Co-optimization of Amine Formulation and Process Flowsheet for Postcombustion Carbon Capture with Ternary Amine Blends

This study established a rate-based model for the ternary amine (MEA/MDEA/AMP) CO2 capture process and employed a multiobjective genetic algorithm to achieve coordinated optimization of solvent formulation and process parameters. The basic process for CO2 capture using a ternary amine blend is constructed, and the absorber intercooler (AIC) configuration and split-flow (SF) configuration are designed. The results indicate that the AIC process is suitable for higher-concentration absorbents, achieving a 12.25% reduction in liquid-to-gas ratio compared to the basic process and 5.53% reduction in total annual cost (TAC). The SF process significantly decreases the water content in the gas phase of the stripper column, leading to a 22.75% reduction in TAC. When combined, the effects demonstrate cumulative superposition, resulting in a 27.11% reduction in TAC and a 37.39% reduction in carbon emissions. The integration of a multiobjective genetic algorithm for parameter optimization provides an efficient solution for improving composite amine-based carbon capture technology.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2025-12-08
DOI
https://doi.org/10.1021/acs.iecr.5c03117
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
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article

Co-optimization of Amine Formulation and Process Flowsheet for Postcombustion Carbon Capture with Ternary Amine Blends

Shih‐Kang Fan, Xia Tong, Lanyi Sun, Zhenyu Zhang et al.
Industrial & Engineering Chemistry Research
Carbon Dioxide Capture Technologies
article

Co-optimization of Amine Formulation and Process Flowsheet for Postcombustion Carbon Capture with Ternary Amine Blends

Shih‐Kang Fan, Xia Tong, Lanyi Sun, Zhenyu Zhang, Jing Li, Jun Li
article en

Abstract

This study established a rate-based model for the ternary amine (MEA/MDEA/AMP) CO2 capture process and employed a multiobjective genetic algorithm to achieve coordinated optimization of solvent formulation and process parameters. The basic process for CO2 capture using a ternary amine blend is constructed, and the absorber intercooler (AIC) configuration and split-flow (SF) configuration are designed. The results indicate that the AIC process is suitable for higher-concentration absorbents, achieving a 12.25% reduction in liquid-to-gas ratio compared to the basic process and 5.53% reduction in total annual cost (TAC). The SF process significantly decreases the water content in the gas phase of the stripper column, leading to a 22.75% reduction in TAC. When combined, the effects demonstrate cumulative superposition, resulting in a 27.11% reduction in TAC and a 37.39% reduction in carbon emissions. The integration of a multiobjective genetic algorithm for parameter optimization provides an efficient solution for improving composite amine-based carbon capture technology.

Industrial & Engineering Chemistry ResearchVol. 64(50)
China University of Petroleum, East China (CN)
Openalex Percentile: Top 60%
Carbon Dioxide Capture Technologies
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