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Thomas F. Edgar
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2020 – today
- 2024
- [j30]Alkiviadis Skouteris
, Ioannis Giannikopoulos
Implementation of nonlinear variable-cost network optimization models for technology assessment in the petrochemicals industry. Comput. Chem. Eng. 180: 108459 (2024) - 2023
- [j29]Kyeongjun Seo, Adhika P. Retnanto, Jorge L. Martorell, Thomas F. Edgar, Mark A. Stadtherr, Michael Baldea
Simultaneous design and operational optimization for flexible carbon capture process using ionic liquids. Comput. Chem. Eng. 178: 108344 (2023) - 2021
- [j28]Kyeongjun Seo, Zhichao Chen
Modeling and optimization of ionic liquid-based carbon capture process using a thin-film unit. Comput. Chem. Eng. 155: 107522 (2021) - 2020
- [j27]Jietae Lee, Friedrich Y. Lee, Michael Baldea, Thomas F. Edgar:
Methods of weighted moments for the relay feedback autotuning of conservative PI controllers. Comput. Chem. Eng. 136: 106797 (2020)
2010 – 2019
- 2018
- [j26]Joseph G. Costandy
A scheduling perspective on the monetary value of improving process control. Comput. Chem. Eng. 112: 121-131 (2018) - [j25]Thomas F. Edgar, Efstratios N. Pistikopoulos
Smart manufacturing and energy systems. Comput. Chem. Eng. 114: 130-144 (2018) - [j24]Joseph G. Costandy
Reprint of: A scheduling perspective on the monetary value of improving process control. Comput. Chem. Eng. 116: 268-278 (2018) - [c34]Hari S. Ganesh, Ofodike A. Ezekoye
Improving energy efficiency of an austenitization furnace by heat integration and real-time optimization. AQTR 2018: 1-6 - [c33]Jietae Lee, Thomas F. Edgar:
Three-Parameter Models for Conservative Relay Feedback Autotuning*. ICCA 2018: 975-980 - 2017
- [j23]Ankur Kumar, Michael Baldea, Thomas F. Edgar:
A physics-based model for industrial steam-methane reformer optimization with non-uniform temperature field. Comput. Chem. Eng. 105: 224-236 (2017) - [j22]Ankur Kumar, Thomas F. Edgar, Michael Baldea:
Multi-resolution model of an industrial hydrogen plant for plantwide operational optimization with non-uniform steam-methane reformer temperature field. Comput. Chem. Eng. 107: 271-283 (2017) - [c32]Hari S. Ganesh, Eric M. Taleff, Thomas F. Edgar, Michael Baldea:
Simultaneous optimization of material properties and energy efficiency of a steel quench hardening process. ACC 2017: 2219-2224 - 2016
- [c31]Krystian X. Perez, Michael Baldea, Thomas F. Edgar:
Integrated smart appliance scheduling and HVAC control for peak residential load management. ACC 2016: 1458-1463 - 2014
- [j21]Ricardo Dunia, Gary T. Rochelle, Thomas F. Edgar, Mark Nixon:
Multivariate monitoring of a carbon dioxide removal process. Comput. Chem. Eng. 60: 381-395 (2014) - [j20]Kye Hyun Baek, Thomas F. Edgar, Kiwook Song, Gilheyun Choi, Han Ku Cho, Chonghun Han:
An effective procedure for sensor variable selection and utilization in plasma etching for semiconductor manufacturing. Comput. Chem. Eng. 61: 20-29 (2014) - [j19]John D. Hedengren
Nonlinear modeling, estimation and predictive control in APMonitor. Comput. Chem. Eng. 70: 133-148 (2014) - [c30]Wesley J. Cole, Krystian X. Perez, Joshua D. Rhodes, Michael E. Webber, Michael Baldea, Thomas F. Edgar:
Community-scale air conditioning control for high penetration of rooftop photovoltaics. ACC 2014: 398-403 - 2013
- [j18]Ricardo Dunia, Gary T. Rochelle, Matt Walters, Thomas F. Edgar:
Control of carbon dioxide solubility in aqueous piperazine. Comput. Chem. Eng. 54: 122-124 (2013) - [c29]Wesley J. Cole
Building energy model reduction for model predictive control using OpenStudio. ACC 2013: 449-454 - [c28]Kody M. Powell
Dynamic optimization of a solar thermal energy storage system over a 24 hour period using weather forecasts. ACC 2013: 2946-2951 - [c27]Jong S. Kim, Kody M. Powell
Nonlinear model predictive control for a heavy-duty gas turbine power plant. ACC 2013: 2952-2957 - [c26]Ricardo Dunia, Thomas F. Edgar, Gary T. Rochelle, Mark Nixon:
Monitoring of carbon dioxide capture processes. ACC 2013: 3723-3728 - [c25]Sepideh Ziaiifashami, Gary T. Rochelle, Thomas F. Edgar:
An effective multi-loop control system to improve control performance of CO2 capture. ACC 2013: 3729-3734 - [c24]Jin Wang, Q. Peter He, Thomas F. Edgar:
Improved state estimation for high-mix semiconductor manufacturing. ACC 2013: 6649-6654 - [c23]Kody M. Powell
Dynamic optimization of a campus cooling system with thermal storage. ECC 2013: 4077-4082 - 2012
- [j17]Jeffrey J. Siirola, Thomas F. Edgar:
Process energy systems: Control, economic, and sustainability objectives. Comput. Chem. Eng. 47: 134-144 (2012) - [j16]Jim Davis, Thomas F. Edgar, James Porter, John Bernaden, Michael Sarli:
Smart manufacturing, manufacturing intelligence and demand-dynamic performance. Comput. Chem. Eng. 47: 145-156 (2012) - [c22]Benjamin J. Spivey, John D. Hedengren, Thomas F. Edgar:
Constrained control and optimization of tubular solid oxide fuel cells for extending cell lifetime. ACC 2012: 1356-1361 - [c21]Wesley J. Cole, Thomas F. Edgar, Atila Novoselac:
Use of model predictive control to enhance the flexibility of thermal energy storage cooling systems. ACC 2012: 2788-2793 - [c20]Ricardo Dunia, Thomas F. Edgar, Terry Blevins, Willy Wojsznis:
Multistate PLS for continuous processes. ACC 2012: 2794-2799 - [c19]Ricardo Dunia, Vinay Kumar, Thomas F. Edgar, Terry Blevins, Willy Wojsznis:
Multistate PCA for continuous processes. ACC 2012: 6673-6678 - 2011
- [j15]Ricardo Dunia, Thomas F. Edgar:
Modeling of tumor growth undergoing virotherapy. Comput. Biol. Medicine 41(10): 922-935 (2011) - [c18]Kody M. Powell
Control of a large scale solar thermal energy storage system. ACC 2011: 1530-1535 - [c17]Ricardo Dunia, Thomas F. Edgar:
Tumor irrigation model for virotherapy cancer treatment. ACC 2011: 5426-5431 - 2010
- [c16]Iván Castillo, Thomas F. Edgar, Benito R. Fernández:
Robust nonlinear fault detection applied to chemical processes. ACC 2010: 3623-3628 - [c15]Jin Wang, Q. Peter He, Thomas F. Edgar:
Control performance assessment and diagnosis for semiconductor processes. ACC 2010: 7004-7009
2000 – 2009
- 2009
- [j14]Amogh V. Prabhu, Thomas F. Edgar, Rick Good:
Missing data estimation for run-to-run EWMA-controlled processes. Comput. Chem. Eng. 33(11): 1861-1869 (2009) - [c14]Ivan Castillo, Thomas F. Edgar:
Using a distributed control system (DCS) for distillation column control in an undergraduate unit operations laboratory. ACC 2009: 2744-2748 - [p1]Thomas F. Edgar, Juergen Hahn:
Process Automation. Handbook of Automation 2009: 529-543 - 2008
- [j13]John D. Hedengren
Approximate nonlinear model predictive control with in situ adaptive tabulation. Comput. Chem. Eng. 32(4-5): 706-714 (2008) - [c13]Ricardo Dunia, Thomas F. Edgar, Finn Haugen:
A complete programming framework for process control education. CCA 2008: 516-521 - [c12]Yang Zhang, Thomas F. Edgar:
A robust Dynamic Time Warping algorithm for batch trajectory synchronization. ACC 2008: 2864-2869 - 2007
- [j12]Christopher A. Bode, Jin Wang
Run-to-run control and state estimation in high-mix semiconductor manufacturing. Annu. Rev. Control. 31(2): 241-253 (2007) - [c11]Terry G. Farmer, Nicholas A. Peppas, Thomas F. Edgar:
Design of A Polymeric Insulin Infusion System For Blood Glucose Control. ACC 2007: 607-612 - [c10]Yang Zhang, Thomas F. Edgar:
On-line batch process monitoring using modified dynamic batch PCA. ACC 2007: 2551-2556 - [c9]Jin Wang, Q. Peter He, Thomas F. Edgar:
A General Framework for State Estimation in High-Mix Semiconductor Manufacturing. ACC 2007: 3636-3641 - 2006
- [j11]Thomas F. Edgar, Babatunde A. Ogunnaike
Renovating the undergraduate process control course. Comput. Chem. Eng. 30(10-12): 1749-1762 (2006) - [j10]Thomas F. Edgar, Babatunde A. Ogunnaike
A global view of graduate process control education. Comput. Chem. Eng. 30(10-12): 1763-1774 (2006) - 2005
- [j9]John D. Hedengren
Order reduction of large scale DAE models. Comput. Chem. Eng. 29(10): 2069-2077 (2005) - 2004
- [j8]Jietae Lee, Thomas F. Edgar:
ISE tuning rule revisited. Autom. 40(8): 1455-1458 (2004) - [j7]Jietae Lee, Thomas F. Edgar:
Simulations of stable non-conventional and large dimensional linear processes using the FFT method. Comput. Chem. Eng. 28(4): 479-485 (2004) - [j6]Thomas F. Edgar:
Control and operations: when does controllability equal profitability? Comput. Chem. Eng. 29(1): 41-49 (2004) - [j5]Yue Chen, Thomas F. Edgar, Vasilios I. Manousiouthakis:
On infinite-time nonlinear quadratic optimal control. Syst. Control. Lett. 51(3-4): 259-268 (2004) - [c8]John D. Hedengren, Thomas F. Edgar:
In situ adaptive tabulation for real-time control. ACC 2004: 2222-2226 - 2003
- [c7]Dale E. Seborg, Thomas F. Edgar, Duncan A. Mellichamp:
Teaching process control in the 21st century: what has changed? ACC 2003: 710-712 - [c6]Yue Chen, Thomas F. Edgar, Vasilios I. Manousiouthakis:
On infinite-time nonlinear quadratic optimal control. CDC 2003: 221-226 - [c5]Jietae Lee, Thomas F. Edgar:
Upper bounds of structured singular values for mixed uncertainties. CDC 2003: 798-802 - 2002
- [c4]Jietae Lee, Thomas F. Edgar:
Interaction measure for decentralized control of multivariable processes. ACC 2002: 454-458 - [c3]W. Jarrett Campbell, Stacy K. Firth
A comparison of run-to-run control algorithms. ACC 2002: 2150-2155 - 2001
- [j4]Byung-Su Ko, Thomas F. Edgar:
Performance assessment of multivariable feedback control systems. Autom. 37(6): 899-905 (2001) - [j3]Jietae Lee, Thomas F. Edgar:
Real structured singular value conditions for the strong D-stability. Syst. Control. Lett. 44(4): 273-277 (2001) - 2000
- [j2]Thomas F. Edgar, Stephanie W. Butler, W. Jarrett Campbell, Carlos Pfeiffer, Christopher A. Bode, Sung Bo Hwang, K. S. Balakrishnan, Juergen Hahn
Automatic control in microelectronics manufacturing: Practices, challenges, and possibilities. Autom. 36(11): 1567-1603 (2000) - [j1]Yinlun Huang, Helen H. Lou
Fuzzy model predictive control. IEEE Trans. Fuzzy Syst. 8(6): 665-678 (2000) - [c2]Juergen Hahn, Thomas F. Edgar:
Reduction of nonlinear models using balancing of empirical gramians and Galerkin projections. ACC 2000: 2864-2868 - [c1]Byung-Su Ko, Thomas F. Edgar:
Performance assessment of multivariable feedback control systems. ACC 2000: 4373-4377
Coauthor Index
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last updated on 2024-10-07 21:21 CEST by the dblp team
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