Abstract
Detailed experimental data, including temperature profiles over the absorber, for a carbon dioxide (CO 2) absorber with structured packing in an integrated laboratory pilot plant using an aqueous 2-amino-2-methyl-1-propanol (AMP) solution are presented. The experimental gas–liquid material balance was within an average of 3.5% for the experimental conditions presented. A predictive rate-based steady-state model for CO 2 absorption into an AMP solution, using an implicit expression for the enhancement factor, has been validated against the presented pilot plant data. Furthermore, a parameter sensitivity analysis for the proposed model has been carried out.
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