No abstract

To achieve carbon peaking and carbon neutrality goals, the chemical absorption method is the most widely used and mature carbon capture technology. In this method, organic amine solution is a commonly used absorbent for CO2 absorption. Biphasic solvents have been designed due to their significant advantages in reducing energy consumption for regeneration, and the development of new and efficient biphasic solvents has become the current research focus. The CO2 absorption performance of absorbents with different ratios of triethylenetetramine (TETA) and 1-diethylamino-2-propanol (1DMA2P) was investigated by the bubbling absorption method, and it was found that the absorbent of 2 mol/L TETA + 2 mol/L 1DMA2P biphasic solvent showed the best performance. The volume of the rich phase after CO2 absorption by the absorbent was 20% lower than that of the ethanolamine (MEA) solution, and the CO2 absorption loading was as high as 0.656 mol CO2/mol of total amine. The absorption temperature had little effect on absorption performance and the absorbent had a lower rich-phase volume and better absorption performance when the total amine concentration was 4 mol/L, and the optimum desorption temperature was 393.15 K. Meanwhile, the material composition was characterized by 13C NMR. It could be concluded that the biphasic solvent generated carbamate and protonated amine after absorbing CO2, and the reaction product was mainly concentrated in the lower layer of the phase separation.