Machine learning-based ethylene concentration estimation, real-time optimization and feedback control of an experimental electrochemical reactor
Journal Article
·
· Chemical Engineering Research and Design
- University of California, Los Angeles, CA (United States); OSTI
- University of California, Los Angeles, CA (United States)
With the increase in electricity supply from clean energy sources, electrochemical reduction of carbon dioxide (CO2) has received increasing attention as an alternative source of carbon-based fuels. As CO2 reduction is becoming a stronger alternative for the clean production of chemicals, the need to model, optimize and control the electrochemical reduction of the CO2 process becomes inevitable. However, on one hand, a first-principles model to represent the electrochemical CO2 reduction has not been fully developed yet because of the complexity of its reaction mechanism, which makes it challenging to define a precise state-space model for the control system. On the other hand, the unavailability of efficient concentration measurement sensors continues to challenge our ability to develop feedback control systems. Gas chromatography (GC) is the most common equipment for monitoring the gas product composition, but it requires a period of time to analyze the sample, which means that GC can provide only delayed measurements during the operation. Moreover, the electrochemical CO2 reduction process is catalyzed by a fast-deactivating copper catalyst and undergoes a selectivity shift from the product-of-interest at the later stages of experiments, which can pose a challenge for conventional control methods. To this end, machine learning (ML) techniques provide a potential approach to overcome those difficulties due to their demonstrated ability to capture the dynamic behavior of a chemical process from data. Motivated by the above considerations, we propose a machine learning-based modeling methodology that integrates support vector regression and first-principles modeling to capture the dynamic behavior of an experimental electrochemical reactor; this model, together with limited gas chromatography measurements, is employed to predict the evolution of gas-phase ethylene concentration. The model prediction is directly used in a proportional-integral (PI) controller that manipulates the applied potential to regulate the gas-phase ethylene concentration at energy-optimal set-point values computed by a real-time process optimizer (RTO). Specifically, the RTO calculates the operation set-point by solving an optimization problem to maximize the economic benefit of the reactor. Finally, suitable compensation methods are introduced to further account for the experimental uncertainties and handle catalyst deactivation. The proposed modeling, optimization, and control approaches are the first demonstration of active control for a CO2 electrolyzer and contribute to the automation and scale-up efforts for electrified manufacturing of fuels and chemicals starting from CO2.
- Research Organization:
- University of California, Los Angeles, CA (United States)
- Sponsoring Organization:
- USDOE Office of Energy Efficiency and Renewable Energy (EERE)
- Grant/Contract Number:
- EE0007613
- OSTI ID:
- 1976960
- Alternate ID(s):
- OSTI ID: 1961079
- Journal Information:
- Chemical Engineering Research and Design, Journal Name: Chemical Engineering Research and Design Journal Issue: C Vol. 185; ISSN 0263-8762
- Publisher:
- ElsevierCopyright Statement
- Country of Publication:
- United States
- Language:
- English
Similar Records
Machine learning-based ethylene and carbon monoxide estimation, real-time optimization, and multivariable feedback control of an experimental electrochemical reactor
CO2 Conversion to Butene via a Tandem Photovoltaic–Electrochemical/Photothermocatalytic Process: A Co-design Approach to Coupled Microenvironments
Reactor design and integration with product detection to accelerate screening of electrocatalysts for carbon dioxide reduction
Journal Article
·
Tue Feb 07 19:00:00 EST 2023
· Chemical Engineering Research and Design
·
OSTI ID:2418511
CO2 Conversion to Butene via a Tandem Photovoltaic–Electrochemical/Photothermocatalytic Process: A Co-design Approach to Coupled Microenvironments
Journal Article
·
Wed Aug 14 20:00:00 EDT 2024
· ACS Energy Letters
·
OSTI ID:2441454
Reactor design and integration with product detection to accelerate screening of electrocatalysts for carbon dioxide reduction
Journal Article
·
Tue Dec 25 19:00:00 EST 2018
· Review of Scientific Instruments
·
OSTI ID:1610788