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Sigurd Skogestad
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2020 – today
- 2024
- [j43]Lucas Ferreira Bernardino
, Sigurd Skogestad
Optimal measurement-based cost gradient estimate for feedback real-time optimization. Comput. Chem. Eng. 189: 108815 (2024) - 2023
- [j42]Sigurd Skogestad
Advanced control using decomposition and simple elements. Annu. Rev. Control. 56: 100903 (2023) - [i1]David Pérez-Piñeiro, Sigurd Skogestad, Stephen Boyd:
Home Energy Management with Dynamic Tariffs and Tiered Peak Power Charges. CoRR abs/2307.07580 (2023) - 2022
- [j41]Cristina Zotica
Bidirectional inventory control with optimal use of intermediate storage. Comput. Chem. Eng. 159: 107677 (2022) - [j40]Dinesh Krishnamoorthy
Real-Time optimization as a feedback control problem - A review. Comput. Chem. Eng. 161: 107723 (2022) - 2021
- [j39]Cristina Zotica
Supervisory control design for balancing supply and demand in a district heating system with thermal energy storage. Comput. Chem. Eng. 149: 107306 (2021) - [c27]Saket Adhau
Constrained Neural Networks for Approximate Nonlinear Model Predictive Control. CDC 2021: 295-300 - 2020
- [j38]Esmaeil Jahanshahi, Krishnamoorthy Dinesh
Plantwide control of an oil production network. Comput. Chem. Eng. 136: 106765 (2020) - [j37]Cristina Zotica
Optimal operation and control of heat to power cycles: A new perspective from a systematic plantwide control approach. Comput. Chem. Eng. 141: 106995 (2020) - [j36]Krishnamoorthy Dinesh
Systematic design of active constraint switching using selectors. Comput. Chem. Eng. 143: 107106 (2020) - [j35]Christoph Josef Backi
Combined state and parameter estimation for not fully observable dynamic systems. IFAC J. Syst. Control. 13: 100103 (2020) - [c26]Krishnamoorthy Dinesh
Real-time Optimal Resource Allocation in an Industrial Symbiotic Network using Transient Measurements. ACC 2020: 3541-3546
2010 – 2019
- 2019
- [j34]Julian Straus
A new termination criterion for sampling for surrogate model generation using partial least squares regression. Comput. Chem. Eng. 121: 75-85 (2019) - [c25]Krishnamoorthy Dinesh
Multistage Model Predictive Control with Online Scenario Tree Update using Recursive Bayesian Weighting. ECC 2019: 1443-1448 - 2018
- [j33]Krishnamoorthy Dinesh
Steady-state real-time optimization using transient measurements. Comput. Chem. Eng. 115: 34-45 (2018) - [j32]Prodromos Daoutidis, Jay H. Lee
Integrating operations and control: A perspective and roadmap for future research. Comput. Chem. Eng. 115: 179-184 (2018) - [j31]Lingjian Ye
Dynamic self-optimizing control for unconstrained batch processes. Comput. Chem. Eng. 117: 451-468 (2018) - [j30]Julian Straus
Surrogate model generation using self-optimizing variables. Comput. Chem. Eng. 119: 143-151 (2018) - [j29]Krishnamoorthy Dinesh
Improving Scenario Decomposition for Multistage MPC Using a Sensitivity-Based Path-Following Algorithm. IEEE Control. Syst. Lett. 2(4): 581-586 (2018) - [c24]Krishnamoorthy Dinesh
A Distributed Optimization Strategy for Large Scale Oil and Gas Production Systems. CCTA 2018: 521-526 - [c23]Christoph Josef Backi, Krishnamoorthy Dinesh
Combined Nonlinear Moving Horizon Estimation and Model Predictive Control Applied to a Compressor for Active Surge Control. CCTA 2018: 1552-1557 - 2017
- [j28]Thomas Bisgaard
Optimal operation and stabilising control of the concentric heat-integrated distillation column (HIDiC). Comput. Chem. Eng. 96: 196-211 (2017) - [c22]Sveinung Johan Ohrem, Christian Holden, Esmaeil Jahanshahi, Sigurd Skogestad:
ℒ1 adaptive anti-slug control. ACC 2017: 444-449 - [c21]Christoph Josef Backi, Sigurd Skogestad:
A simple dynamic gravity separator model for separation efficiency evaluation incorporating level and pressure control. ACC 2017: 2823-2828 - [c20]Torstein Thode Kristoffersen, Christian Holden, Sigurd Skogestad, Olav Egeland
Control-oriented modelling of gas-liquid cylindrical cyclones. ACC 2017: 2829-2836 - [c19]Christoph Josef Backi, Sigurd Skogestad:
Virtual inflow monitoring for a three phase gravity separator. CCTA 2017: 1499-1504 - 2016
- [j27]Xing Qian
Control structure selection for four-product Kaibel column. Comput. Chem. Eng. 93: 372-381 (2016) - [c18]Christoph Josef Backi, Jan Tommy Gravdahl, Sigurd Skogestad:
Robust control of a two-state Greitzer compressor model by state-feedback linearization. CCA 2016: 1226-1231 - [c17]Alejandro Regalado-Méndez
Plant-Wide Control of a Reactive Distillation Column on Biodiesel Production. CSOC (3) 2016: 107-117 - 2015
- [j26]Mario Francisco, Sigurd Skogestad, Pastora Vega:
Model predictive control for the self-optimized operation in wastewater treatment plants: Analysis of dynamic issues. Comput. Chem. Eng. 82: 259-272 (2015) - [r1]Sigurd Skogestad:
Control Structure Selection. Encyclopedia of Systems and Control 2015 - 2014
- [j25]Johannes Jäschke
Optimal operation of heat exchanger networks with stream split: Only temperature measurements are required. Comput. Chem. Eng. 70: 35-49 (2014) - [j24]Kwang Ki Kevin Kim
Necessary and sufficient conditions for robust reliable control in the presence of model uncertainties and system component failures. Comput. Chem. Eng. 70: 67-77 (2014) - 2013
- [c16]Esmaeil Jahanshahi, Sigurd Skogestad, Esten Ingar Grøtli:
Anti-slug control experiments using nonlinear observers. ACC 2013: 1056-1062 - [c15]Esmaeil Jahanshahi, Sigurd Skogestad:
Comparison between nonlinear model-based controllers and gain-scheduling Internal Model Control based on identified model. CDC 2013: 853-860 - [c14]Esmaeil Jahanshahi, Sigurd Skogestad, M. Lieungh:
Subsea solution for anti-slug control of multiphase risers. ECC 2013: 4094-4099 - [c13]Nabil Magbool Jan, Sigurd Skogestad, Sridharakumar Narasimhan:
Optimal selection of sensor network and backed-off operating point based on economics. ECC 2013: 4472-4477 - 2011
- [j23]James J. Downs, Sigurd Skogestad:
An industrial and academic perspective on plantwide control. Annu. Rev. Control. 35(1): 99-110 (2011) - [c12]Ramprasad Yelchuru, Sigurd Skogestad:
Optimal controlled variable selection for individual process units in self optimizing control with MIQP formulations. ACC 2011: 342-347 - [c11]Johannes Jäschke
Self-optimizing invariants in dynamic optimization. CDC/ECC 2011: 7753-7758
2000 – 2009
- 2009
- [j22]Andreas Linhart, Sigurd Skogestad:
Computational performance of aggregated distillation models. Comput. Chem. Eng. 33(1): 296-308 (2009) - [c10]Johannes Jäschke
Optimal operation of a waste incineration plant for district heating. ACC 2009: 665-670 - [c9]Henrik Manum, Sigurd Skogestad, Johannes Jäschke
Convex initialization of the H2-optimal static output feedback problem. ACC 2009: 1724-1729 - [c8]Henrik Manum, Colin N. Jones, Johan Löfberg, Manfred Morari, Sigurd Skogestad:
Bilevel programming for analysis of low-complexity control of linear systems with constraints. CDC 2009: 946-951 - 2008
- [j21]Elvira Marie B. Aske, Stig Strand, Sigurd Skogestad:
Coordinator MPC for maximizing plant throughput. Comput. Chem. Eng. 32(1-2): 195-204 (2008) - [j20]Tore Lid, Sigurd Skogestad:
Scaled steady state models for effective on-line applications. Comput. Chem. Eng. 32(4-5): 990-999 (2008) - [j19]Antonio Araújo, Sigurd Skogestad:
Control structure design for the ammonia synthesis process. Comput. Chem. Eng. 32(12): 2920-2932 (2008) - [c7]Henrik Manum, Sridharakumar Narasimhan
A new approach to explicit MPC using self-optimizing control. ACC 2008: 435-440 - [c6]Hakon Dahl-Olsen, Sridharakumar Narasimhan
Optimal output selection for control of batch processes. ACC 2008: 2870-2871 - [c5]J. Cai, Jørgen Bauck Jensen, Sigurd Skogestad, Jakob Stoustrup
On the trade-off between energy consumption and food quality loss in supermarket refrigeration systems. ACC 2008: 2880-2885 - 2007
- [j18]Jørgen Bauck Jensen, Sigurd Skogestad:
Optimal operation of simple refrigeration cycles: Part I: Degrees of freedom and optimality of sub-cooling. Comput. Chem. Eng. 31(5-6): 712-721 (2007) - [j17]Jørgen Bauck Jensen, Sigurd Skogestad:
Optimal operation of simple refrigeration cycles: Part II: Selection of controlled variables. Comput. Chem. Eng. 31(12): 1590-1601 (2007) - [j16]Vinay Kariwala, J. Fraser Forbes, Sigurd Skogestad:
µ-Interaction measure for unstable systems. Int. J. Autom. Control. 1(4): 295-313 (2007) - 2006
- [c4]Vinay Kariwala, J. Fraser Forbes, Sigurd Skogestad:
-Interaction Measure for Unstable Systems. ICARCV 2006: 1-6 - 2004
- [j15]Sigurd Skogestad:
Control structure design for complete chemical plants. Comput. Chem. Eng. 28(1-2): 219-234 (2004) - [j14]H. K. Engelien, Sigurd Skogestad:
Selecting appropriate control variables for a heat-integrated distillation system with prefractionator. Comput. Chem. Eng. 28(5): 683-691 (2004) - [j13]S. Skouras, Sigurd Skogestad:
Time (energy) requirements in closed batch distillation arrangements. Comput. Chem. Eng. 28(5): 829-837 (2004) - [j12]Audun Faanes, Sigurd Skogestad:
pH-neutralization: integrated process and control design. Comput. Chem. Eng. 28(8): 1475-1487 (2004) - [j11]S. Skouras, Sigurd Skogestad:
Time requirements for heteroazeotropic distillation in batch columns. Comput. Chem. Eng. 28(9): 1689-1700 (2004) - [j10]Sigurd Skogestad:
Near-optimal operation by self-optimizing control: from process control to marathon running and business systems. Comput. Chem. Eng. 29(1): 127-137 (2004) - [j9]Audun Faanes, Sigurd Skogestad:
Feedforward Control under the Presence of Uncertainty. Eur. J. Control 10(1): 30-46 (2004) - [c3]Vinay Kariwala, Sigurd Skogestad, J. Fraser Forbes, Edward S. Meadows:
Input performance limitations of feedback control. ACC 2004: 2063-2068 - 2003
- [j8]Kwo-Liang Wu, Cheng-Ching Yu, William L. Luyben, Sigurd Skogestad:
Reactor/separator processes with recycles-2. Design for composition control. Comput. Chem. Eng. 27(3): 401-421 (2003) - [j7]Kjetil Havre, Sigurd Skogestad:
Selection of variables for stabilizing control using pole vectors. IEEE Trans. Autom. Control. 48(8): 1393-1398 (2003) - [c2]Audun Faanes, Sigurd Skogestad:
Feedforward control under the presence of uncertainty. ECC 2003: 1387-1392
1990 – 1999
- 1999
- [j6]Petter Lundström, Sigurd Skogestad, John C. Doyle:
Two-degree-of-freedom controller design for an ill-conditioned distillation process using μ-synthesis. IEEE Trans. Control. Syst. Technol. 7(1): 12-21 (1999) - [c1]Audun Faanes, Sigurd Skogestad:
Control structure selection for serial processes with application to pH-Neutralization. ECC 1999: 3280-3285 - 1997
- [j5]Morten Hovd
SVD controllers for H2-, H∞- and μ-optimal control. Autom. 33(3): 433-439 (1997) - 1994
- [j4]Morten Hovd
Control of symmetrically interconnected plants. Autom. 30(6): 957-973 (1994) - [j3]Morten Hovd
Sequential design of decentralized controllers. Autom. 30(10): 1601-1607 (1994) - 1992
- [j2]Morten Hovd
Simple frequency-dependent tools for control system analysis, structure selection and design. Autom. 28(5): 989-996 (1992)
1980 – 1989
- 1989
- [j1]Sigurd Skogestad, Manfred Morari:
Robust performance of decentralized control systems by independent designs. Autom. 25(1): 119-125 (1989)
Coauthor Index
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last updated on 2024-12-10 20:48 CET by the dblp team
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