LAPSE:2026.0431
Published Article

LAPSE:2026.0431
A Framework for Flexible Start/Stop Operation of Electrified Chemical Processes
June 12, 2026
Abstract
A flexible start-stop operating policy that involves full shut-down and start-up may be beneficial for electrified plants under certain grid conditions, such as dispatchable demand response. This paper introduces a multi-period Hamilton-Jacobi reachability framework to explore the space of state trajectories for plant shut-down and start-up. Shut-down is defined in terms of operations leading to a stand-by state with no material flows or energy inputs, and variables within safety constraints. Candidate stand-by states are identified by constructing backwards reachability tubes from the desired steady-state operating point. The candidate shut-down/stand-by state is partitioned in fast and slow regions. Admissible control input trajectories are determined for the fast region, from which the minimum time trajectory is selected as optimal for fast start-up. A proof-of-concept simulation using a reaction/separation/recycle plant is presented.
A flexible start-stop operating policy that involves full shut-down and start-up may be beneficial for electrified plants under certain grid conditions, such as dispatchable demand response. This paper introduces a multi-period Hamilton-Jacobi reachability framework to explore the space of state trajectories for plant shut-down and start-up. Shut-down is defined in terms of operations leading to a stand-by state with no material flows or energy inputs, and variables within safety constraints. Candidate stand-by states are identified by constructing backwards reachability tubes from the desired steady-state operating point. The candidate shut-down/stand-by state is partitioned in fast and slow regions. Admissible control input trajectories are determined for the fast region, from which the minimum time trajectory is selected as optimal for fast start-up. A proof-of-concept simulation using a reaction/separation/recycle plant is presented.
Record ID
Keywords
Hamilton-Jacobi Reachability, Optimal Control, Plant Start-up, Process Electrification
Subject
Suggested Citation
Mercer S, Baldea M. A Framework for Flexible Start/Stop Operation of Electrified Chemical Processes. Systems and Control Transactions 5:1825-1832 (2026) https://doi.org/10.69997/sct.125437
Author Affiliations
Mercer S: McKetta Department of Chemical Engineering, The University of Texas at Austin, Austin, TX, USA [ORCID]
Baldea M: McKetta Department of Chemical Engineering, The University of Texas at Austin, Austin, TX, USA. Oden Institute for Computational Science and Engineering, The University of Texas at Austin, Austin, TX, USA [ORCID]
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Baldea M: McKetta Department of Chemical Engineering, The University of Texas at Austin, Austin, TX, USA. Oden Institute for Computational Science and Engineering, The University of Texas at Austin, Austin, TX, USA [ORCID]
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Journal Name
Systems and Control Transactions
Volume
5
First Page
1825
Last Page
1832
Year
2026
Publication Date
2026-06-12
Version Comments
Original Submission
Other Meta
PII: 1825-1832-537-SCT-5-2026, Publication Type: Journal Article
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LAPSE:2026.0431
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https://doi.org/10.69997/sct.125437
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Jun 12, 2026
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References Cited
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