微型反应器
碳酸酐酶
传质
化学
吸收(声学)
固定化酶
化学工程
色谱法
有机化学
酶
催化作用
材料科学
工程类
复合材料
作者
Ion Iliuta,Hannaneh Rasouli,Maria C. Iliuta
标识
DOI:10.1016/j.seppur.2022.122590
摘要
• Green CO 2 capture with carbonic anhydrase immobilized in wall-coated microreactors. • Wall-coated enzyme-immobilized microreactor (WCEI_MR) allows for low enzyme loading. • Gas-liquid Taylor flow generates an enhanced enzyme-mediated CO 2 absorption process. • WCEI_MR allows long-term continuous operation at low pressure. • Promising approach for CO 2 capture when connected in small-scale modular systems. An intensified enzymatic CO 2 capture process in a wall-coated enzyme-immobilized microreactor (WCEI_MR) was investigated experimentally and numerically under diverse flow conditions, at different human carbonic anhydrase II (hCA II) enzyme and buffer concentrations, and using different buffers. The motivation for using this type of microreactor for the CO 2 capture process is to enhance the absorption rate by improving the flow and mass transfer through Taylor gas-liquid flow to efficiently accommodate the reduced time scales of CO 2 absorption associated with the CA enzyme. hCA II enzyme was covalently immobilized on the internal surface of experimental microreactor (priori amine-functionalized via polydopamine & polyethyleneimine co-deposition) through glutaraldehyde. An unsteady-state two-scale model involving volume-averaged continuity and momentum balance equations, mass transport/reaction in bulk liquid & gas, and diffusion/enzymatic reaction equations in immobilized-enzyme layer was developed to simulate the wall-coated enzyme-loaded microreactor. Gas-liquid two phase Taylor flow in wall-coated microreactor generates an intensified gas-liquid/liquid-solid mass transfer which, coupled with the large surface area and small axial dispersion and backmixing, enhances the utilization of the enormous hCA II enzyme turnover number and ensures an enhanced enzyme-mediated CO 2 absorption process at low pressure drop. WCEI_MR favors low enzyme concentrations, buffers with higher pKa 2 constant that generates higher driving force for CO 2 hydration or higher buffer concentration that improves enzymatic activity and the intermolecular proton-transfer step that stimulate the absorption process, all of which mitigate the impact of resistance to mass transfer. These findings suggest that WCEI_MR has a high potential for CO 2 absorption and, when connected in flexible small-scale modular parallel systems, could represent a promising approach for large-scale green CO 2 capture.
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