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Development of a Validated Rate-Based Model for CO2 Absorption in Aqueous 2‑Amino-2-methyl-1-propanol and Piperazine
Diego Morlando1, Ying Zhang2, Shu Wang3
1Department of Chemical Engineering, Norwegian University of Science and Technology, Trondheim N-7491, Norway.
A new thermodynamic model accurately predicts CO2 absorption in amine solutions, crucial for carbon capture technologies. This framework enhances process design and efficiency for capturing carbon dioxide using 2-amino-2-methyl-1-propanol and piperazine mixtures.
Area of Science:
- Chemical Engineering
- Thermodynamics
- Carbon Capture Technologies
Background:
- Carbon dioxide (CO2) absorption using amine solutions is a key technology for post-combustion carbon capture.
- Aqueous mixtures of 2-amino-2-methyl-1-propanol (AMP) and piperazine (PZ) are promising absorbents due to their favorable properties.
- Accurate thermodynamic models are essential for optimizing the design and operation of CO2 capture processes.
Purpose of the Study:
- To develop and validate a new e-NRTL thermodynamic framework for modeling CO2 absorption in aqueous AMP/PZ mixtures.
- To accurately predict CO2 solubility, total pressure, heat of absorption, and free CO2 concentration.
- To assess the model's performance across a wide range of operating conditions and amine concentrations.
Main Methods:
- Development of an e-NRTL thermodynamic framework in Aspen Plus for the CO2-AMP-PZ-H2O system.
- Fitting the model parameters using experimental data for varying AMP and PZ concentrations, temperatures, and CO2 loadings.
- Validation of the model with pilot-scale campaign data, incorporating mass transfer and kinetics.
Main Results:
- The e-NRTL model achieved an Absolute Average Relative Deviation (AARD) of 26.3% for CO2 solubility and 7.0% for total pressure.
- The model accurately predicted the heat of absorption (AARD 10.2%) and free CO2 concentration (AARD 13.1%).
- Rate-based model predictions for CO2 capture, rich loading, and reboiler duty were within 5% AARD of pilot campaign data.
Conclusions:
- The developed e-NRTL thermodynamic framework provides a robust and accurate representation of CO2 absorption in aqueous AMP/PZ solutions.
- The model demonstrates good predictive capability for key process variables relevant to industrial CO2 capture applications.
- The validated model, coupled with mass transfer and kinetics, is suitable for designing and optimizing large-scale carbon capture facilities.
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