala V, Skogestad S. L1/Q Approach for efficient computation of disturbance rejection measures for feedback control Journal of Process Control. 17: 501-508. DOI: 10.1016/J.Jprocont.2007.01.003 |
0.438 |
|
| 2007 |
Zenith F, Skogestad S. Control of fuel cell power output Journal of Process Control. 17: 333-347. DOI: 10.1016/J.Jprocont.2006.10.004 |
0.381 |
|
| 2007 |
Araújo ACBd, Govatsmark M, Skogestad S. Application of plantwide control to the HDA process. I-steady-state optimization and self-optimizing control Control Engineering Practice. 15: 1222-1237. DOI: 10.1016/J.Conengprac.2006.10.014 |
0.541 |
|
| 2007 |
Storkaas E, Skogestad S. Controllability Analysis of Two-phase Pipeline-riser Systems at Riser Slugging Conditions Control Engineering Practice. 15: 567-581. DOI: 10.1016/J.Conengprac.2006.10.007 |
0.479 |
|
| 2007 |
Jensen JB, Skogestad S. Optimal operation of simple refrigeration cycles Part II: Selection of controlled variables Computers & Chemical Engineering. 31: 1590-1601. DOI: 10.1016/J.Compchemeng.2007.01.008 |
0.432 |
|
| 2007 |
Jensen JB, Skogestad S. Optimal operation of simple refrigeration cycles Part I: Degrees of freedom and optimality of sub-cooling Computers & Chemical Engineering. 31: 712-721. DOI: 10.1016/J.Compchemeng.2006.12.003 |
0.317 |
|
| 2006 |
Sivertsen H, Godhavn J, Faanes A, Skogestad S. Control Solutions For Subsea Processing And Multiphase Transport Ifac Proceedings Volumes. 39: 1069-1074. DOI: 10.3182/20060402-4-Br-2902.01069 |
0.384 |
|
| 2006 |
Araújo A, Govatsmark M, Skogestad S. Application Of Plantwide Control To Large Scale Systems. Part I - Self-Optimizing Control Of The Hda Process Ifac Proceedings Volumes. 39: 1049-1054. DOI: 10.3182/20060402-4-Br-2902.01049 |
0.511 |
|
| 2006 |
Strandberg J, Skogestad S. Stabilizing Control Of An Integrated 4-Product Kaibel Column Ifac Proceedings Volumes. 39: 623-628. DOI: 10.3182/20060402-4-Br-2902.00623 |
0.435 |
|
| 2006 |
Jensen JB, Skogestad S. Optimal Operation Of A Simple Lng Process Ifac Proceedings Volumes. 39: 241-246. DOI: 10.3182/20060402-4-Br-2902.00241 |
0.366 |
|
| 2006 |
Skogestad S. Tuning for Smooth PID Control with Acceptable Disturbance Rejection Industrial & Engineering Chemistry Research. 45: 7817-7822. DOI: 10.1021/Ie0602815 |
0.465 |
|
| 2006 |
and VK, Skogestad S, Forbes JF. Relative Gain Array for Norm-Bounded Uncertain Systems Industrial & Engineering Chemistry Research. 45: 1751-1757. DOI: 10.1021/Ie050790R |
0.315 |
|
| 2006 |
Jensen JB, Skogestad S. Optimal operation of a mixed fluid cascade LNG plant Computer-Aided Chemical Engineering. 21: 1569-1574. DOI: 10.1016/S1570-7946(06)80271-3 |
0.411 |
|
| 2006 |
Araújo A, Baldea M, Skogestad S, Daoutidis P. Time scale separation and the link between open-loop and closed-loop dynamics Computer Aided Chemical Engineering. 21: 1455-1460. DOI: 10.1016/S1570-7946(06)80252-X |
0.506 |
|
| 2006 |
Kariwala V, Skogestad S. Branch and bound methods for control structure design Computer-Aided Chemical Engineering. 21: 1371-1376. DOI: 10.1016/S1570-7946(06)80238-5 |
0.41 |
|
| 2006 |
Aske EMB, Strand S, Skogestad S. Coordinator MPC with focus on maximizing throughput Computer-Aided Chemical Engineering. 21: 1203-1208. DOI: 10.1016/S1570-7946(06)80210-5 |
0.354 |
|
| 2006 |
Zenith F, Seland F, Kongstein OE, Børresen B, Tunold R, Skogestad S. Control-oriented modelling and experimental study of the transient response of a high-temperature polymer fuel cell Journal of Power Sources. 162: 215-227. DOI: 10.1016/J.Jpowsour.2006.06.022 |
0.309 |
|
| 2005 |
Aske EMB, Strand S, Skogestad S. Implementation Of Mpc On A Deethanizer At Kårstø Gas Plant Ifac Proceedings Volumes. 38: 437-442. DOI: 10.3182/20050703-6-Cz-1902.01647 |
0.392 |
|
| 2005 |
Sivertsen H, Skogestad S. Cascade Control Experiments Of Riser Slug Flow Using Topside Measurements Ifac Proceedings Volumes. 38: 129-134. DOI: 10.3182/20050703-6-Cz-1902.01597 |
0.458 |
|
| 2005 |
Araújo A, Skogestad S. Controllability Of Processes With Large Gains Ifac Proceedings Volumes. 38: 67-72. DOI: 10.3182/20050703-6-Cz-1902.00581 |
0.416 |
|
| 2005 |
Storkaas E, Skogestad S. Controllability Analysis Of An Unstable, Non-Minimum Phase Process Ifac Proceedings Volumes. 38: 592-597. DOI: 10.3182/20050703-6-Cz-1902.00499 |
0.48 |
|
| 2005 |
Kariwala V, Skogestad S, Forbes JF, Meadows ES. Achievable input performance of linear systems under feedback control International Journal of Control. 78: 1327-1341. DOI: 10.1080/00207170500204815 |
0.475 |
|
| 2005 |
Govatsmark MS, Skogestad S. Selection of Controlled Variables and Robust Setpoints Industrial & Engineering Chemistry Research. 44: 2207-2217. DOI: 10.1021/Ie049750Y |
0.527 |
|
| 2005 |
Hori ES, Skogestad S, Alstad V. Perfect Steady-State Indirect Control Industrial & Engineering Chemistry Research. 44: 863-867. DOI: 10.1021/Ie049736L |
0.473 |
|
| 2005 |
Faanes A, Skogestad S. Offset-free tracking of model predictive control with model mismatch : Experimental results Industrial & Engineering Chemistry Research. 44: 3966-3972. DOI: 10.1021/Ie049422Y |
0.447 |
|
| 2005 |
Jensen JB, Skogestad S. Control and optimal operation of simple heat pump cycles Computer-Aided Chemical Engineering. 20: 1429-1434. DOI: 10.1016/S1570-7946(05)80080-X |
0.39 |
|
| 2005 |
Hori ES, Skogestad S, Kwong WH. Use of perfect indirect control to minimize the state deviations Computer-Aided Chemical Engineering. 20: 1219-1224. DOI: 10.1016/S1570-7946(05)80045-8 |
0.449 |
|
| 2005 |
Sivertsen H, Skogestad S. Anti-slug control experiments on a small-scale two-phase loop Computer-Aided Chemical Engineering. 20: 1021-1026. DOI: 10.1016/S1570-7946(05)80012-4 |
0.344 |
|
| 2005 |
Faanes A, Skogestad S. Controller design for serial processes Journal of Process Control. 15: 259-271. DOI: 10.1016/J.Jprocont.2004.07.001 |
0.472 |
|
| 2005 |
Skouras S, Kiva V, Skogestad S. Feasible separations and entrainer selection rules for heteroazeotropic batch distillation Chemical Engineering Science. 60: 2895-2909. DOI: 10.1016/J.Ces.2004.11.056 |
0.329 |
|
| 2005 |
Skouras S, Skogestad S, Kiva V. Analysis and control of heteroazeotropic batch distillation Aiche Journal. 51: 1144-1157. DOI: 10.1002/Aic.10376 |
0.402 |
|
| 2004 |
Skogestad S. Simple analytic rules for model reduction and PID controller tuning Modeling Identification and Control. 25: 85-120. DOI: 10.4173/Mic.2004.2.2 |
0.396 |
|
| 2004 |
Faanes A, Skogestad S. Feedforward Control under the Presence of Uncertainty European Journal of Control. 10: 30-46. DOI: 10.3166/Ejc.10.30-46 |
0.461 |
|
| 2004 |
Halvorsen IJ, Skogestad S. Shortcut Analysis of Optimal Operation of Petlyuk Distillation Industrial & Engineering Chemistry Research. 43: 3994-3999. DOI: 10.1021/Ie034177O |
0.335 |
|
| 2004 |
Alstad V, Halvorsen IJ, Skogestad S. Optimal operation of a Petlyuk Distillation Column: Energy Savings by Over-fractionation Computer-Aided Chemical Engineering. 18: 547-552. DOI: 10.1016/S1570-7946(04)80157-3 |
0.302 |
|
| 2004 |
Skogestad S. Chapter D1 – Integration of optimal operation control Computer-Aided Chemical Engineering. 17: 485-500. DOI: 10.1016/S1570-7946(04)80071-3 |
0.389 |
|
| 2004 |
Skogestad S. Lower Limit on Controller Gain for Acceptable Disturbance Rejection Ifac Proceedings Volumes. 37: 499-503. DOI: 10.1016/S1474-6670(17)38781-5 |
0.482 |
|
| 2004 |
Storkaas E, Skogestad S. Cascade Control of Unstable Systems with Application to Stabilization of Slug Flow Ifac Proceedings Volumes. 37: 335-340. DOI: 10.1016/S1474-6670(17)38754-2 |
0.43 |
|
| 2004 |
Alstad V, Skogestad S. Combinations of Measurements as Controlled Variables: Application to a Petlyuk Distillation Column Ifac Proceedings Volumes. 37: 233-238. DOI: 10.1016/S1474-6670(17)38737-2 |
0.424 |
|
| 2004 |
Skouras S, Skogestad S. Separation of ternary heteroazeotropic mixtures in a closed multivessel batch distillation-decanter hybrid Chemical Engineering and Processing. 43: 291-304. DOI: 10.1016/S0255-2701(03)00126-0 |
0.342 |
|
| 2004 |
Skogestad S. Corrections and comments from the author on the paper “Simple analytic rules for model reduction and PID controller tuning”, Journal of Process Control 13 (2003) 291–309 Journal of Process Control. 14: 465. DOI: 10.1016/J.Jprocont.2003.09.001 |
0.446 |
|
| 2004 |
Skogestad S. Near-optimal operation by self-optimizing control: from process control to marathon running and business systems Computers & Chemical Engineering. 29: 127-137. DOI: 10.1016/J.Compchemeng.2004.07.011 |
0.463 |
|
| 2004 |
Engelien HK, Skogestad S. Selecting appropriate control variables for a heat-integrated distillation system with prefractionator Computers & Chemical Engineering. 28: 683-691. DOI: 10.1016/J.Compchemeng.2004.02.023 |
0.439 |
|
| 2004 |
Skouras S, Skogestad S. Time (energy) requirements in closed batch distillation arrangements Computers & Chemical Engineering. 28: 829-837. DOI: 10.1016/J.Compchemeng.2004.02.021 |
0.342 |
|
| 2004 |
Skouras S, Skogestad S. Time requirements for heteroazeotropic distillation in batch columns Computers & Chemical Engineering. 28: 1689-1700. DOI: 10.1016/J.Compchemeng.2004.01.004 |
0.324 |
|
| 2004 |
Faanes A, Skogestad S. Ph-Neutralization: Integrated Process And Control Design Computers & Chemical Engineering. 28: 1475-1487. DOI: 10.1016/J.Compchemeng.2003.11.001 |
0.417 |
|
| 2004 |
Skogestad S. Control structure design for complete chemical plants Computers & Chemical Engineering. 28: 219-234. DOI: 10.1016/J.Compchemeng.2003.08.002 |
0.501 |
|
| 2003 |
Faanes A, Skogestad S. State Space Realization of Model Predictive Controllers Without Active Constraints Modeling Identification and Control. 24: 231-244. DOI: 10.4173/Mic.2003.4.4 |
0.438 |
|
| 2003 |
Engelien HK, Larsson T, Skogestad S. Implementation of Optimal Operation for Heat Integrated Distillation Columns Chemical Engineering Research & Design. 81: 277-281. DOI: 10.1205/026387603762878755 |
0.384 |
|
| 2003 |
Havre K, Skogestad S. Selection of variables for stabilizing control using pole vectors Ieee Transactions On Automatic Control. 48: 1393-1398. DOI: 10.1109/Tac.2003.816062 |
0.366 |
|
| 2003 |
Halvorsen IJ, Skogestad S, Morud JC, Alstad V. Optimal Selection of Controlled Variables Industrial & Engineering Chemistry Research. 42: 3273-3284. DOI: 10.1021/Ie020833T |
0.441 |
|
| 2003 |
Faanes A, Skogestad S. Buffer Tank Design for Acceptable Control Performance Industrial & Engineering Chemistry Research. 42: 2198-2208. DOI: 10.1021/Ie020525V |
0.45 |
|
| 2003 |
Larsson T, Govatsmark MS, Skogestad S, Yu CC. Control Structure Selection for Reactor, Separator, and Recycle Processes Industrial & Engineering Chemistry Research. 42: 1225-1234. DOI: 10.1021/Ie0200860 |
0.512 |
|
| 2003 |
Halvorsen IJ, Skogestad S. Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column Industrial & Engineering Chemistry Research. 42: 596-604. DOI: 10.1021/Ie010863G |
0.314 |
|
| 2003 |
Skogestad S. Self-optimizing control: From key performance indicators to control of biological systems Computer-Aided Chemical Engineering. 15: 340-345. DOI: 10.1016/S1570-7946(03)80567-9 |
0.485 |
|
| 2003 |
Skouras S, Skogestad S. Separation of azeotropic mixtures in closed batch distillation arrangements Computer-Aided Chemical Engineering. 14: 935-940. DOI: 10.1016/S1570-7946(03)80237-7 |
0.318 |
|
| 2003 |
Engelien HK, Skogestad S. Selecting appropriate control variables for a heat integrated distillation system with prefractionator Computer-Aided Chemical Engineering. 14: 407-412. DOI: 10.1016/S1570-7946(03)80149-9 |
0.436 |
|
| 2003 |
Alstad V, Skogestad S. Combination of measurements as controlled variables for self-optimizing control Computer-Aided Chemical Engineering. 14: 353-358. DOI: 10.1016/S1570-7946(03)80140-2 |
0.465 |
|
| 2003 |
Skogestad S. Simple analytic rules for model reduction and PID controller tuning Journal of Process Control. 13: 291-309. DOI: 10.1016/S0959-1524(02)00062-8 |
0.393 |
|
| 2003 |
Wu K, Yu C, Luyben WL, Skogestad S. Reactor/separator processes with recycles-2. Design for composition control Computers & Chemical Engineering. 27: 401-421. DOI: 10.1016/S0098-1354(02)00218-1 |
0.472 |
|
| 2002 |
Govatsmark MS, Skogestad S. Selection Of Controlled Variables And Robust Setpoints Ifac Proceedings Volumes. 35: 351-356. DOI: 10.3182/20020721-6-Es-1901.00627 |
0.458 |
|
| 2002 |
Skogestad S, Havre K, Larsson T. Control Limitations For Unstable Plants Ifac Proceedings Volumes. 35: 485-490. DOI: 10.3182/20020721-6-Es-1901.00330 |
0.414 |
|
| 2002 |
Govatsmark MS, Skogestad S. Optimal Number of Stages in Distillation with respect to Controllability Computer-Aided Chemical Engineering. 10: 499-504. DOI: 10.1016/S1570-7946(02)80111-0 |
0.365 |
|
| 2002 |
Skogestad S. Plantwide control: Towards a systematic procedure Computer-Aided Chemical Engineering. 10: 57-69. DOI: 10.1016/S1570-7946(02)80039-6 |
0.5 |
|
| 2001 |
Havre K, Skogestad S. Achievable performance of multivariable systems with unstable zeros and poles International Journal of Control. 74: 1131-1139. DOI: 10.1080/00207170110053346 |
0.371 |
|
| 2001 |
Larsson T, Hestetun K, Hovland E, Skogestad S. Self-optimizing control of a large-scale plant: The Tennessee Eastman process Industrial & Engineering Chemistry Research. 40: 4889-4901. DOI: 10.1021/Ie000586Y |
0.449 |
|
| 2001 |
Lid T, Skogestad S. Implementation issues for real-time optimization of a crude unit heat exchanger network Computer-Aided Chemical Engineering. 9: 1041-1046. DOI: 10.1016/S1570-7946(01)80167-X |
0.518 |
|
| 2001 |
Govatsmark MS, Skogestad S. Control structure selection for an evaporation process Computer-Aided Chemical Engineering. 9: 657-662. DOI: 10.1016/S1570-7946(01)80104-8 |
0.49 |
|
| 2000 |
Skogestad S. Self-Optimizing Control: A Distillation Case Study Ifac Proceedings Volumes. 33: 977-982. DOI: 10.1016/S1474-6670(17)38667-6 |
0.487 |
|
| 2000 |
Faanes A, Skogestad S. pH-Neutralization: Integrated Process and Control Design Ifac Proceedings Volumes. 33: 75-80. DOI: 10.1016/S1474-6670(17)38521-X |
0.432 |
|
| 2000 |
Skogestad S. Plantwide control: the search for the self-optimizing control structure Journal of Process Control. 10: 487-507. DOI: 10.1016/S0959-1524(00)00023-8 |
0.537 |
|
| 2000 |
Faanes A, Skogestad S. A systematic approach to the design of buffer tanks Computers & Chemical Engineering. 24: 1395-1401. DOI: 10.1016/S0098-1354(00)80007-1 |
0.424 |
|
| 2000 |
Skogestad S. Self-optimizing control: the missing link between steady-state optimization and control Computers & Chemical Engineering. 24: 569-575. DOI: 10.1016/S0098-1354(00)00405-1 |
0.468 |
|
| 2000 |
Wittgens B, Skogestad S. Closed operation of multivessel batch distillation: Experimental verification Aiche Journal. 46: 1209-1217. DOI: 10.1002/Aic.690460613 |
0.384 |
|
| 1999 |
Skogestad S, Halvorsen IJ, Larsson T, Govatsmark MS. Plantwide control: The search for the self-optimizing control structure Ifac Proceedings Volumes. 32: 6932-6937. DOI: 10.1016/S1474-6670(17)57183-9 |
0.535 |
|
| 1999 |
Halvorsen IJ, Skogestad S. Optimal operation of Petlyuk distillation: steady-state behavior Journal of Process Control. 9: 407-424. DOI: 10.1016/S0959-1524(99)00009-8 |
0.487 |
|
| 1999 |
Hilmen EK, Kiva VN, Skogestad S. Analysis of closed multivessel batch distillation of ternary azeotropic mixtures using elementary VLE cells Computers & Chemical Engineering. 23. DOI: 10.1016/S0098-1354(99)80085-4 |
0.362 |
|
| 1999 |
Glemmestad B, Skogestad S, Gundersen T. Optimal operation of heat exchanger networks Computers & Chemical Engineering. 23: 509-522. DOI: 10.1016/S0098-1354(98)00289-0 |
0.391 |
|
| 1998 |
Havre K, Skogestad S. Selection of Variables for Regulatory Control Using Pole Vectors Ifac Proceedings Volumes. 31: 583-588. DOI: 10.1016/S1474-6670(17)44989-5 |
0.437 |
|
| 1998 |
Wittgens B, Skogestad S. Multivessel Batch Distillation - Potential Energy Savings Ifac Proceedings Volumes. 31: 493-498. DOI: 10.1016/S1474-6670(17)44975-5 |
0.349 |
|
| 1998 |
Halvorsen IJ, Skogestad S. Use Of Feedback For Indirect Optimizing Control: Application To Petlyuk Distillation Ifac Proceedings Volumes. 31: 397-402. DOI: 10.1016/S1474-6670(17)44959-7 |
0.479 |
|
| 1998 |
Morud JC, Skogestad S. Analysis of instability in an industrial ammonia reactor Aiche Journal. 44: 888-895. DOI: 10.1002/Aic.690440414 |
0.305 |
|
| 1997 |
Skogestad S. Dynamics and control of distillation columns : a critical survey Modeling Identification and Control. 18: 177-217. DOI: 10.4173/Mic.1997.3.1 |
0.44 |
|
| 1997 |
Skogestad S. DYNAMICS AND CONTROL OF DISTILLATION COLUMNS A tutorial introduction Chemical Engineering Research & Design. 75: 539-562. DOI: 10.1205/026387697524092 |
0.436 |
|
| 1997 |
Zhao Y, Skogestad S. Comparison of various control configurations for continuous bioreactors Industrial & Engineering Chemistry Research. 36: 697-705. DOI: 10.1021/Ie960123L |
0.43 |
|
| 1997 |
Glemmestad B, Skogestad S, Gundersen T. On-line optimization and choice of optimization variables for control of heat exchanger networks Computers & Chemical Engineering. 21. DOI: 10.1016/S0098-1354(97)87531-X |
0.392 |
|
| 1997 |
Halvorsen IJ, Skogestad S. Optimizing control of Petlyuk distillation : Understanding the steady-state behavior Computers & Chemical Engineering. 21. DOI: 10.1016/S0098-1354(97)87510-2 |
0.491 |
|
| 1997 |
Christiansen AC, Skogestad S, Lien K. Complex distillation arrangements: Extending the petlyuk ideas Computers & Chemical Engineering. 21. DOI: 10.1016/S0098-1354(97)87508-4 |
0.311 |
|
| 1997 |
Hovd M, Braatz RD, Skogestad S. SVD controllers for H2−, H∞− and μ-optimal control Automatica. 33: 433-439. DOI: 10.1016/S0005-1098(96)00167-7 |
0.642 |
|
| 1997 |
Skogestad S, Wittgens B, Litto R, Sørensen E. Multivessel batch distillation Aiche Journal. 43: 971-978. DOI: 10.1002/Aic.690430412 |
0.393 |
|
| 1996 |
Skogestad S, Wolff EA. Controllability measures for disturbance rejection Modeling Identification and Control. 17: 167-181. DOI: 10.4173/Mic.1996.3.1 |
0.451 |
|
| 1996 |
Wolff EA, Skogestad S. Temperature Cascade Control of Distillation Columns Industrial & Engineering Chemistry Research. 35: 475-484. DOI: 10.1021/Ie940758P |
0.471 |
|
| 1996 |
Harve K, Skogestad S. Input/Output Selection and Partial Control Ifac Proceedings Volumes. 29: 5977-5982. DOI: 10.1016/S1474-6670(17)58638-3 |
0.485 |
|
| 1996 |
Morud J, Skogestad S. Dynamic behaviour of integrated plants Journal of Process Control. 6: 145-156. DOI: 10.1016/0959-1524(95)00045-3 |
0.373 |
|
| 1996 |
Skogestad S. A PROCEDURE FOR SISO CONTROLLABILITY ANALYSIS--WITH APPLICATION TO DESIGN OF pH NEUTRALIZATION PROCESSES Computers & Chemical Engineering. 20: 373-386. DOI: 10.1016/0098-1354(96)80910-0 |
0.447 |
|
| 1996 |
Sørensen E, Skogestad S. Optimal startup procedures for batch distillation Computers & Chemical Engineering. 20. DOI: 10.1016/0098-1354(96)00217-7 |
0.357 |
|
| 1996 |
Wittgens B, Litto R, Sørensen E, Skogestad S. Total reflux operation of multivessel batch distillation Computers & Chemical Engineering. 20. DOI: 10.1016/0098-1354(96)00181-0 |
0.391 |
|
| 1996 |
Skogestad S, Havre K. The use of RGA and condition number as robustness measures Computers & Chemical Engineering. 20. DOI: 10.1016/0098-1354(96)00175-5 |
0.398 |
|
| 1996 |
Sørense E, Skogestad S. Comparison of regular and inverted batch distillation Chemical Engineering Science. 51: 4949-4962. DOI: 10.1016/0009-2509(96)00287-4 |
0.324 |
|
| 1996 |
Braatz RD, Morari M, Skogestad S. Loopshaping For Robust Performance International Journal of Robust and Nonlinear Control. 6: 805-823. DOI: 10.1002/(Sici)1099-1239(199610)6:8<805::Aid-Rnc192>3.0.Co;2-X |
0.669 |
|
| 1995 |
Wolff EA, Skogestad S. Operation of Integrated Three-Product (Petlyuk) Distillation Columns Industrial & Engineering Chemistry Research. 34: 2094-2103. DOI: 10.1021/Ie00045A018 |
0.478 |
|
| 1995 |
Jacobsen EW, Skogestad S. Multiple Steady States and Instability in Distillation. Implications for Operation and Control Industrial & Engineering Chemistry Research. 34: 4395-4405. DOI: 10.1021/Ie00039A031 |
0.44 |
|
| 1995 |
Wittgens B, Skogestad S. Evaluation of Dynamic Models of Distillation Columns with Emphasis on the Initial Response Ifac Proceedings Volumes. 28: 261-267. DOI: 10.1016/S1474-6670(17)47047-9 |
0.301 |
|
| 1995 |
Zhao Y, Skogestad S. Modeling And Control Of A Continuous Bioreactor With Cross-Flow Filtration Ifac Proceedings Volumes. 28: 321-325. DOI: 10.1016/S1474-6670(17)45654-0 |
0.472 |
|
| 1995 |
Lundström P, Skogestad S. Opportunities and difficulties with 5 × 5 distillation control Journal of Process Control. 5: 249-261. DOI: 10.1016/0959-1524(95)00017-K |
0.515 |
|
| 1995 |
Lundstrom P, Lee J, Morari M, Skogestad S. Limitations of dynamic matrix control Computers & Chemical Engineering. 19: 409-421. DOI: 10.1016/0098-1354(94)00063-T |
0.581 |
|
| 1994 |
Hovd M, Skogestad S. Improved independent design of robust decentralized controllers Modeling Identification and Control. 15: 93-107. DOI: 10.4173/Mic.1994.2.3 |
0.428 |
|
| 1994 |
Wang Z, Lundström P, Skogestad S. Representation of uncertain time delays in the H∞ framework‡ International Journal of Control. 59: 627-638. DOI: 10.1080/00207179408923097 |
0.354 |
|
| 1994 |
Hovd M, Skogestad S. Pairing Criteria for Decentralized Control of Unstable Plants Industrial & Engineering Chemistry Research. 33: 2134-2139. DOI: 10.1021/Ie00033A016 |
0.406 |
|
| 1994 |
Jacobsen EW, Skogestad S. Inconsistencies in Dynamic Models for Ill-Conditioned Plants: Application to Low-Order Models of Distillation Columns Industrial & Engineering Chemistry Research. 33: 631-640. DOI: 10.1021/Ie00027A021 |
0.384 |
|
| 1994 |
Skogestad S. Controllability Analysis of SISO Systems Ifac Proceedings Volumes. 27: 469-474. DOI: 10.1016/S1474-6670(17)48194-8 |
0.45 |
|
| 1994 |
Lundström F, Skogestad S. Opportunities and Difficulties with 5 × 5 Distillation Control Ifac Proceedings Volumes. 27: 363-369. DOI: 10.1016/S1474-6670(17)48178-X |
0.519 |
|
| 1994 |
Zhao Y, Skogestad S. A Comparison Of Various Control Schemes For Continuous Bioreactor Ifac Proceedings Volumes. 27: 309-314. DOI: 10.1016/S1474-6670(17)48169-9 |
0.408 |
|
| 1994 |
Flatby P, Skogestad S, Lundström P. Rigorous Dynamic Simulation of Distillation Columns Based on UV-Flash Ifac Proceedings Volumes. 27: 261-266. DOI: 10.1016/S1474-6670(17)48161-4 |
0.326 |
|
| 1994 |
Skogestad S. A procedure for siso controllability analysis - with application to design of pH processes Ifac Proceedings Volumes. 27: 25-30. DOI: 10.1016/S1474-6670(17)47959-6 |
0.432 |
|
| 1994 |
Sørensen E, Skogestad S. Control strategies for reactive batch distillation Journal of Process Control. 4: 205-217. DOI: 10.1016/0959-1524(94)80042-1 |
0.456 |
|
| 1994 |
Sørensen E, Macchietto S, Stuart G, Skogestad S. Optimal control and on-line operation of reactive batch distillation Computers & Chemical Engineering. 20: 1491-1498. DOI: 10.1016/0098-1354(95)00234-0 |
0.507 |
|
| 1994 |
Morud J, Skogestad S. Effects of recycle on dynamics and control of chemical processing plants Computers & Chemical Engineering. 18. DOI: 10.1016/0098-1354(94)80086-3 |
0.333 |
|
| 1994 |
Mathisen KW, Morari M, Skogestad S. Dynamic models for heat exchangers and heat exchanger networks Computers & Chemical Engineering. 18. DOI: 10.1016/0098-1354(94)80075-8 |
0.496 |
|
| 1994 |
Hovd M, Skogestad S. Control of symmetrically interconnected plants Automatica. 30: 957-973. DOI: 10.1016/0005-1098(94)90190-2 |
0.452 |
|
| 1994 |
Hovd M, Skogestad S. Sequential design of decentralized controllers Automatica. 30: 1601-1607. DOI: 10.1016/0005-1098(94)90099-X |
0.463 |
|
| 1994 |
Jacobsen EW, Skogestad S. Instability of distillation columns Aiche Journal. 40: 1466-1478. DOI: 10.1002/Aic.690400906 |
0.36 |
|
| 1993 |
Wang Z, Skogestad S. Robust control of time-delay systems using the Smith predictor International Journal of Control. 57: 1405-1420. DOI: 10.1080/00207179308934454 |
0.357 |
|
| 1993 |
Hovd M, Braatz RD, Skogestad S. On the Structure of the Robust Optimal Controller for a Class of Problems Ifac Proceedings Volumes. 26: 133-136. DOI: 10.1016/S1474-6670(17)48911-7 |
0.47 |
|
| 1993 |
Hovd M, Skogestad S. Improved Independent Design of Robust Decentralized Controllers Ifac Proceedings Volumes. 26: 203-206. DOI: 10.1016/S1474-6670(17)48454-0 |
0.5 |
|
| 1993 |
Lundström P, Skogestad S, Wang Z-. Modelling of Gain and Delay Uncertainty in the Structured Singular Value Framework Ifac Proceedings Volumes. 26: 49-52. DOI: 10.1016/S1474-6670(17)48424-2 |
0.402 |
|
| 1993 |
Jacobsen EW, Skogestad S. Dynamics And Control Of Unstable Distillation Columns Modeling Identification and Control. 14: 59-72. DOI: 10.1016/B978-0-08-041711-0.50033-7 |
0.488 |
|
| 1993 |
Hovd M, Skogestad S. Improved independent design of robust decentralized controllers Journal of Process Control. 3: 43-51. DOI: 10.1016/0959-1524(93)80014-3 |
0.481 |
|
| 1993 |
Hovd M, Skogestad S. Procedure for regulatory control structure selection with application to the FCC process Aiche Journal. 39: 1938-1953. DOI: 10.1002/Aic.690391205 |
0.486 |
|
| 1992 |
Skogestad S, Morari M. Variable selection for decentralized control Modeling Identification and Control. 13: 113-125. DOI: 10.4173/Mic.1992.2.3 |
0.56 |
|
| 1992 |
Hovd M, Skogestad S. Controllability Analysis for Unstable Processes Ifac Proceedings Volumes. 25: 49-54. DOI: 10.1016/S1474-6670(17)54011-2 |
0.419 |
|
| 1992 |
Skogestad S, Wolff EA. Controllability Measures for Disturbance Rejection Ifac Proceedings Volumes. 25: 23-29. DOI: 10.1016/S1474-6670(17)54008-2 |
0.452 |
|
| 1992 |
Jacobsen EW, Skogestad S. Dynamics and Control of Unstable Distillation Columns Ifac Proceedings Volumes. 25: 201-206. DOI: 10.1016/S1474-6670(17)50992-1 |
0.488 |
|
| 1992 |
Skogestad S. Dynamics and Control of Distillation Columns - A Critical Survey Ifac Proceedings Volumes. 25: 11-35. DOI: 10.1016/S1474-6670(17)50966-0 |
0.441 |
|
| 1992 |
Mathisen KW, Skogestad S, Wolff EA. Bypass selection for control of heat exchanger networks Computers & Chemical Engineering. 16. DOI: 10.1016/S0098-1354(09)80031-8 |
0.448 |
|
| 1992 |
Hovd M, Skogestad S. Simple frequency-dependent tools for control system analysis, structure selection and design: thr Automatica. 28: 989-996. DOI: 10.1016/0005-1098(92)90152-6 |
0.477 |
|
| 1991 |
Skogestad S, Hovd M, Lundström P. Simple frequency-dependent tools for analysis of inherent control limitations Modeling Identification and Control. 12: 159-177. DOI: 10.4173/Mic.1991.4.1 |
0.346 |
|
| 1991 |
Lundström P, Skogestad S, Wang Z. Performance weight selection for H-infinity and μ-control methods Transactions of the Institute of Measurement and Control. 13: 241-252. DOI: 10.1177/014233129101300504 |
0.365 |
|
| 1991 |
Mejdell T, Skogestad S. Composition estimator in a pilot-plant distillation column using multiple temperatures Industrial & Engineering Chemistry Research. 30: 2555-2564. DOI: 10.1021/Ie00060A008 |
0.305 |
|
| 1991 |
Mejdell T, Skogestad S. Estimation of distillation compositions from multiple temperature measurements using partial-least-squares regression Industrial & Engineering Chemistry Research. 30: 2543-2543. DOI: 10.1021/Ie00060A007 |
0.306 |
|
| 1991 |
Skogestad S, Jacobsen EW, Morari M. Comments on "Tuning controllers on distillation columns with the distillate-bottoms structure" Industrial & Engineering Chemistry Research. 30: 2019-2020. DOI: 10.1021/Ie00056A056 |
0.541 |
|
| 1991 |
Skogestad S. Consistency of Steady-State Models Using Insight about Extensive Variables? Industrial & Engineering Chemistry Research. 30: 654-661. DOI: 10.1021/Ie00052A009 |
0.342 |
|
| 1991 |
Jacobsen EW, Laroche L, Morari M, Skogestad S, Andersen HW. Robust control of homogeneous azeotropic distillation columns Aiche Journal. 37: 1810-1824. DOI: 10.1002/Aic.690371206 |
0.603 |
|
| 1991 |
Jacobsen EW, Skogestad S. Multiple steady states in ideal two‐product distillation Aiche Journal. 37: 499-511. DOI: 10.1002/Aic.690370404 |
0.325 |
|
| 1990 |
Skogestad S, Jacobsen EW, Morari M. Inadequacy of steady-state analysis for feedback control: distillate-bottom control of distillation columns Industrial & Engineering Chemistry Research. 29: 2339-2346. DOI: 10.1021/Ie00108A006 |
0.587 |
|
| 1990 |
Skogestad S, Jacobsen EW, Lundström P. Modelling Requirements for Robust Control of Distillation Columns Ifac Proceedings Volumes. 23: 191-197. DOI: 10.1016/S1474-6670(17)51418-4 |
0.462 |
|
| 1990 |
Skogestad S, Lundström P. Mu-optimal LV-control of distillation columns Computers & Chemical Engineering. 14: 401-413. DOI: 10.1016/0098-1354(90)87016-I |
0.53 |
|
| 1990 |
Skogestad S, Lundström P, Jacobsen EW. Selecting the best distillation control configuration Aiche Journal. 36: 753-764. DOI: 10.1002/Aic.690360512 |
0.471 |
|
| 1989 |
Skogestad S, Jacobsen EW, Lundström P. Selecting the Best Distillation Control Structure Ifac Proceedings Volumes. 22: 315-322. DOI: 10.1016/S1474-6670(17)53373-X |
0.472 |
|
| 1989 |
Skogestad S, Morari M. Robust performance of decentralized control systems by independent designs Automatica. 25: 119-125. DOI: 10.1016/0005-1098(89)90127-1 |
0.596 |
|
| 1988 |
Skogestad S, Morari M. Some new properties of the structured singular value Ieee Transactions On Automatic Control. 33: 1151-1154. DOI: 10.1109/9.14437 |
0.509 |
|
| 1988 |
Skogestad S, Morari M, Doyle J. Robust control of ill-conditioned plants: high-purity distillation Ieee Transactions On Automatic Control. 33: 1092-1105. DOI: 10.1109/9.14431 |
0.598 |
|
| 1988 |
Skogestad S, Morari M. Understanding the Dynamic Behavior of Distillation Columns Industrial & Engineering Chemistry Research. 27: 1848-1862. DOI: 10.1021/Ie00082A018 |
0.434 |
|
| 1988 |
Skogestad S, Morari M. Implications of large RGA-elements on control performance [Erratum to document cited in CA107(22):201333n] Industrial & Engineering Chemistry Research. 27: 898-898. DOI: 10.1021/Ie00077A031 |
0.474 |
|
| 1988 |
Skogestad S, Morari M. LV-Control of a high-purity distillation column Chemical Engineering Science. 43: 33-48. DOI: 10.1016/0009-2509(88)87124-0 |
0.604 |
|
| 1987 |
Skogestad S, Morari M. Implications of large RGA elements on control performance Industrial & Engineering Chemistry Research. 26: 2323-2330. DOI: 10.1021/Ie00071A025 |
0.578 |
|
| 1987 |
Skogestad S, Morari M. Effect of disturbance directions on closed-loop performance Industrial & Engineering Chemistry Research. 26: 2029-2035. DOI: 10.1021/Ie00070A017 |
0.589 |
|
| 1987 |
Skogestad S, Morari M. Robust Control of Distillation Columns Ifac Proceedings Volumes. 20: 265-270. DOI: 10.1016/S1474-6670(17)55449-X |
0.619 |
|
| 1987 |
Skogestad S, Morari M. LV-control of a High-purity Distillation Column Ifac Proceedings Volumes. 20: 387-396. DOI: 10.1016/S1474-6670(17)55115-0 |
0.602 |
|
| 1987 |
Skogestad S, Morari M. The Dominant Time Constant For Distillation Columns Computers & Chemical Engineering. 11: 607-617. DOI: 10.1016/0098-1354(87)87006-0 |
0.514 |
|
| 1987 |
Skogestad S, Morari M. Design of resilient processing plants-IX. Effect of model uncertainty on dynamic resilience Chemical Engineering Science. 42: 1765-1780. DOI: 10.1016/0009-2509(87)80181-1 |
0.59 |
|
| 1987 |
Skogestad S, Morari M. Control configuration selection for distillation columns Aiche Journal. 33: 1620-1635. DOI: 10.1002/Aic.690331006 |
0.629 |
|
| 1986 |
Rivera DE, Morari M, Skogestad S. Internal model control: PID controller design Industrial & Engineering Chemistry Process Design and Development. 25: 252-265. DOI: 10.1021/I200032A041 |
0.705 |
|
| Show low-probability matches. |
