Abstract
Background: The use of an amine solution to capture CO2 from flue gases is one of the
methods applied commercially to clean up the exhaust gas stream of a power plant. One of the
issues in this process is foaming which should be known in order to select a suitable amine for
design.
Objectives: In this work, all possible types of amines used for CO2 capture, namely, alkanolamines,
sterically hindered alkanolamines, multi-alkylamines and cyclic amines, were investigated to elucidate
their chemical structure–foaming relationships.
Methods: Foam volume produced by each type of 2M amine solution with its equilibrium CO2
loading was measured at 40°C using 94 mL/min of N2 flow.
Results: Amines with a higher number or a longer chain of the alkyl group exhibited higher foam
volume because of alkyl group’s ability to decrease the surface tension while increasing the viscosity
of the solution. An increase in the number of hydroxyl or amino groups in the amine led to the
reduction of foam formation due to the increase in surface tension and a decrease in viscosity of the
solution. The predictive foam models for non-cyclic and cyclic-amines developed based on the
structural variations, surface tension and viscosity of 29 amines predicted the foam volume very
well with average absolute deviations (AAD) of 12.7 and 0.001%, respectively. The model accurately
predicted the foam volume of BDEA, which was not used in model development with 13.3
%AD.
Conclusion: This foam model is, therefore, indispensable in selecting a suitable amine for an
amine-based CO2 capture plant design and operation.
Keywords:
Foam, CO2 absorption, amine structure, prediction model, mine-based CO2 and surface tension.
Graphical Abstract
[1]
Metz B, Davidson O, Bosch P, Dave R, Meyer L. Climate change 2007: Mitigation: contribution of working group III to the fourth assessment report of the intergovernmental panel on climate change: Summary for policymakers and technical summary. Cambridge University Press 2007.
[2]
International Energy Agency (IEA). CO2 emission from fuel combustion 2019: Overview. OECD/IEA 2019.
[8]
Gondule YA, Dhenge SD, Motghare K. Control of foam formation in the amine gas treating system. IARJSET 2017; 4(4): 183-8.
[19]
von Phul SA. Control of foaming in amine systems, D-foam incorporated, MPR services, Inc. TX, USA: Dickinson 2007.
[20]
Thomason J. Reclaim gas treating solvent. Hydrocarbon Process 1985; 64(4): 75-8.
[21]
Pauley CR. Face the facts about amine foaming. Chem Eng Prog 1991; 87(1): 33-8.
[22]
Stewart EJ, Lanning RA. Reduce amine plant solvent losses Part1. Hydrocarbon Process 1994; 73(5): 67-81.
[23]
Abdi MA, Golkar MM, Meisen A. Improve contaminant control in amine systems. Hydrocarbon Process 2001; 80(10): 102C-I.
[29]
Nivaldo JT. Chemistry: A Molecular Approach. 4th ed. Boston: Pearson 2017.
[30]
Al Dhafeeri MA. Identifyng sources key to detailed troubleshooting of amine foaming. Oil Gas J 2007; 105(32): 56-67.
[31]
Walstra P. Principle of foam formation and stability. In: Wilson A, EdFoams: Physics, chemistry and structure. Berlin, Heidelberg: Springer-Verlag 1989; pp. 1-15.
[32]
Adamson AW, Gast AP. Physical chemistry of surfaces. 6th ed. New York: John Wiley and Sons 1997.
[33]
Horwitz W. Association of Official Analytical Chemists (AOAC). Menasha, WI: Methods George Banta Company 1975.
[34]
American Society for Testing and Materials (ASTM) ASTM D892-standard test method for foaming characteristics of lubricating oil. West Conshohocken, PA: ASTM 1999.
[38]
Gooch JW. Surface tension and hansen solubility parameters. In: Gooch JW, Ed. Encyclopedic Dictionary of Polymers. New York: Springer 2011.