Kinetic characterization of carbonic anhydrase immobilized on magnetic nanoparticles as biocatalyst for CO2 capture

被引:27
作者
Peirce, S. [1 ]
Russo, M. E. [2 ]
Perfetto, R. [3 ]
Capasso, C. [3 ]
Rossi, M. [3 ]
Fernandez-Lafuente, R. [4 ]
Salatino, P. [1 ]
Marzocchella, A. [1 ]
机构
[1] Univ Napoli Federico 11, Dipartimento Ingn Chim Mat & Prod Ind, Ple V Tecchio 80, I-80125 Naples, Italy
[2] CNR, Ist Ric Sulla Combust, Ple V Tecchio 80, I-80125 Naples, Italy
[3] CNR, Ist Biosci & Biorisorse, Via P Castellino 111, I-80131 Naples, Italy
[4] CSIC, Inst Catalisis & Petroquim, E-28049 Madrid, Spain
关键词
CO2; capture; Carbonic anhydrase; Immobilized enzyme; Reactive absorption; ENZYME IMMOBILIZATION; BICARBONATE SOLUTIONS; GAS-ABSORPTION; STABILITY; DIOXIDE; TEMPERATURE; STRATEGIES; HYDRATION; SOLVENTS; REMOVAL;
D O I
10.1016/j.bej.2018.06.017
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Carbon dioxide absorption into carbonate solutions promoted by the enzyme carbonic anhydrase (CA, E.C. 4.2.1.1) has been proposed as potential technology for CO2 capture. The use of solid CA-based biocatalysts allows the enzyme recovery and reuse under continuous operating conditions typical of industrial applications. The present study regards the development and the kinetic characterization of a solid CA based biocatalyst to be used in CO2 capture processes based on reactive absorption. A technical grade thermostable CA was immobilized by covalent bonding on aminated paramagnetic Fe3O4 nanoparticles via carbodiimide activation of the enzyme. The effective covalent binding of the enzyme on the support was verified in the alkaline carbonate solution used as solvent for CO2 absorption tests. The kinetics of the biocatalyst were assessed by means of CO2 absorption tests in a stirred cell reactor. The liquid solvents used in the CO2 absorption tests were 0.5 M Na2CO3/NaHCO3 buffer (pH 9.6) at 298 and 313 degrees K and 10% wt/wt K2CO3 solutions at different carbonate conversion degrees (0-40%). The Danckwerts' theory for gas-liquid reactive absorption was applied to assess the intrinsic second order kinetic constant k(cat)/K-M for the CO2 hydration reaction catalyzed by the immobilized CA. Results pointed out that k(cat)/K-M ranged between 102 and 103 m3.kg(-1).s(-1) and that it increased with the temperature and with the decrease of carbonate conversion degree. (C) 2018 Elsevier B.V. All rights reserved.
引用
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页码:1 / 11
页数:11
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