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Carbon dioxide capture from pulp mill using 2-amino-2-methyl-1-propanol and monoethanolamine blend: Techno-economic assessment of advanced process configuration

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  • Nwaoha, Chikezie
  • Tontiwachwuthikul, Paitoon

Abstract

This project study involves the techno-economic assessment of two new advanced configurations for amine-based carbon dioxide capture from a pulp mill. The newly proposed advanced configurations include advanced rich amine four split (ARA4S), and advanced rich amine three split with desorber inter-heating (ARA3S-DI) which is aimed at reducing carbon capture cost and carbon emissions. The rate-based model in ProMax® 4.0 was used for the simulation study while the flue gas was provided by a 365,000 air dry tonne of pulp (ADt Pulp) per annum pulp mill in British Columbia, Canada. Comparative analysis revealed that the Capture Cost (US$/tCO2 and US$/ADt Pulp) of the 5 kmol/m3 MEA system was lowest for the conventional configuration, while for the 2 kmol/m3 AMP-3 kmol/m3 MEA blend it was lowest for the advanced rich amine 3-split with desorber inter-heating configuration. In addition, the Capture Costs of the MEA solution with a conventional configuration system is 8.7% higher than the AMP-MEA blend with advanced rich amine three split with desorber inter-heating configuration. Sensitivity analysis revealed that the combined effect of a carbon tax (US$ 40/tCO2), CO2 sales price (US$ 40/tCO2) and advanced configuration only led to a slight increase (2.6% for MEA and 2.1% for AMP-MEA blend) in the price of the northern bleached softwood kraft pulp. With an even better-performing solvent system and process configuration, the price of NBSK pulp may not be affected given the indicated CO2 tax and CO2 price regime.

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  • Nwaoha, Chikezie & Tontiwachwuthikul, Paitoon, 2019. "Carbon dioxide capture from pulp mill using 2-amino-2-methyl-1-propanol and monoethanolamine blend: Techno-economic assessment of advanced process configuration," Applied Energy, Elsevier, vol. 250(C), pages 1202-1216.
    • Handle: RePEc:eee:appene:v:250:y:2019:i:c:p:1202-1216
    DOI: 10.1016/j.apenergy.2019.05.097
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    References listed on IDEAS

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    Cited by:

    1. Wang, Rujie & Yang, Yuying & Wang, Mengfan & Lin, Jinshan & Zhang, Shihan & An, Shanlong & Wang, Lidong, 2021. "Energy efficient diethylenetriamine–1-propanol biphasic solvent for CO2 capture: Experimental and theoretical study," Applied Energy, Elsevier, vol. 290(C).
    2. Furszyfer Del Rio, Dylan D. & Sovacool, Benjamin K. & Griffiths, Steve & Bazilian, Morgan & Kim, Jinsoo & Foley, Aoife M. & Rooney, David, 2022. "Decarbonizing the pulp and paper industry: A critical and systematic review of sociotechnical developments and policy options," Renewable and Sustainable Energy Reviews, Elsevier, vol. 167(C).
    3. Patrón, Gabriel D. & Ricardez-Sandoval, Luis, 2022. "An integrated real-time optimization, control, and estimation scheme for post-combustion CO2 capture," Applied Energy, Elsevier, vol. 308(C).
    4. Haider Sultan & Umair Hassan Bhatti & Hafiz Ali Muhammad & Sung Chan Nam & Il Hyun Baek, 2021. "Modification of postcombustion CO2 capture process: A techno‐economic analysis," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 11(1), pages 165-182, February.

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