Journal of Oil, Gas and Petrochemical Technology

Journal of Oil, Gas and Petrochemical Technology

Optimal solvent definition for gas treatment units with the aim of acid gas enrichment

Document Type : Research Paper

Authors
1 Department of Chemical Engineering, Faculty of Engineering, Ferdowsi University of Mashhad, Mashhad, Iran
2 Department of Chemical Engineering, Faculty of Engineering, Bojnord University, Bojnord, Iran
10.22034/jogpt.2025.513545.1137
Abstract
Increasing the concentration of H2S in the acid gas entering the sulfur recovery unit is one of the key parameters for enhancing the sulfur recovery efficiency. This research aims to determine the optimal solvent for a gas treatment unit with a focus on enriching hydrogen sulfide gas in the feed of the sulfur recovery unit. The data from the design of an industrial-scale gas-treating unit was utilized to achieve the research objectives. For simulation, analysis of results, and plotting graphs, ASPEN-HYSYS V11 and DESIGN EXPERT V10 software were employed, respectively. The solvents available in the GPSA handbook were utilized for the solvent and additives selection. In the formulation of a composite solvent, DEA and MDEA solvents were considered as the base solvents, considering the weight percentage range used in the gas processing industry, and other solvents were considered as additives to the composite solvent. Simulation results were analyzed by comparing them with the standards of the Iranian National Gas Company. The results indicated that the combination of MDEA with 42.5wt% as the base solvent and Sulfolane with 7.5wt% as an additive will be the optimum solvent. The reason for this selection is that there will be the maximum H2S concentration in the acid gas while adhering to the mentioned standards. The optimum solvent can increase the concentration of H2S from 33.6 mol% to 41.84 mol% in the acidic gas to the Sulphur recovery unit.
Keywords

[1]          B. Zarenezhad, "Consider different alternatives for enriching lean acid gases," in "Hydrocarbon Processing," 0018-8190, 2011, vol. 90 Available: https://www.cheric.org/research/tech/periodicals/view.php?seq=1000552.
[2]          P. P. Crevier, P. D. Clark, N. I. Dowling, and M. Huang, "Quantifying the Effect of Individual Aromatic Contaminants on a Claus Catalyst," Saudi Aramco J. Tech, vol. 47, no. 1, 2001.
[3]          J. Shams and B. Karami, Natural gas & Iran’s gas refinery, 1st ed. Tehran: INGC, 2016, p. 126.
[4]          M. Vakili, P. Koutník, and J. Kohout, "Addressing Hydrogen Sulfide Corrosion in Oil and Gas Industries: A Sustainable Perspective," vol. 16, no. 4, p. 1661, 2024.
[5]          M. Koolivand Salooki, M. Keshavaz Bahdori, M. Esfandyari, K. Mohammad Beigi, J. Sadeghzade, and Ahari, "Economical investigation and optimization of rich amine inlet temperature of regeneration column and its effect on Amine solvent gas sweetening plant %J Journal of Mineral Resources Engineering," (in Fa), Journal of Mineral Resources Engineering, vol. 4, no. 1, pp. 35-43, 2019.
[6]          A. Shahsavand and A. Garmroodi, "Simulation of Khangiran gas treating units for various cooling scenarios," Journal of Natural Gas Science and Engineering, vol. 2, no. 6, pp. 277-283, 2010/12/01/ 2010.
[7]          H. Soltani Panah, A. H. Mohammadi, and D. Ramjugernath, "Development of a novel approach for modeling acid gas solubility in alkanolamine aqueous solution," Journal of Natural Gas Science and Engineering, vol. 34, pp. 112-123, 2016/08/01/ 2016.
[8]          M. Stewart and K. Arnold, "Part 1 - Gas Sweetening1,2," in Gas Sweetening and Processing Field Manual, M. Stewart and K. Arnold, Eds. Boston: Gulf Professional Publishing, 2011, pp. 1-140.
[9]          V. K. IKPEZE, J. O. OWOLABI, I. I. OLATEJU, and A. GIWA, "Modelling and Simulation of Acid Gas Absorption from Natural Gas by Amine Solution Using Aspen HYSYS," in SPE Nigeria Annual International Conference and Exhibition, 2021, vol. Day 2 Tue, August 03, 2021, D021S006R005.
[10]        N. M. A. Al-Lagtah, S. Al-Habsi, and S. A. Onaizi, "Optimization and performance improvement of Lekhwair natural gas sweetening plant using Aspen HYSYS," Journal of Natural Gas Science and Engineering, vol. 26, pp. 367-381, 2015/09/01/ 2015.
[11]        Y. E. Chew, Z. A. Putra, and D. C. Y. Foo, "Process simulation and optimisation for acid gas removal system in natural gas processing," Journal of Natural Gas Science and Engineering, vol. 107, p. 104764, 2022/11/01/ 2022.
[12]        M. M. Vaidya et al., "Hybrid Membrane and Solvent Acid Gas Enrichment for Enhanced CO2 Capture," in ADIPEC, 2022, vol. Day 3 Wed, November 02, 2022, D031S077R004.
[13]        M. Ghavami, M. Gholizadeh, and M. Deymi-Dashtebayaz, "Parametric study and optimization of an acid gas enrichment plant with outlet streams and energy usage consideration," Journal of Cleaner Production, vol. 440, p. 140496, 2024/02/10/ 2024.
[14]        A. Garmroodi Asil and A. Shahsavand, "Reliable estimation of optimal sulfinol concentration in gas treatment unit via novel stabilized MLP and regularization network," Journal of Natural Gas Science and Engineering, vol. 21, pp. 791-804, 2014/11/01/ 2014.
[15]        J. Xue, C. Yang, J. Fu, J. He, and J. Li, "Research and Performance Evaluation on Selective Absorption of H2S from Gas Mixtures by Using Secondary Alkanolamines," Processes, vol. 10, no. 9, p. 1795, 2022.
[16]        V. Pirouzfar and C.-H. Su, "Acid gas pretreatment for modification of sulfur recovery process and CO2 capturing by optimized liquefaction process," Energy, vol. 335, p. 137849, 2025/10/30/ 2025.
[17]        X. Cui, W. Lv, H. Ye, and H. Dong, "Development of a selective sequential process for H2S enrichment and CO2 capture in aqueous MDEA solutions," Journal of Cleaner Production, vol. 478, p. 143858, 2024/11/01/ 2024.
[18]        N. S. Darani, R. M. Behbahani, Y. Shahebrahimi, A. Asadi, and A. H. Mohammadi, "Simulation and Optimization of the Acid Gas Absorption Process by an Aqueous Diethanolamine Solution in a Natural Gas Sweetening Unit," ACS Omega, vol. 6, no. 18, pp. 12072-12080, 2021/05/11 2021.
[19]        SGPC, "The enhanced capacity projects of gas purification units," Shahid hashminejhad gas refinery, Sarakhs2004 2004.