Abstract
A primary focus among researchers is to reduce the energy required for CO2 capture. Here, we report a system designed to capture CO2 while simultaneously generating electricity. The reaction heat of amine-CO2 in the point-source CO2-capture process is harvested. Amine-functionalized mixtures (TEPA-SBA/MEA+PZ) exhibit 52% higher reaction enthalpy compared to primary amine absorbents. A membrane composed of tetraethylenepentamine-impregnated poly(ethylene glycol) dimethacrylate is employed, which selectively permeates CO2 and minimizes heat loss by separating the flue gas channel and solvent reservoir. CO2 working capacity of TEPA-SBA/MEA+PZ is 6.6 mmol/g under steady-state conditions of 15 mol % CO2/N2. Electricity can be harvested at a rate of 7.5 kJ/kg, and direct utilization of thermal energy yields 445 kJ/kg (net thermal energy consumption is 2.2 MJ/kg). While the proposed system has the potential to reduce CO2 emissions from power plants to 0.25 ton/MWh and increase total electricity production by 0.6%, addressing device energy penalties remains a significant challenge.
Original language | English |
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Article number | 101698 |
Journal | Cell Reports Physical Science |
Volume | 4 |
Issue number | 12 |
DOIs | |
Publication status | Published - 2023 Dec 20 |
Bibliographical note
Publisher Copyright:© 2023 The Author(s)
Keywords
- amine-functionalized solvent
- energy optimization
- hybrid energy harvesting
- membrane reactor
- point-source CO capture
ASJC Scopus subject areas
- General Chemistry
- General Materials Science
- General Engineering
- General Energy
- General Physics and Astronomy