• Title/Summary/Keyword: TIPA (triisopropanolamine)

Search Result 1, Processing Time 0.018 seconds

Absorption and Regeneration of Carbon Dioxide in Aqueous AMP + AEPD and AMP + TIPA Solutions (AMP + AEPD와 AMP + TIPA 수용액을 이용한 이산화탄소의 흡수 및 재생)

  • Kim, Mi-Sook;Choi, Won-Joon;Seo, Jong-Beom;Cho, Ki-Chul;Kim, Soo-Gon;Oh, Kwang-Joong
    • Journal of Korean Society for Atmospheric Environment
    • /
    • v.23 no.5
    • /
    • pp.539-546
    • /
    • 2007
  • Increasing emission of $CO_2$ significantly effects the global warming. Chemical absorption is one of separation methods of $CO_2$ from the industrial flue gases. In this study, the $CO_2$ removal efficiency as well as the $CO_2$ absorption amount of aqueous AMP (2-amino-2-methyl-1-propanol) solutions were measured using the continuous absorption and regeneration apparatus. We investigated the effect of aqueous AMP+AEPD(2-amino-2-ethyl-1, 3-propanediol) and AMP+TIPA (triisopropanolamine) solutions to enhance absorption characteristics of AMP. As a result of this study, the absorption amount and $CO_2$ removal efficiency were increased with adding TIPA into 30 wt.% AMP. The absorption amount and $CO_2$ removal efficiency of aqueous 30 wt.% AMP+5 wt.% TIPA solution were $1.70\;kg-CO_2/kg-absorbent$ and 91.1%, while those of aqueous 30 wt.% AMP solution were $1.58\;kg-CO_2/kg-absorbent$ and 89.3%. In addition, aqueous 30 wt.% AMP+5 wt.% TIPA solution used in the study revealed the high stripping efficiency, which was almost 98%, at the temperature of $110^{\circ}C$. Thus, the temperature of regenerator should be operated at $110^{\circ}C$.