A mixture of 2-(2-aminoethylamine)ethanol (AEEA) with benzyl alcohol (BP) as absorbent was developed to reduce energy consumption in an amine-based CO 2 capture process. The solubility of CO 2 in the AEEA + BP solution was compared with AEEA + diethylene glycol (DEG), AEEA + triethylene glycol (TEG), and AEEA + H 2 O. The CO 2 loading (mol CO 2 /kg amine) at the same CO 2 partial pressure was in the order AEEA + H 2 O > AEEA + BP > AEEA + TEG > AEEA + DEG, and CO 2 loading of all these solutions increased with increasing vapor pressure of CO 2 . Besides, the CO 2 loading in AEEA + BP solution significantly decreased with increasing reaction temperature. The desorption rate of AEEA + BP solution was about 1.3 times faster than that of aqueous AEEA solution at the same desorption temperature, and AEEA + BP solution needed 30% time less than AEEA + H 2 O solution to reach reaction end point. The AEEA + BP solution showed stable repeatability in four cycles of absorption−desorption tests.
INTRODUCTIONCO 2 capture technology in postcombustion continues to be one of the attractive options for the reduction of CO 2 emissions from the fossil fuel combustion process, particularly coal-fired power plants. Among the applicable CO 2 removal processes, chemical absorption using aqueous alkanolamine solutions is the most effective method. 1 The major aqueous alkanolamine solutions applied in the industrial process are monoethanolamine (MEA), diethanolamine (DEA), diglycolamine (DGA), N-methyldiethanolamine (MDEA), and 2-amino-2-methyl-1-propanol (AMP). Recently, attention has been paid to diamines which present a higher absorption capacity than primary and secondary alkanolamines. 2−5 Among them, aqueous 2-(2-aminoethylamine)ethanol (AEEA) solutions (5 to 25) wt % have a CO 2 capacity of (1.35 to 1.12) mol CO 2 /mol amine at 296 K and atmospheric pressure. 2,3 In the modern industry, the heat of regeneration for the stripping out of CO 2 from rich amine solutions in a regeneration process, which consists of sensible heat, reaction heat, latent heat of partial water, and partial latent heat of solvent vaporization, contributes (50 to 80) % of the total energy consumption in a chemical solvent based on the CO 2 separation process. 6 Many researchers have used blended amines, a solution of two or more amines in a variety of compositions, to improve absorption or desorption ability. 7,8 However, regardless of what the compositions of solutions are, the high sensible heat, and the latent heat of water vaporization will inevitably consume excessive energy in the regeneration process. During the regeneration process, a large amount of sensible heat is first utilized to increase the solution temperature to the stripping temperature because of the specific heat capacity of the aqueous solution. Meanwhile,