Muhammad Zubair Shahid , Ahmad Salam Farooqi , Mohammad Mozahar Hossain , Usama Ahmed , Medhat A. Nemitallah
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引用次数: 0
Abstract
The CO2 sorption-enhanced water gas shift reaction (SE-WGSR) is a promising approach that facilitates in-situ CO2 capture and promotes hydrogen yields by shifting the equilibrium of the WGSR towards higher CO conversion. Developing an effective sorbent/catalyst is one of the key challenges for industrial-scale applications of SE-WGSR technology. The present study investigated mixed CaO/MgO as a sorbent material for an SE-WGSR process. The performances of the SE-WGSR with various concentrations of CaO/MgO mixtures were analyzed by using the Gibbs free energy minimization method. The ultimate objective was to secure a high CO conversion and a low energy requirement for sorbent regeneration. The results showed that the increasing CaO in the CaO/MgO mixture significantly increased the CO conversion, while the increase in MgO decreased the total sorbent regeneration enthalpy. A CaO/MgO mixture of 20 mol % CaO was identified as the optimal sorbent composition, achieving a 29.3 % higher CO conversion in comparison to 100 % MgO sorbent at 40 bar pressure and 350 °C, requiring 14.1 % less regeneration enthalpy than a 100 mol % CaO sorbent. Therefore, the optimal sorbent mixture composition can result in the realization of an efficient SE-WGS process to achieve high CO conversion at the appropriate regeneration energy cost.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.