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Simulation and Optimization of Urban Small-Scale Centralized Bio-Gas Purification Process Based on Methyl Diethanolamine Absorbent

Luling Li1, Minghui Li2, Zhengxiang Xu2, Haofeng Lin2, Xuemei Lang2, Peiming Li1, Hengrong Zhang1,*, Dongxu Ji3,*, Jian Liu1, Jianhui Liu1, Guang Yang1, Shuanshi Fan2,*

1 China Shenzhen Gas Corporation Ltd., Shenzhen, 518040, China
2 School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou, 510640, China
3 School of Science and Engineering, The Chinese University of Hong Kong, Shenzhen, 518172, China

* Corresponding Authors: Hengrong Zhang. Email: email; Dongxu Ji. Email: email; Shuanshi Fan. Email: email

Frontiers in Heat and Mass Transfer 2026, 24(1), 8 https://doi.org/10.32604/fhmt.2026.075692

Abstract

This study addresses the energy-intensive challenge of small-scale biogas upgrading by optimizing a chemical absorption process employing methyl diethanolamine (MDEA). Focusing on a typical distributed application of 300 Nm3/d, we developed an integrated simulation-optimization framework using Aspen HYSYS 14.0 to systematically evaluate the effects of critical operating parameters—absorption pressure, MDEA concentration, flow rate, temperature, number of trays, and reboiler duty—on methane purity and energy consumption. The key finding is the identification of an optimal parameter set: absorption pressure of 1200 kPa, MDEA concentration of 20 mol%, lean flow rate of 2.5 kmol/h, temperature of 298.15 K, 20 absorber trays, 10 regenerator trays, and a reboiler duty of 4 kW, which enabled the product gas to achieve a high CH4 concentration of 97 mol%, compliant with pipeline standards. A detailed energy consumption analysis revealed that the reboiler is the most energy-intensive unit, accounting for 75.40% of the total 5.29 kW energy consumption, followed by the gas compressor (23.38%). The specific energy consumption for CH4 recovery and the Energy Consumption Index (ECI) were quantified at 0.8852 kWh/kg CH4 and 6.82, respectively. This work provides a validated optimization strategy and critical energy breakdown, offering practical guidance for enhancing the technical and economic viability of small-scale, centralized biogas purification systems.

Keywords

Chemical absorption process; CO2 capture; bio-gas; optimization; MDEA

Cite This Article

APA Style
Li, L., Li, M., Xu, Z., Lin, H., Lang, X. et al. (2026). Simulation and Optimization of Urban Small-Scale Centralized Bio-Gas Purification Process Based on Methyl Diethanolamine Absorbent. Frontiers in Heat and Mass Transfer, 24(1), 8. https://doi.org/10.32604/fhmt.2026.075692
Vancouver Style
Li L, Li M, Xu Z, Lin H, Lang X, Li P, et al. Simulation and Optimization of Urban Small-Scale Centralized Bio-Gas Purification Process Based on Methyl Diethanolamine Absorbent. Front Heat Mass Transf. 2026;24(1):8. https://doi.org/10.32604/fhmt.2026.075692
IEEE Style
L. Li et al., “Simulation and Optimization of Urban Small-Scale Centralized Bio-Gas Purification Process Based on Methyl Diethanolamine Absorbent,” Front. Heat Mass Transf., vol. 24, no. 1, pp. 8, 2026. https://doi.org/10.32604/fhmt.2026.075692



cc Copyright © 2026 The Author(s). Published by Tech Science Press.
This work is licensed under a Creative Commons Attribution 4.0 International License , which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
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