The effect of increasing CO2 concentration and flow rate on amine still performance in meeting gas sale specifications

Yuswan Muharam; Hendra Kristianto

doi:10.1051/e3sconf/20186703006

All issues

Volume 67 (2018)

E3S Web Conf., 67 (2018) 03006

References

Open Access

Issue		E3S Web Conf. Volume 67, 2018 The 3^rd International Tropical Renewable Energy Conference “Sustainable Development of Tropical Renewable Energy” (i-TREC 2018)


Article Number		03006
Number of page(s)		8
Section		Multifunctional and Advanced Materials
DOI		https://doi.org/10.1051/e3sconf/20186703006
Published online		26 November 2018

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[1] Fernando Camacho. “Kinetics of the reaction of pure CO₂ with N-methyldiethanolamine in aqueous solutions”. International journal of chemical kinetics. DOI 10.1002/kin.20375. (2008). [Google Scholar]

[2] IMTP packing specification detail. “www.chemicalpackings.com/category/news/IMTPpacking-specificationdetail”. Accessed Apr 23_rd 2018. (2016). [Google Scholar]

[3] Kakusaburo Onda. “Mass transfer coefficients between gas and liquid phases in packed columns”. Journal of chemical engineering of Japan. vol 1 no 1. (1968). [Google Scholar]

[4] Muharam, Y., Kusrini, E., Saubryani, N., Ulfa, M., “Simulation of a Metal Organic Framework-based Adsorbed Natural Gas Storage Tank”. International Journal of Technology, Volume 2, pp. 412–421. (2018). [CrossRef] [Google Scholar]

[5] Reinhard Billet. “Packed towers in processing and environmental technology”. VCH Verlagsgesellschaft mbH Weinheim. (1995). [Google Scholar]

[6] Separation columns (distillation, absorbtion. and extraction). chemical engineering. ”Onda's method“. page 601–602. [Google Scholar]

[7] Steven Jan Martin De Rijke. “CO₂ Removal by amine absorption and condensed rotational separation: energy consumption and equipment sizing”. Department of mechanical engineering. Technical university eindhoven. (2012). [Google Scholar]