Jiajia
Sun
ab,
Raghuvara
Yendluri
c,
Kai
Liu
ad,
Ying
Guo
b,
Yuri
Lvov
*ce and
Xuehai
Yan
*a
aState Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, P. R. China. E-mail: yanxh@ipe.ac.cn
bSchool of Chemistry and Environmental Engineering, Harbin University of Science and Technology, Harbin 150080, China
cInstitute for Micromanufacturing and Biomedical Engineering Program, Louisiana Tech University, Ruston, LA 7172, USA. E-mail: ylvov@latech.edu
dUniversity of Chinese Academy of Sciences, Beijing 100049, P. R. China
eI. Gubkin Russian State University of Oil and Gas, Moscow 119991, Russia
First published on 22nd November 2016
We have developed a simple and effective strategy to prepare an enzymatic membrane by the admixing of a halloysite clay nanotube–lipase complex and a chitosan solution. The loading of 3 wt% lipase into the lumen of halloysite clay nanotubes was enhanced with an electrostatic interaction. 10 wt% of lipase–nanotubes were dispersed in an aqueous chitosan solution and cast as a coating. The enzymatic chitosan–halloysite membranes displayed increased pH, temperature stability and long-term usability for the catalytic decomposition of lipids: 90% of the initial activity was preserved at 80 °C, 70% of the functionality remained at the high pH of 9, and 85% of the activity was sustained after ten continuous cycles of use. The placement of the second antimicrobial enzyme–lysozyme at the outer surface of the clay nanotubes allowed for a synergistic increase in the activity of the composite antibacterial formulation. The lipase/lysozyme-co-immobilized clay nanotube–chitosan membranes are promising in anti-biofouling applications.
Biocompatible halloysite clay nanotubes are a promising carrier for various guest molecules, e.g. enzymes and drugs, due to their unique hollow cylindrical structure and abundant availability.15–22 Halloysite has a tubular structure, with a length of 500–800 nm, an outer diameter of 50–60 nm, and a lumen diameter of 12–15 nm.23 Globular enzymes with a typical diameter of 3–6 nm can be loaded into the lumen of these tubes and slowly diffused out. Halloysite nanotubes have a positively charged inner lumen (zeta-potential ξ = +24 mV) which consists of aluminum hydroxide and a negatively charged silicon dioxide outer surface (ξ = −35 mV).23–25 Therefore, the selective immobilization of charged macromolecules on the tubes' inside/outside surfaces can be realized. Negatively charged enzymes will be attracted into the lumen and positively charged enzymes will be adsorbed on the tubes' outer surface.15,24–27
Chitosan, a natural biopolymer mainly composed of β (1-4) linked glucosamine units, is a desirable material for the membranes due to its physiological inertness, biocompatibility, hydrophilicity, good affinity to proteins, and high mechanical strength.28,29 Chitosan has good film-forming capabilities due to its solubility in organic acids.30 Cross-linkers are usually used for covalent binding of enzymes on chitosan carriers,30 but this method involves organic solvents and toxic reagents, and was not used in our membranes, enhancing enzyme immobilization with tubular containers.
We have developed an effective method to fabricate enzymatic membranes using easily accessible materials, halloysite clay nanotubes, chitosan and enzymes with antimicrobial activities – lipase and lysozyme. First, lipase loading into the lumen of the clay nanotube was optimized, and then the resulting enzyme–nanotube complex was mixed with chitosan to fabricate the enzymatic membrane (Scheme 1). The obtained clay nanotube/enzyme hybrid chitosan membranes showed good catalytic lipid decomposition, stability and reusability. Secondly, the cationic lysozyme was adsorbed onto the halloysite tubes' outer surface, which may synergistically increase the antifouling capability of the dual enzyme composite.
:
1) and HNT/lipase (2
:
1) by dissolving the enzyme in phosphate buffer and dispersing the halloysite in an appropriate ratio. The dispersion was placed in 3 cycles of vacuum for 20 minutes. The sample was washed thrice and the pellet obtained after centrifugation was re-dispersed and sonicated. The second enzyme was added to the dispersion in an appropriate ratio and the vacuum loading procedure was repeated. The sample was washed thrice with water, dried and powdered. Thermogravimetric analysis (TGA DuPont 1090B Thermal Analyzer) was also used for protein loading estimation.
The amount of immobilized enzyme on the halloysite clay nanotubes was determined by measuring the initial and final concentrations of protein in the enzyme and washing solutions using the micro bicinchoninic acid (Micro BCA) assay (Pierce Biotechnology, Rockford, IL). A standard calibration curve was constructed by using bovine serum albumin (BSA).
The enzymatic activity of lipase was studied as follows: 20 μL of hexadecanoic acid, 4-nitrophenyl ester (0.5 M) dissolved in acetone was added to the phosphate solution (100 mM, pH 7) containing halloysite clay nanotube/lipase. The reaction system was incubated at 40 °C for 30 min under shaking at 50 rpms. Afterwards, the absorbance of the supernatant was measured at 410 nm. One unit of the lipase was defined as the amount of enzyme required to liberate 1 μmoL p-nitrophenol per minute.
The antibacterial activities of lysozyme and the dual enzyme composites were determined using the bacteria Micrococcus lysodeikticus.32 A 0.01% (w/v) dispersion of the bacteria was prepared in phosphate buffer saline to obtain an initial absorption of 0.6–0.7 at 450 nm. 1 mL of the bacterial dispersion was added to a cuvette and its absorbance (A450) was measured for 60 seconds with readings taken every 10 s using a UV-Vis spectrophotometer. 50 μL of 1 mg mL−1 of halloysite–lysozyme (HNT–L) and halloysite–dual-enzyme composite dispersions was added to the bacteria and the kinetic measurement was continued for 600 s. Lysozyme activity was expressed as the rate of reduction in the absorbance of the bacteria.
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10, and the composite membrane contained 10 wt% of halloysite. Then 1 mL of the mixture was poured into a Teflon dish with a bottom diameter of 36 mm. The enzymatic chitosan was dried at room temperature for 7 days to form halloysite clay nanotube/enzyme/chitosan membranes. A dilute NaOH solution was used to neutralize the membrane. The membrane could be peeled off from the dish using forceps. To determine the amount of enzymes released from these membranes, the membranes were immersed in a phosphate solution (100 mM, pH 7) for 6 hours and the amount of enzymes in the solution was measured using a micro bicinchoninic acid (Micro BCA) assay (Pierce Biotechnology, Rockford, IL).
The catalytic activity of the nanotube/enzyme/chitosan membrane was determined via the hydrolysis of hexadecanoic acid, 4-nitrophenyl ester. In a typical process, the enzymatic membranes were cut into 1 cm2 squares and dipped into 2 mL of phosphate solution (100 mM, pH 7). Then 20 μL of hexadecanoic acid, 4-nitrophenyl ester (0.5 M) dissolved in acetone was added to the above buffer. The reaction system was incubated at 40 °C for 10 min under shaking at 50 rpms. Afterwards, the absorbance of the supernatant was measured at 410 nm. One unit of the WPU-L film was defined as the dimension of the membranes required to liberate 1 μmoL p-nitrophenol per minute.
The loading of enzymes did not change the morphology of the halloysite clay nanotubes. In the BCA analysis, the content of lipase loaded into the halloysite clay nanotubes increases with an increase in the initial content of lipase, and reaches a maximum loading capability of ∼3 wt% (Fig. 2). The samples were carefully washed after enzyme loading, so we assume that most of the adsorbed enzymes are located in the inner lumen, as shown in Fig. 1b. The corresponding catalytic activity of halloysite/lipase also increases with the increase in the loaded enzyme (Fig. 2). These observations indicate that the substrate lipid molecules are accessible to the immobilized enzyme and the product can diffuse into the bulk phase from the tubes' openings. Lysozyme loading was higher, 7 wt%, reaching saturation in the same range of enzyme concentration of 2.5–3 wt%. The catalytic activities of both enzymes were increased in proportion to the loading and reached saturation in the same concentration region (Fig. 3).
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| Fig. 3 Effects of temperature (a) and pH (b) on the relative catalytic activity of free lipase, halloysite–lipase (HNT–L) and halloysite–lipase–chitosan (HNT–L–chitosan) formulations. | ||
Lysozyme has an isoelectric point at pH 11 and it is positively charged at pH 6–7. This results in a larger amount of adsorbed protein of 7 wt%, which is probably located on the outer negative surface, while less loading of negative proteins occurs inside the tubes. Proteins adsorbed on the halloysite tube have a density of ca. 1.3 g cm−3 and the halloysite density is 2.53 ± 0.03 g cm−3, so the equal protein volume will give a mass twice as small. The ratio of the volume fraction of the protein layer ΔL on the outer tube surface (R) to the total tube volume will be 2ΔL/R, and for a protein monolayer of 5 nm thickness, this gives ca. 16 vol% or 8 wt%. Therefore, the experimental 7 wt% lysozyme coating on halloysite results in a monolayer of proteins adsorbed on the outer surface of the tube. While for lipase, the ratio of the volume fraction of the protein layer on the inner lumen tube (r) surface to the total tube volume will be 2ΔLr/R2 and the monolayer coverage is ca. 6 vol% or 3 wt%. So, the results presented in Fig. 2 for the anionic lipase and cationic lysozyme correspond to the tube coverage of the internal and external proteins, respectively.
The halloysite clay nanotube/lipase reveals a better preserved activity under acidic conditions, pH 4 (10 vs. 3%), and is spatially well stabilized under alkaline conditions, pH 10 (55 vs. 8% for the free enzymes) (Fig. 3b). The optimum pH values for the free and immobilized enzymes are the same, pH 7. Similar observations were made for the halloysite-immobilized lysozyme.
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| Fig. 4 Relative catalytic activity of the halloysite clay nanotube/lipase/chitosan membranes with different amounts of lipase. | ||
The HNT–L–chitosan membranes retained ca. 20 and 80% of their residual activity at pH 4 and 9, and 90% at 80 °C, which is a remarkable improvement in temperature stability (Fig. 3a and b). This higher stability is possibly due to the enhanced retention of the enzyme molecules in the nanotubes after admixing into the chitosan matrix. The immobilization of lipase onto the chitosan membrane did not change the optimum temperature or pH. In the BCA analysis, less than 1 wt% of the protein loaded into the chitosan was detected in the incubation solution, and no activity was observed, indicating that almost all of the lipase was irreversibly immobilized into the chitosan–halloysite membranes. We suggest that the cationic chitosan molecular chain binds to the halloysite and blocks the ends of the tubes, thereby decreasing the enzyme leakage.
In this study, the film activity was almost unchanged in the first five cycles. Halloysite clay nanotube/lipase is efficiently entangled within the polymer matrix, thereby allowing enzymes to be retained and to possess activity after long-term reuse of these materials. This property of retention of the enzymatic activity can be compared to the microgel oral delivery system which contained halloysite loaded with bovine serum albumin (BSA).31 BSA immobilized in a pure microgel system retained only 5% of its activity in a digestive environment (PBS with trypsin), whereas BSA encapsulated halloysite incorporated in microgels retained 82% of its activity.
The loading efficiency of individual enzymes and lipase/lysozyme adsorbed at different combinations was determined using TGA, and is presented in Table 1. The loading efficiency of individual enzymes was lower when compared to the sequential enzyme loading, which is in agreement with our hypothesis that first we should load lipase inside the tubes and then load lysozyme outside the tube as defined by the negative–positive charge electrostatic interaction.
| Protein charge | Sample architecture | Loading, ±0.1 (%) |
|---|---|---|
| + | HNT–lysozyme | 7.0 |
| − | HNT–lipase | 3.5 |
| ± | HNT–lipase/lysozyme | 6.9 |
| Mixed | HNT–lysozyme + lipase | 6.3 |
The lipase activity was highest in the sample where lipase was loaded next to lysozyme. It is twice the activity of the sample where lipase was loaded prior to lysozyme. This may be due to the difference in availability of the enzymes from the halloysite. The addition of lipase did not essentially change the overall protein loading because the tube-opening to the inside lumen is blocked by lysozyme. Similarly, starting with negative lipase did not increase the loading efficiency.
The antibacterial activity of a single enzyme and dual enzyme nanotube composites was measured as the rate of decrease in bacterial M. lysodeikticus turbidity in their dispersions.32 The rate of activity of the control sample with pristine halloysite was also measured in order to ensure that halloysite does not contribute to the overall turbidity. Samples which had lysozyme loaded halloysite later had the highest rate (−754.5 AU s−1), suggesting that it was adsorbed on the outside making it more available for the substrate. Halloysite lysozyme composites had a lower rate (−252 AU s−1) compared to the dual enzyme composites (−492.8 AU s−1), suggesting that the presence of another enzyme contributes synergistically to the activity.
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