Alkanolamines are widely used in the purification of the sour gas sweetening process. During the sour gas absorption process
CO
2
significantly degrades the amine solvent and creates enormous problems for plant operation. In this work
CO
2
induced degradation of aqueous diethanolamine (DEA) solution was conducted in a 1.25 L jacketed glass reactor that functioned as an absorber and stripper at atmospheric conditions. Pure CO
2
was bubbled through the reactor until the solution became saturated. In this study
the concentrations of DEA used were in the range of concentrations between 2 mol·L
-1
and 4 mol·L
-1
. In the degradation experiment
six generic cycles were conducted for each run. Each cycle was configured with the absorption and desorption of carbon dioxide at 55℃ and 100℃
respectively. Samples were collected after a predetermined experimental time and analyzed by ion chromatography (IC) to identify unknown ionic degradation products (DGPs). In the IC analysis
three different columns were used for anion
cation and ion exclusion systems
which are Metrosep A Supp 5 150/4.0
Metrosep C Supp 4 150/4.0 and Metrosep Organic Acids
respec
tively. The major identified DGPs of D01DEA2M
D02DEA3M
and D03DEA4M are nitrite
acetate and ammonium. Phosphate product was found in the degraded amine samples which might be due to the contamination of water or chromatographic system.
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Thermal degradation of diethanolamine at stripper condition for CO2 capture: Product types and reaction mechanisms
Understanding temperature-dependent degradation in proton exchange membrane water electrolyzer: The critical role of porous transport layer
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Microbubble-based chemical process intensification: A review
Synthesis of magnetically separable and recyclable MnFe2O4@SiO2@NH2 nanocomposite coupled-acylated MWCNTS with enhanced photocatalytic performance under visible-light irradiation
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