Carbon dioxide capture using bi-blended and tri-blended amines solution in packed bed absorber

Authors

  • Noor Taha Abdullah Chemical Engineering Department, College of Engineering, University of Baghdad, Baghdad, Iraq
  • Ibtehal K. Shakir Chemical Engineering Department, College of Engineering, University of Baghdad, Baghdad, Iraq https://orcid.org/0000-0001-8333-461X
  • Munaf Al-lami Department of Chemical and Environmental Process Engineering, Faculty of Chemical Technology and Biotechnology, Budapest University of Technology and Economics, Műegyetem rkp. 3., H–1111 Budapest, Hungary

DOI:

https://doi.org/10.31699/IJCPE.2025.4.9

Keywords:

Amine absorption; CO2 removal; Packed bed absorption; amines promoter; piperazine; benzylamine

Abstract

   Carbon capture and storage technologies are crucial in mitigating greenhouse gas emissions. This study investigates the enhancement of CO2 absorption through refining amine blends, specifically diethylenetriamine (DETA) with monoethanolamine (MEA) and tetraethylenepentamine (TEPA) with MEA at different concentrations and employing chemical promoters to boost the performance of the gas treatment system. The behaviour of these amines was evaluated by the impact of mixing DETA and MEA across different concentrations. The results showed that the removal efficiency increased with increasing DETA concentration. Similarly, the TEPA-MEA blend was investigated, demonstrating an increase in removal efficiency with increasing TEPA concentration. Removing efficiency improved from 75% with 30% MEA to about 96% with a 15% MEA and 15% TEPA mixture while maintaining the absorption rate due to the sufficient column height. Also, the study explores the effect of utilizing chemical promoters, specifically piperazine (PZ), potassium carbonate (K₂CO₃), and benzylamine (BZ), when combined with 15 % MEA and 10% DETA to boost the absorption rate and improve the CO2 loading capacity. The findings indicate that adding 5% BZ to the MEA-DETA solution increases removal efficiency by 10%. Moreover, adding 5% PZ to the same mixture increased efficiency by about 18%. Meanwhile, the volumetric mass transfer coefficient, KGav, more than doubled. Finally, the study examined the effect of using the same promoters with 15% MEA and 10% TEPA on CO2 capacity and mass transfer rates. The outcomes demonstrate that both removal effectiveness and KGav were dropped when using BZ and K₂CO₃ in the MEA-TEPA blend. The removal efficiency increased somewhat with PZ, but KGav was not significantly affected. In conclusion, the mass transfer rate and CO2 removal efficiency from flue gases will be enhanced by the use of bi-amines such as MEA-DETA and MEA-TEPA in chemical absorption. However, because they enhance the amine group in the absorbent, promoters such as PZ and BA can raise the carbon dioxide removal efficiency to an economically valuable level.

References

[1] S. T. A. Al-Aridhee and M. Moghiman, “Yearly Energy, Exergy, and Environmental (3E) Analyses of A Photovoltaic Thermal Module and Solar Thermal Collector in Series,” Al-Khwarizmi Engineering Journal, vol. 19, no. 1, pp. 36–56, Mar. 2023, https://doi.org/10.22153/kej.2023.01.001

[2] M. N. Procopio, G. Urquiza, and L. Castro, “Analysis of Absorber Packed Height for Power Plants with Post-Combustion CO2 Capture,” Sustainability, vol. 15, no. 12, p. 9536, Jun. 2023, https://doi.org/10.3390/su15129536

[3] B. I. Waisi, J. T. Majeed, and N. S. Majeed, “Carbon dioxide capture using nonwoven activated carbon nanofiber,” IOP Conference Series Earth and Environmental Science, vol. 779, no. 1, p. 012056, Jun. 2021, https://doi.org/10.1088/1755-1315/779/1/012056

[4] R. Cassia, M. Nocioni, N. Correa-Aragunde, and L. Lamattina, “Climate Change and the Impact of Greenhouse Gasses: CO2 and NO, Friends and Foes of Plant Oxidative Stress,” Frontiers in Plant Science, vol. 9, Mar. 2018, https://doi.org/10.3389/fpls.2018.00273

[5] M. M. Hason, A. O. Al-Sulttani, I. S. Abbood, and A. N. Hanoon, “Emissions Investigating of Carbon Dioxide Generated by the Iraqi Cement Industry,” IOP Conference Series Materials Science and Engineering, vol. 928, no. 2, p. 022041, Nov. 2020, https://doi.org/10.1088/1757-899x/928/2/022041

[6] T. R. Anderson, E. Hawkins, and P. D. Jones, “CO2, the greenhouse effect and global warming: from the pioneering work of Arrhenius and Callendar to today’s Earth System Models,” Endeavour, vol. 40, no. 3, pp. 178–187, Sep. 2016, https://doi.org/10.1016/j.endeavour.2016.07.002

[7] A. W. Dhuyool, I. K. Shakir, and M. Al-Lami, “Carbon Dioxide Removal Using Blended Amine Solution in a Randomly Packed Bed Column,” Iraqi Journal of Chemical and Petroleum Engineering, vol. 25, no. 2, pp. 95–107, Jun. 2024, https://doi.org/10.31699/ijcpe.2024.2.9

[8] M. K. H. Al-Mashhadani and E. M. Khudhair, “Cultivation of Chlorella Vulgaris Using Airlift Photobioreactor Sparged with 5%CO2 -Air as a Biofixing Process,” Journal of Engineering, vol. 23, no. 4, pp. 22–41, Mar. 2017, https://doi.org/10.31026/j.eng.2017.04.02

[9] B. Jaffary, L. Jaafari, and R. Idem, “CO2 Capture Performance Comparisons of Polyamines at Practical Concentrations for Use as Activators for Methyldiethanolamine for Natural Gas Sweetening,” Energy & Fuels, vol. 35, no. 9, pp. 8081–8094, Apr. 2021, https://doi.org/10.1021/acs.energyfuels.1c00164

[10] A. Bhavsar, D. Hingar, S. Ostwal, I. Thakkar, S. Jadeja, and M. Shah, “The current scope and stand of carbon capture storage and utilization ∼ A comprehensive review,” Case Studies in Chemical and Environmental Engineering, vol. 8, p. 100368, Dec. 2023, https://doi.org/10.1016/j.cscee.2023.100368

[11] H. Ling, S. Liu, H. Gao, H. Zhang, and Z. Liang, “Solubility of N2O, equilibrium solubility, mass transfer study and modeling of CO2 absorption into aqueous monoethanolamine (MEA)/1-dimethylamino-2-propanol (1DMA2P) solution for post-combustion CO2 capture,” Separation and Purification Technology, vol. 232, p. 115957, Feb. 2020, https://doi.org/10.1016/j.seppur.2019.115957

[12] A. W. Dhuyool and I. K. Shakir, “Carbon Dioxide Capturing via a Randomly Packed Bed Scrubber Using Primary and Poly Amine Absorbents,” Journal of Ecological Engineering, vol. 24, no. 11, pp. 14–29, Nov. 2023, https://doi.org/10.12911/22998993/170205

[13] Y. Liu, “Research on Status and Outlook of Using Different Solvents for CO2 Capture in a Rotating Packed Bed,” E3S Web of Conferences, vol. 294, p. 06004, Jan. 2021, https://doi.org/10.1051/e3sconf/202129406004

[14] Y. Lee Kim, J., Kim, H., Park, T., Jin, H., Kim, H., Park, S., & Lee, K. S., “Operation of a Pilot-Scale CO2 Capture Process with a New Energy-Efficient Polyamine Solvent,” Applied Sciences, vol. 10, no. 21, p. 7669, Oct. 2020, https://doi.org/10.3390/app10217669

[15] F. Barzagli, M. Peruzzini, and R. Zhang, “Direct CO2 capture from air with aqueous and nonaqueous diamine solutions: a comparative investigation based on 13C NMR analysis,” Carbon Capture Science & Technology, vol. 3, p. 100049, Jun. 2022, https://doi.org/10.1016/j.ccst.2022.100049

[16] B. Aghel, S. Janati, S. Wongwises, and M. S. Shadloo, “Review on CO2 capture by blended amine solutions,” International Journal of Greenhouse Gas Control, vol. 119, p. 103715, Sep. 2022, https://doi.org/10.1016/j.ijggc.2022.103715

[17] X. Luo. Fu, K., Yang, Z., Gao, H., Rongwong, W., Liang, Z., and Tontiwachwuthikul, P “Experimental Studies of Reboiler Heat Duty for CO2 Desorption from Triethylenetetramine (TETA) and Triethylenetetramine (TETA) + N-Methyldiethanolamine (MDEA),” Industrial & Engineering Chemistry Research, vol. 54, no. 34, pp. 8554–8560, Aug. 2015, https://doi.org/10.1021/acs.iecr.5b00158

[18] A. Aroonwilas and A. Veawab, “Characterization and Comparison of the CO2 Absorption Performance into Single and Blended Alkanolamines in a Packed Column,” Industrial & Engineering Chemistry Research, vol. 43, no. 9, pp. 2228–2237, Apr. 2004, http://dx.doi.org/10.1021/ie0306067

[19] A. Naami, M. Edali, T. Sema, R. Idem, and P. Tontiwachwuthikul, “Mass Transfer Performance of CO2 Absorption into Aqueous Solutions of 4-Diethylamino-2-butanol, Monoethanolamine, and N-Methyldiethanolamine,” Industrial & Engineering Chemistry Research, vol. 51, no. 18, pp. 6470–6479, Apr. 2012, http://dx.doi.org/10.1021/ie2008357

[20] M. Afkhamipour and M. Mofarahi, “Effects of operating parameters of packed columns on the KGav for CO2 absorption by amine solutions using optimization–simulation framework,” Separation and Purification Technology, vol. 202, pp. 86–102, Aug. 2018, http://dx.doi.org/10.1016/j.seppur.2018.03.026

[21] P. Vaewhongs , K. Photein, R. Nimchareon, T. Limlertchareonwanit1 , K. Minakanishtha, K. Maneeintr and T. Charinpanitkul, “Gas-phase mass transfer coefficient of CO2 in different alkanolamine solutions within packed-bed absorption column,” The Second Materials Research Society Of Thailand International Conference, 2020, Published, http://dx.doi.org/10.1063/5.0023685

[22] K. Fu, Sema, T., Liang, Z., Liu, H., Na, Y., Shi, H., Idem, R., & Tontiwachwuthikul, P.., “Investigation of Mass-Transfer Performance for CO2 Absorption into Diethylenetriamine (DETA) in a Randomly Packed Column,” Industrial & Engineering Chemistry Research, vol. 51, no. 37, pp. 12058–12064, Sep. 2012, https://doi.org/10.1021/ie300830h

[23] M. Afkhamipour and M. Mofarahi, “Review on the mass transfer performance of CO2 absorption by amine-based solvents in low- and high-pressure absorption packed columns,” RSC Advances, vol. 7, no. 29, pp. 17857–17872, Jan. 2017, https://doi.org/10.1039/c7ra01352c

[24] N. E. Hadri, D. V. Quang, E. L. V. Goetheer, and M. R. M. A. Zahra, “Aqueous amine solution characterization for post-combustion CO2 capture process,” Applied Energy, vol. 185, pp. 1433–1449, Jan. 2017, https://doi.org/10.1016/j.apenergy.2016.03.043

[25] J. Narku-Tetteh, P. Muchan, C. Saiwan, T. Supap, and R. Idem, “Selection of components for formulation of amine blends for post combustion CO2 capture based on the side chain structure of primary, secondary and tertiary amines,” Chemical Engineering Science, vol. 170, pp. 542–560, Oct. 2017, https://doi.org/10.1016/j.ces.2017.02.036

[26] C. Nwaoha .Supap, T., Idem, R., Saiwan, C., Tontiwachwuthikul, P., Al-Marri, M. J., and Benamor, A., “Advancement and new perspectives of using formulated reactive amine blends for post-combustion carbon dioxide (CO2) capture technologies,” Petroleum, vol. 3, no. 1, pp. 10–36, Mar. 2017, https://doi.org/10.1016/j.petlm.2016.11.002

[27] T.-W. Wu, Y.-T. Hung, M.-T. Chen, and C.-S. Tan, “CO2 capture from natural gas power plants by aqueous PZ/DETA in rotating packed bed,” Separation and Purification Technology, vol. 186, pp. 309–317, Oct. 2017, https://doi.org/10.1016/j.seppur.2017.05.040

Downloads

Published

2025-12-30

How to Cite

Abdullah, N. T., Shakir, I. K., & Al-lami, M. (2025). Carbon dioxide capture using bi-blended and tri-blended amines solution in packed bed absorber. Iraqi Journal of Chemical and Petroleum Engineering, 26(4), 97-108. https://doi.org/10.31699/IJCPE.2025.4.9