Scalable and Highly Porous Membrane Adsorbents for Direct Air Capture of CO2

被引:3
作者
Tran, Thien [1 ,2 ,3 ]
Singh, Shweta [1 ]
Cheng, Shiwang [4 ]
Lin, Haiqing [1 ]
机构
[1] SUNY Buffalo, Dept Chem & Biol Engn, Buffalo, NY 14260 USA
[2] US DOE, Natl Energy Technol Lab, Pittsburgh, PA 15236 USA
[3] NETL Support Contractor, Pittsburgh, PA 15236 USA
[4] Michigan State Univ, Dept Chem Engn & Mat Sci, E Lansing, MI 48824 USA
基金
美国国家科学基金会;
关键词
direct air capture; polyethylenimine; membraneadsorbent; CO2; sorption; porous support; TEMPERATURE; SEPARATION; PEI; DYNAMICS;
D O I
10.1021/acsami.4c02873
中图分类号
TB3 [工程材料学];
学科分类号
0805 ; 080502 ;
摘要
Direct air capture (DAC) of CO2 is a carbon-negative technology to mitigate carbon emissions, and it requires low-cost sorbents with high CO2 sorption capacity that can be easily manufactured on a large scale. In this work, we develop highly porous membrane adsorbents comprising branched polyethylenimine (PEI) impregnated in low-cost, porous Solupor supports. The effect of the PEI molecular mass and loading on the physical properties of the adsorbents is evaluated, including porosity, degradation temperature, glass transition temperature, and CO(2 )permeance. CO2 capture from simulated air containing 400 ppm of CO2 in these sorbents is thoroughly investigated as a function of temperature and relative humidity (RH). Polymer dynamics was examined using differential scanning calorimetry (DSC) and broadband dielectric spectroscopy (BDS), showing that CO2 sorption is limited by its diffusion in these PEI-based sorbents. A membrane adsorbent containing 48 mass% PEI (800 Da) with a porosity of 72% exhibits a CO2 sorption capacity of 1.2 mmol/g at 25 C-degrees and RH of 30%, comparable to the state-of-the-art adsorbents. Multicycles of sorption and desorption were performed to determine their regenerability, stability, and potential for practical applications.
引用
收藏
页码:22715 / 22723
页数:9
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