Open Access
Numéro
Oil & Gas Science and Technology - Rev. IFP Energies nouvelles
Volume 73, 2018
Numéro d'article 19
Nombre de pages 10
DOI https://doi.org/10.2516/ogst/2018015
Publié en ligne 5 juin 2018
  • Aleixo M., Prigent M., Gibert A., Porcheron F., Mokbel I., Joseb J., Jacquin M. (2011) Physical and chemical properties of DMXTM solvents, Energy Procedia 4, 148–155. [Google Scholar]
  • Al-Ghawas H.A., Hagewiesch D., Ruiz-Ibanez G., Sandall O. (1989) Physicochemical properties important for carbon dioxide absorption in aqueous methyldiethanolamine, J. Chem. Eng. Data. 34, 385–391. [Google Scholar]
  • Amann J.-M.G., Bouallou C. (2009) Kinetics of the absorption of CO2 in aqueous solution of N-methyldiethanolamine + triethylenetetramine, Ind. Eng. Chem. Res. 48, 3761–3770. [Google Scholar]
  • Amrarene F., Bouallou C. (2004) Kinetics of carbonyl sulfide (COS) absorption withaqueous solution of diethanolamine and methyldiethanolamine, Ind. Eng. Chem. Res. 43, 6136–6141. [Google Scholar]
  • Aroua M.K., Haji-Sulaiman M.Z., Ramasamy K. (2002) Modelling of carbon dioxideabsorption in aqueous solutions of AMP and MDEA and their blends using Aspen plus, Sep. Purif. Technol. 29, 153. [Google Scholar]
  • Bashipour F., Rahimi A., Nouri Khorasani S., Naderinik A. (2017) Experimental optimization and modeling of sodium sulfide production from H2S-rich off-gas via response surface methodology and artificial neural network, Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles 72, 9. [Google Scholar]
  • Bosoaga A., Masek O., Oakey J.E. (2009) CO2 capture technologies for cement industry, Energy Procedia 1, 133–140. [Google Scholar]
  • Bishnoi S., Rochelle G.T. (2002) Thermodynamics of piperazine/methyldiethanolamine/water/carbon dioxide, Ind. Eng. Chem. Res. 41, 604–612. [Google Scholar]
  • Cadours R., Bouallou C. (1998) Rigorous simulation of gas absorption into aqueous solutions, Ind. Eng. Chem. Res. 37, 1063–1070. [Google Scholar]
  • IEA Greenhouse gas R and D Programme. (2008) CO2 capture in the cement industry, 2008/3, July 2008. [Google Scholar]
  • Intergovernmental Panel on Climate Change. (IPCC, 2013). [Google Scholar]
  • Kanniche M., Gros-Bonnivard R., Jaud Ph., Valle-Marcos J., Amann J.-M., Bouallou C. (2010) Precombustion, postcombustion and oxycombustion in thermal power plant for CO2 capture, Appl. Therm. Eng. 30, 53–62. [Google Scholar]
  • Knuutila H.K., Nannestad A. (2017) Effect of the concentration of MAPA on the heat of absorption of CO2 and on the cyclic capacity in DEEA-MAPA blends, Int. J. Greenh. Gas Control. 61, 94–103. [CrossRef] [Google Scholar]
  • Lecomte F., Broutin P., Lebas E. (2009) Le captage du CO2 des technologies pour réduire les Émissions de gaz à effet de serre, Édition technip, IFP publication. [Google Scholar]
  • Mehassouel A., Derriche R., Bouallou C. (2016) A new CO2 absorption data for aqueous solutions of N-methyldiethanolamine + hexylamine, Chem. Eng.Trans. 52, 595–600. [Google Scholar]
  • Mudhasakul S., Ku H.M., Douglas P.L. (2013) A simulation model of a CO2 absorption process with methyldiethanolamine solvent and piperazine as an activator, Int. J. Greenh. Gas Control. 15, 134–141. [CrossRef] [Google Scholar]
  • Nazmul H.S.M. (2005) Techno-Economic study of CO2 captures process for cement plants, Master thesis, University of Waterloo, Ontario, Canada. [Google Scholar]
  • Passalacqua R., Centi G., Perathoner S. (2015) Solar production of fuels from water and Co2: Perspectives and opportunities for a sustainable use of renewable energy, Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles 70, 799–815. [CrossRef] [Google Scholar]
  • Paul S., Ghoshal A.K., Mandal B. (2009) Kinetics of absorption of carbon dioxide into aqueous blends of 2-(1-piprazinyl)-ethylamine and N-methyldiethanolamine, Chem. Eng. Sci. 64, 1618–1622. [Google Scholar]
  • Pinto D.D.D., Monteiro J.G.M.-S., Bersas A., Haug-Warberg T., Svendsen H.F. (2013) eNRTL parameter fitting procedure for blended amine systems: MDEA-PZ case study, Energy Procedia 37, 1613–1620. [Google Scholar]
  • Raynal L., Alix P., Bouillon P.A., Gomez A., de Nailly M.F., Jacquin M., Kittel J., di Lella A., Mougin P., Trapy J. (2011a) The DMX™ process: An original solution for lowering the cost of post-combustion carbon capture, Energy Procedia 4, 779–786. [Google Scholar]
  • Raynal L., Bouillon P.A., Gomez A., Broutin P. (2011b) From MEA to demixing solvents and future steps, a roadmap for lowering the cost of post-combustion carbon capture, Chem. Eng. J. 171, 742–752. [Google Scholar]
  • Sharifi A., Omidbakhsh A.E. (2017) Effect of the tower type on the gas sweetening process, Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles 72, 24. [Google Scholar]
  • Tan M. Sc. (2010) Study of CO2 absorption into thermomorphic lipophilic amine solvents, Ph.D. Dissertation, University of Dortmund, Germany. [Google Scholar]
  • Toro-Molina C., Bouallou C. (2013) Kinetics study and simulation of CO2 absorption into mixed aqueous solutions of methyldiethanolamine and diethanolamine, Chem. Eng. Trans. 35, 319–324. [Google Scholar]
  • Tursunov O., Kustov L., Kustov A. (2017) A brief review of carbon dioxide hydrogenation to methanol over copper and iron based catalysts, Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles 72, 30. [Google Scholar]
  • Wang L., An S., Li Q., Yu S., Wu S. (2017) Phase change behavior and kinetics of CO2 absorption into DMBA/DEEA solution in a wetted-wall column, Chem. Eng. J. 314, 681–687. [Google Scholar]
  • Whitman W.G. (1923) Preliminary confirmation of the two-film theory of gas absorption, Chem. Met. Eng. 29, 146–148. [Google Scholar]
  • Xu Z., Wang S., Liu S., Chen C. (2012) Solvent with low critical solution temperature for CO2 capture, Energy Procedia 23, 64–71. [Google Scholar]
  • Xu Z., Shujuan W., Bo Z., Changhe C. (2013) Study on potential biphasic solvents: Absorption capacity, CO2 loading and reaction rate, Energy Procedia 37, 494–498. [Google Scholar]
  • Ye Q., Wang X., Lu Y. (2015) Screening and evaluation of novel biphasic solvents for energy-efficient post-combustion CO2 capture, Int. J. Greenh. Gas Control. 39, 205–214. [CrossRef] [Google Scholar]
  • Ye Q., Zhu L., Wang X., Lu Y. (2017) On the mechanisms of CO2 absorption and desorption with phase transitional solvents, Int. J. Greenh. Gas Control. 56, 278–288. [CrossRef] [Google Scholar]
  • Zhang J., Nwani O., Tan Y., Agar D.W. (2011) Carbon dioxide absorption into biphasic amine solvent with solvent loss reduction, Chem. Eng. Res. Des. 89, 1190–1196. [Google Scholar]
  • Zhang J., Qiao Y., Agar D.W. (2012a) Improvement of lipophilic-amine-basedthermomorphic biphasic solvent for energy-efficient carbon capture, Energy Procedia 23, 92–101. [Google Scholar]
  • Zhang J., Qiao Y., Agar D.W. (2012b) Intensification of low temperature thermomorphic biphasic amine solvent regeneration for CO2 capture, Chem. Eng. Res. Des. 90, 743–749. [Google Scholar]
  • Zhang J., Qiao Y., Wang W., Misch R., Hussain K., Agar D.W. (2013) Development of an energy efficient CO2 capture process using thermomorphic biphasic solvents, Energy Procedia 37, 1254–1261. [Google Scholar]
  • Zoghi A.T., Feyzi F., Zarrinpashneh S. (2012) Experimental investigation on the effect of addition of amine activators to aqueous solutions of N-methyldiethanolamine on the rate of carbon dioxide absorption, Int. J. Greenh. Gas Control. 7, 12–19. [CrossRef] [Google Scholar]

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