Chinese Science Citation Database Core Library(CSCD)Source Journals
Chinese Core Journals
Chinese Core Science and Technology Journals
RCCSE China Authoritative Academic Journal(A+)
Dutch Digest and Citation Database (Scopus)

Selection of MDEA based phase change absorbers and carbondioxide capture performance

2024 No. 06
377
101
OnlineView
Download
Authors:
HU Yanlong
WANG Qiang
HU Dingkai
ZHANG Yingshuang
CHEN Yali
LU Shijian
Unit:
School of Chemical Engineering,Xinjiang University
School of Chemical Engineering,China University of Mining and Technology
Abstract:

To achieve the purpose of rapid screening of phase change absorbent, a new phase change absorbent-MDEA/ polyethylene glycoldimethyl ether (NHD) / H2O was quickly screened with N-methyl diethanolamine (MDEA) as the main absorbent, organic solvent as thephase separation accelerator and water as the solvent, guided by the theory of Hansen solubility parameter. The thermal stability of thephase change absorbent was tested by thermogravimetric analysis ( TGA), and the CO2 absorption and desorption performance of thephase change absorbent was investigated by CO2 absorption and desorption experiments, as well as the recycling ability.1HNMR was usedto test the distribution of the substances before and after the phase change. The results show that MDEA/ NHD/ H2O phase change absorbent has the highest thermal stability compared with 30% ethanolamine (MEA) absorbent and MDEA/ n-butanol/ H2O phase change absorbent reported in the literature. NHD as a phase separation accelerator can promote the dissolution of CO2 in the phase transition absorbent, MDEA/ NHD/ H2O phase transition absorbent liquid-liquid phase separation requires the coexistence of NHD and H2O. At the absorption temperature of 25 ℃ , the MDEA/ NHD/ H2O phase change absorbent with a mass ratio of 3 ∶ 5 ∶ 2 has the highest CO2 absorption capacity of 1.069 5 mol/ L. The phase change absorbent developed in this paper can reduce the volume of desorption liquid sent to thedesorption unit to 42%. The CO2 desorption efficiency reached 98.96% at a desorption temperature of 90 ℃ . The total CO2 cycling capacity of MDEA/ NHD/ H2O phase change absorbent with a mass ratio of 3 ∶ 5 ∶ 2 was 9.260 4 mol/ L after 10 cycles of absorption at 25 ℃and thermal desorption at 90 ℃ . Compared with 30% MEA absorbent, 30% MDEA absorbent and MDEA/ n-butanol / H2O phase changeabsorbent, it has the highest CO2 cycling capacity. The 1HNMR test results showed that the upper liquid phase of the phase change absorbent was mainly composed of NHD, which was a CO2-lean phase. The lower liquid phase is mainly composed of MDEA and MDEAH+,which is a CO2-rich phase.

Keywords:
phase change absorbent
CO2 absorption capacity
Hansen solubility parameter
CO2 cycle capacity
CO2 desorption efficiency
Citation format:
胡彦陇(1997—),男,陕西汉中人,硕士研究生。E-mail:1550653862@qq.com
Chart:
Articles:
--
Citation format:
HU Yanlong,WANG Qiang,HU Dingkai,et al.Selection of MDEA based phase change absorbers and carbon dioxide capture performance[J].Clean Coal Technology,2024,30(6):158-170.

About Journal

  • Executive director

    China Coal Science and Industry Group Co., Ltd

  • Sponsored by

    Coal Science Research Institute Co., Ltd
    Coal Industry Clean Coal Engineering
    Technology Research Center

  • Editor in Chief

    XIE Qiang

  • Vice Editor-in-Chief

    YU Chang
    SHI Yixiang
    ZHAO Yongchun
    DUAN Linbo
    CAO Jingpei
    ZENG Jie

  • Publication Frequencies

    Monthly

  • ISSN

    1006-6772

  • CN

    11-3676/TD

Covered by

  • CSTPCD
  • RCCSE(A+)
  • AJ
  • EBSCO host
  • Ulrichsweb
  • JST
  • Scopus

Contact us

New Media

  • Meichuanmei
    Meichuanmei
  • Clean Coal Technology
    Clean Coal Technology
  • Online Journals
    Online Journals
Website Copyright © {year} Clean Coal Technology
京ICP备05086979号-19
地址:Coal Tower, Hepingli, Chaoyang District, Beijing, China.
邮编:100013
Tel:86-10-87986452 / 010-87986451
E-mail:jjmjs@263.net