(675e) Carbon Capture Plant Model Identification through Simultaneous State and Parameter Estimation with Sensitivity Analysis
AIChE Annual Meeting
2024
2024 AIChE Annual Meeting
Computing and Systems Technology Division
10D: Applied Math for Energy and Environmental Systems
Thursday, October 31, 2024 - 1:50pm to 2:10pm
necessitating a high-fidelity model.
In this study, we focus on an industrial CCP illustrated in the attached figure. The plant comprises an absorber and a desorber, forming a vital component pair. Within the absorber, a liquid amine-based solution facilitates the absorption of CO2 from the flue gas. Adjacent to the desorber, a reboiler supplies energy to the process, aiding in the separation of CO2 from the liquid, with the captured CO2 collected from the top gas outlet of the desorber. An integral lean-rich heat exchanger (LRHE) positioned between the absorber and desorber effectively utilizes internal energy, thereby reducing the need for additional cooling and heating energy inputs.
The aim of this study is to identify a first-principles model for a CCP utilizing simultaneous state and parameter estimation with sensitivity analysis, leveraging temperature sensor measurements to predict captured CO2 . First, a first-principles model is derived. Then, simultaneous state and parameter estimation is employed to estimate the model parameters based on measured output data. In the process, the model parameters are treated as augmented system states. The sensitivity matrix of the measured outputs to the states and parameters is evaluated based on process data. Based on the sensitivity matrix, orthogonalization is used to determine estimable states and parameters. These estimable states and parameters are then estimated within a moving horizon estimation (MHE) framework.
The resulting model is utilized to predict captured CO2 , with its performance compared against benchmark approaches to demonstrate effectiveness. Preliminary results reveal approximately a 12.0% discrepancy between estimated and actual captured CO2 measurements, showcasing the potential for predictions in advanced control and planning. The subsequent part of the study investigates the benefits of simultaneous state and parameter estimation combined with variable selection using sensitivity analysis. Results indicate a notable improvement in estimation accuracy, with enhancements of 27.5% and 32.3% observed when compared to state-only estimation and state and parameter estimation without selection, respectively.
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