2015
DOI: 10.1039/c5tb00870k
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MOF-templated rough, ultrathin inorganic microcapsules for enzyme immobilization

Abstract: Ultrathin titania microcapsules with rough surfaces were prepared by using a metal-organic framework (ZIF-8) as one kind of hard template to mediate the structures of the microcapsule shell. Specifically, CaCO 3 particles were first coated with tannic acid (TA) followed by the deposition of hydrophobic ZIF-8 and another TA layer, the obtained particles were then assembled with protamine/TiO 2 bilayers through biomimetic mineralization. Finally, the microcapsules (Z-TiO 2 ) were obtained after simultaneously re… Show more

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Cited by 25 publications
(22 citation statements)
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“…We used 50 mM Ethylenediaminetetraacetic acid (EDTA) as a chelating agent for our positive control. [33] Furthermore two phosphate-citrate buffers at pH 5 and 6 were used and finally the cell medium DMEM at pH 7.4. After 5 days on a shaker at 150 rpm, the tubes were centrifuged and the supernatant was transferred into a new tube for further preparation steps.…”
Section: Atomic Absorption For the Measurement Of Zn 2+ Concentrationmentioning
confidence: 99%
“…We used 50 mM Ethylenediaminetetraacetic acid (EDTA) as a chelating agent for our positive control. [33] Furthermore two phosphate-citrate buffers at pH 5 and 6 were used and finally the cell medium DMEM at pH 7.4. After 5 days on a shaker at 150 rpm, the tubes were centrifuged and the supernatant was transferred into a new tube for further preparation steps.…”
Section: Atomic Absorption For the Measurement Of Zn 2+ Concentrationmentioning
confidence: 99%
“…It is known that the Michaelis–Menten equation is related to the rate of an enzyme‐catalyzed reaction to the concentration of substratesnormalRsi=normalrmaxnormalCsinormalKnormalm+normalCsiwhere R si (×10 −3 m s −1 ) is the initial enzyme‐catalyzed reaction rate in Pickering emulsion system, C si (×10 −3 m ) is the initial substrate concentration at the W/O interfaces, K m (×10 −3 m ) is the Michaelis–Menten constant, and r max (×10 −3 m s −1 ) is the maximum reaction rate in this system. Within the Pickering emulsion systems (which catalyze the oil‐soluble substrates at the W/O interfaces of emulsion droplets by enzymes in the aqueous system), the enzymatic reaction rate is also crucially depended on the diffusion of substrates from oil phase to the W/O interfaces . The diffusion rate equation is as followingnormalRsd=normalknormalGnormalSnormalg(normalCsonormalCsi)where R sd (×10 −3 m s −1 ) is the diffusion rate of substrates from oil phase to the W/O interfaces, k G (g s −1 m −2 ) is the mass transfer coefficient, and S g (m 2 g −1 ) is the specific surface area of the total Pickering emulsion droplets.…”
Section: Resultsmentioning
confidence: 99%
“…Subsequently, full removal of the CaCO3/ZIF-8 core could be achieved by treating the biocomposite with EDTA. 65 After the dissolution of the MOF template, PGA encapsulated in TiO2 retained activity, furthermore, the composite was reused eight times and showed higher activity than the same enzyme immobilized into silica-based monoliths. Alternatively, Chen and co-workers 66 encapsulated bovine serum albumin (BSA) and catalase (CAT) in ZIF-90 or ZPF-10 2 (constructed from Zn 2+ and 2-hydroxy-5-fluoropyrimidine; ZPF = zeolitic pyrimidine framework), which allowed a covalent-organic framework (COF) shell to be grown on the surface of the composites via condensation of 1,3,5-triformylbenzene (or 1,3,5-tris(pformylphenyl)benzene) and 2,5-bis(ethoxy)terephthalohydrazide (COF-42-B or COF-43-B).…”
Section: Figurementioning
confidence: 99%