(48g) CA@ZIF-L-Stabilized Pickering Interfacial Catalytic System for Efficient CO2 Conversion | AIChE

(48g) CA@ZIF-L-Stabilized Pickering Interfacial Catalytic System for Efficient CO2 Conversion

Authors 

Shi, J. - Presenter, Tianjin University
Zhao, Y., Tianjin University
Chen, Y., Tianjin University
Wang, X., Tianjin University
Sun, Y., Tianjin University
Enzymatic catalysis offers a green and potent alternative for efficient CO2 conversion due to its high selectivity and specificity, high efficiency, and mild operational conditions. Carbonic anhydrase (CA) enzyme-based absorption technology for CO2 capture has been intensively investigated. The main issue related to this method is the activity, stability and reusability of the CA enzyme in vitro. To address this issue, CA@ZIF-L-stabilized Pickering interfacial catalytic system was constructed. In detail, CA enzymes were embedded into zeolitic imidazolate framework-L (ZIF-L) particles through biomimetic crystallization. The as-synthesized CA@ZIF-L particles were then spontaneously assembled into capsule at the interface between the oil phase (hexadecane) and water phase during the formation of Pickering emulsions. CA@ZIF-L-stabilized Pickering interfacial catalytic system was finally constructed to convert CO2 to bicarbonates. The performance of the system was evaluated by adding calcium ions to form calcium carbonate.

The results showed that CA could rapidly initiate the crystallization of ZIF-L to form CA@ZIF-L particles under mild aqueous conditions. The immobilization efficiency of CA could be above 90%. The synthesized CA@ZIF-L, which was served as a solid emulsifier to stabilize Pickering emulsion with its self-assembly properties at the oil-water interface, exhibited excellent catalytic activity in Pickering interfacial reaction and the corresponding cyclic performance. In detail, CA@ZIF-L-stabilized Pickering interfacial catalytic system exhibited higher catalytic efficiency than that of free CA@ZIF-L mainly because of the shortened diffusion path of CO2 from gas phase to enzyme active center. The production rate of CaCO3 through Pickering interfacial catalysis reached 2.73 mg min-1, which is 1.14 times higher than free CA@ZIF-L. In the cycling experiment, about 96.2% of conversion efficiency could be retained for our system after 6 times recycling. These findings above implies that the system we constructed exhibits high activity and stability, particularly, superior recyclability for conversion of CO2 into CaCO3.

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