Experimental and simulation study of a catalytic-membrane integrated system for efficient CO2 stripping

• Boosted regeneration of CO 2 -rich amines solutions using a catalytic-membrane integrated system for efficient CO 2 capture. • Catalytic integration increased the stripping efficiency of hollow fiber membrane modules from 53 % to 72 % at 80 °C. • Increasing liquid flow rates from 20 mL/min to 100 mL/min improved the CO 2 removal efficiency of catalytically assisted systems from 48 % to 65 %. • Additionally, a mathematical model aligned well with experimental results for self-fabricated membrane module is developed. Global warming, mainly caused by carbon dioxide (CO 2 ) emissions, is rapidly becoming a serious concern. The Carbon Capture, Utilization, and Storage (CCUS) process, particularly the amine-based absorption process, is among the most developed industrial processes for capturing CO 2 from anthropogenic and natural sources. However, the energy-intensive nature of the equipment, as well as its high capital cost, inhibits widespread application. A porous hollow fiber membrane contactor (HFMC) is considered a promising technique for solvent regeneration in CO 2 capture applications. Recent research on catalyst-assisted solvent regeneration has also shown that nano catalytic materials can reduce solvent regeneration energy costs while increasing CO 2 desorption. Therefore, a self-fabricated gas-liquid membrane contactor (GLMC) module integrated with catalytically promoted CO 2 desorption to maximize their potential for solvent regeneration is used in this paper. A polytetrafluoroethylene (PTFE) hollow fiber membrane module combined with and without catalytic stripping is tested for CO 2 stripping performance under varying gas-liquid flowrates, temperatures, and initial CO 2 loading concentrations. Increasing the liquid phase temperature and liquid flowrate significantly improved CO 2 stripping, whereas increasing the gas flowrate did not increase stripping flux as much. Adding nanomaterial increased the stripping efficiency of membrane modules from 53 % to 72 % at 80 °C during CO 2 stripping experiments. Catalytically assisted systems exhibited improved stripping efficiency from 48 % to 65 % when liquid flow rates were increased from 20 mL/min to 100 mL/min. A mathematical model for the fabricated module is developed for CO 2 stripping from rich ethanolamine (MEA) solutions and it is simulated using COMSOL. Model predictions align well with experimental data outcomes.