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Biotechnology and Biological Transformations
Efficient immobilization of bacterial GH family 46 chitosanase by carbohydrate-binding module fusion for the controllable preparation of chitooligosaccharides Si Lin, Zhen Qin, Qiming Chen, Liqiang Fan, Jiachun Zhou, and Liming Zhao J. Agric. Food Chem., Just Accepted Manuscript • DOI: 10.1021/acs.jafc.9b01608 • Publication Date (Web): 27 May 2019 Downloaded from http://pubs.acs.org on May 28, 2019
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Journal of Agricultural and Food Chemistry
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Efficient immobilization of bacterial GH family 46 chitosanase by carbohydrate-
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binding module fusion for the controllable preparation of chitooligosaccharides
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Si Lina†, Zhen Qinab†, Qiming Chenab, Liqiang Fanab, Jiachun Zhouab, and Liming
4
Zhaoab*
5 6
a
7
Center of Separation and Extraction Technology in Fermentation Industry, East China
8
University of Science and Technology, Shanghai 200237, China
9
b
10
School of Biotechnology, State Key Laboratory of Bioreactor Engineering, R&D
Shanghai Collaborative Innovation Center for Biomanufacturing Technology
(SCICBT) , Shanghai 200237, China
11 12
† These
13
*
14
E-mail address:
[email protected] (L.M. Zhao)
15
Fax: +86 021-64250829
16
No. 130 Meilong Road, Shanghai 200237, China
authors contributed equally in this study.
Corresponding author.
17 18 19 20 21 22
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Abstract
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Chitooligosaccharide has been reported to possess diverse bioactivities. The
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development of novel strategies for obtaining optimum degree of polymerization (DP)
26
chitooligosaccharides has become increasingly important. In this study, two glycoside
27
hydrolase family 46 chitosanases were studied for immobilization on curdlan (insoluble
28
β-1,3-glucan) using a novel carbohydrate binding module (CBM) family 56 domain
29
from a β-1,3-glucanase. The CBM56 domain provided a spontaneous and specific
30
sorption of the fusion proteins onto a curdlan carrier, and two fusion enzymes showed
31
increased enzyme stability in comparison with native enzymes. Furthermore, a
32
continuous packed-bed reactor was constructed with chitosanase immobilized on a
33
curdlan
34
chitooligosaccharide products with different molecular weights were prepared in
35
optimized reaction conditions. This study provides a novel CBM tag for the
36
stabilization and immobilization of enzymes. The controllable hydrolysis strategy
37
offers potential for the industrial-scale preparation of chitooligosaccharides with
38
different desired DPs.
carrier
to
control
the
enzymatic
hydrolysis
of
chitosan.
Three
39 40
Keywords: Chitosanase; Carbohydrate binding module; Chitooligosaccharide; One-
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step immobilization-purification; Packed-bed reactor
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INTRODUCTION
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Chitooligosaccharides (COS), the hydrolyzed product of chitosan, are oligomers of
47
β-1,4-linked D-glucosamine with high solubility in neutral aqueous solutions.
48
Chitooligosaccharide has various beneficial biological activities, such as antimicrobial
49
activity
50
activity 5 and immunostimulatory activity 6. As a result of these biological activities,
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chitooligosaccharides are widely applied in various fields, including functional foods,
52
agriculture and pharmacy.
1-2,
antioxidant activity 3, anti-inflammatory activity 4, anti-tumor/anticancer
53
A variety of techniques have thus far been used for the production of
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chitooligosaccharides from chitosan, including chemical 7-8, physical 9-10 and enzymatic
55
methods 11-12. In terms of high safety levels and low toxicity, the enzymatic degradation
56
method has shown great potential in industrial applications. Chitosanase (E C 3.2.1.132)
57
is a specific chitosan degrading enzyme. Most of the reported chitosanases are endo-
58
type glycoside hydrolases, which hydrolyze the β-1,4-linked glycosidic bond inside the
59
chitosan chain, releasing a mixture of chitooligosaccharides with uncontrollable
60
degrees of polymerization (DP)
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biological activities of chitooligosaccharides are related to their DP 15. Although there
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are many advantages in the enzymatic preparation of chitooligosaccharides, obtaining
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chitooligosaccharides with the desired DP is generally time consuming and challenging.
64
The persistent instability and the high cost of the process restricts the application of
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chitosanases in large-scale industrial applications
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highly efficient bioconversion process for the industrial-scale production of
13-14.
However, previous studies have shown that the
16
and, therefore, a controllable and
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chitooligosaccharides is sought.
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Carbohydrate binding modules (CBMs) are independent domains existing in
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carbohydrate active enzymes. The majority of such domains exhibit carbohydrate
70
binding activity, which enhances the catalytic efficiency of carbohydrate active
71
enzymes 17. Due to this highly specific binding ability towards insoluble carbohydrate,
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CBMs have been used as efficient immobilization tools of recombinantly fused proteins
73
for different applications 18-20. Mai-Lan et al. 21 reported the construction of three fusion
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enzymes composed of the chitin-binding domain and β-galactosidase. The fusion β-
75
galactosidases were immobilized on chitin beads to provide an approach for lactose
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hydrolysis and the production of prebiotic galacto-oligosaccharides. Chang et al.
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fused six different CBMs to the double-site variant of β-glucosidase to effectively
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hydrolyze soybean isoflavone glycosides. Furthermore, other CBM-fusion strategies
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enhance the properties (such as catalytic efficiency, organic solvent tolerance and
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stability) of target enzymes 23-25.
81
22
In this study a novel CBM family 56 β-1,3-glucan binding module, derived from 26,
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the Paenibacillus barengoltzii β-1,3-glucanase (PbBgl64A)
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glycoside hydrolase (GH) family 46 chitosanases. The catalytic properties of the fusion
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proteins were then evaluated for the preparation of immobilized enzymes. On this basis,
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the fusion chitosanase was immobilized into curdlan support and then loaded in a
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continuous packed-bed reactor with the potential to control the enzymatic hydrolysis
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process of chitosan. This study thereby provides a novel CBM tag for the stabilization
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and immobilization of enzymes. The subsequent controllable hydrolysis strategy offers
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was fused to two
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the potential for the industrial-scale preparation of different desired DPs
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chitooligosaccharides products.
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MATERIALS AND METHODS
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Materials and microorganisms
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The DNA amplification was performed with EasyPfu DNA Polymerase (TransGen
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Biotech, Beijing, China). Escherichia coli DH5α and BL21 (DE3) strains were
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purchased from Cwbio (Beijing, China) and used as cloning and protein expression
97
hosts, respectively. Both hosts were cultivated in Luria-Bertani (LB) medium.
98
Kanamycin was purchased from Biosharp (Beijing, China) and used as a selectable
99
marker at 50 μg/mL. pET-28a(+) vector was used as an expression vector. Restriction
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enzymes were purchased from Takara (Otsu, Japan). Chitosan (degree of
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deacetylation≥95 %, viscosity < 200 mPa.s) was purchased from Aladdin (Beijing,
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China). Curdlan was purchased from Shandong Zhongke (Shandong, China). All other
103
chemicals were analytically pure.
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Construction of fusion enzymes
105
In our previous study, two GH family 46 chitosanases (GsCsn46A and BaCsn46A)
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from different bacteria were identified and expressed. GsCsn46A was a cold-adapted
107
chitosanase from Gynuella sunshinyii
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amyloliquefaciens, which showed high specific activity towards chitosan (1031.2 U/mg)
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to yield a series of chitooligosaccharides 29. These two chitosanases were typical GH
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family 46 chitosanases, which are widely used in the industrial preparation of
27.
And BaCsn46A was from Bacillus
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chitooligosaccharides. Additionally, in our previous structural study of a GH family 64
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β-1,3-glucanase from Paenibacillus barengoltzii (PbBgl64A)
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family 56 β-1,3-glucan binding module (CBM56) was detected in the N-terminus of
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PbBgl64A. Genes used in this study are listed in Table 1 and gene sequence information
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are listed in supplemental Table S1.
26,
a potential CBM
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Two fusion proteins were constructed, based on the nucleotide sequences of
117
GsCsn46A, BaCsn46A and CBM56. CBM56 was linked at the respective N-terminus
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of two chitosanases, and a natural loop linker, ‘-SGQPDPEPS-’ from PbBgl64A, was
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inserted between CBM56 and the chitosanases in the fusion protein. A total of seven
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PCR primers were used in this study, as listed in Table 2. Both fusion genes (CBM56-
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GsCsn46A and CBM56-BaCsn46A) were constructed by overlapping PCR, and
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engineering the CBM56 gene into the 5’-terminus of GsCsn46A gene and BaCsn46A
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gene, respectively. The detailed protocol of overlapping PCR is described as follows.
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The gene fragment of CBM56-1 and GsCsn46A, for the construction of CBM56-
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GsCsn46A, were amplified by PCR using primers (F1, R1-Gs) and primers (F2-Gs, R2-
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Gs). And the fragments of CBM56-2 and BaCsn46A, for the construction of CBM56-
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BaCsn46A, were amplified by PCR using primers (F1, R3-Ba) and primers (F4-Ba, R4-
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Ba). The template were pUC57-CBM56 plasmid, pET28a(+)-GsCsn46A plasmid and
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pET28a(+)-BaCsn46A plasmid respectively. Using the amplified CBM56-1,
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GsCsn46A as templates and F1, R2-Gs as primers, overlapping of PCR for the entire
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fusion gene, CBM56-GsCsn46A, was carried out as follows: 30 cycles at 94 °C for 5
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min, 55 °C for 30 s, and 72 °C for 2 min. Similarly, another entire fusion gene, CBM56-
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BaCsn46A, was amplified using the PCR products CBM56-2 and BaCsn46A, along
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with the primers F1- and R4-Ba, under the same overlapping conditions. The amplified
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target PCR products were gel-purified using a Gel Extraction Kit (Sangon Biotech,
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Shanghai, China), digested with NheI and XhoI, and inserted into the pET-28a(+) vector,
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5 μL recombinant plasmid was added into 100 uL E. coli DH5α, 37 °C at 200 rpm for
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45 min, and the transformants were cultured on LB agar plates containing 50 μg/mL
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Kanamycin at 37 °C overnight.
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Expression and purification of fusion enzymes
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The constructed plasmids were transformed into E. coli BL21 (DE3) and cultured
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on LB-agar plates containing Kanamycin (50 μg/mL). The expression of fusion
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enzymes was induced at OD600 of about 0.6–0.8 by adding isopropyl β-D-1-
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thiogalactopyranoside (IPTG) to a final concentration of 0.1 mM and further incubating
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at 30°C at 200 rpm overnight.
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The fusion enzyme was purified, as described previously 27. The E. coli cells were
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harvested using centrifugation at 10000 ×g for 5 min. The cells were then re-suspended
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in buffer A (50 mM Tris-HCl pH 8.0, 500 mM NaCl, 20 mM imidazole). The target
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proteins were released from the cells by sonication (the diameter of ultrasonic horn is
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6 mm, ultrasonic 2 s, pause 3 s, repeat 10 min, power 650 W). The debris was removed
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by centrifugation at 10000 ×g for 10 min, and the supernatant was pumped into a Ni-
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IDA column (GE life Sciences) pre-equilibrated with buffer A. Then the recombinant
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protein was eluted by step gradient of 20-200 mM imidazole. The resulting samples
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were analyzed by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-
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PAGE) using 12.5% separation gel. The protein concentration was determined by
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means of a Bradford protein assay kit (Solarbio, Beijing, China), using BSA as the
157
standard.
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Chitosanase activity assay
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Chitosanase activity was determined by the 3,5-dinitrosalicylic acid (DNS) method,
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as described previously 27. The content of reducing sugar was determined by measuring
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OD at 540 nm, using D-glucosamine as standard. The chitosanase activity of CBM56-
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BaCsn46A was determined using the same method, except that the substrate mixture
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was prepared in a 100 mM sodium acetate buffer pH 6.0, and the reaction mixture was
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incubated at 50 °C for 10 min. All reactions were done in triplicate and their mean and
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standard deviation values were used for analysis. One unit (U) of chitosanase activity
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is defined as the amount of enzyme liberating 1 μmol D-glucosamine-equivalent
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reducing sugars per minute under the above conditions.
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Characterization of two fusion enzymes
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Chitosan was used as the substrate to determine the characterization of the fusion
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enzymes. With respect to the enzymatic characterization of CBM56-GsCsn46A, the
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optimal pH was determined by measuring the activity levels from 3.0 to 9.0 using the
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following 0.2 M buffers: Mcllvaine buffer (pH 2.5–5.0), sodium acetate buffer (pH 4.5–
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6.0), phosphate buffer (pH 6.0–7.5), Tris-HCl buffer (pH 7.5–9.0) and glycine-NaOH
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buffer (pH 9.0–11.0). To determine the pH stability, residual activity was measured
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after incubation of the enzyme at 25 °C for 30 min in the various 0.2 M buffers. The
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optimal temperature was determined at 15–60 °C in 0.2 M sodium acetate buffer, pH
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5.5. Enzymatic activity was determined under standard conditions. Thermostability of
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the enzyme was determined by measuring residual activity after incubation of the
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enzyme at various temperatures (15–60 °C) for 30 min in 0.2 M sodium acetate buffer,
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pH 5.5. For CBM56-BaCsn46A, the optimal pH was measured in various 0.2 M buffers,
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pH (4.0–8.0). The pH stability of CBM56-BaCsn46A was measured by incubation of
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the enzyme in the range of pH (2.5–10.5) at 25 °C for 30 min. Optimal temperature of
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CBM56-BaCsn46A was measured at temperatures of 30–70 °C in 0.2 M sodium acetate
184
buffer, pH 6.0. The thermal stability was investigated at 30–70 °C and determined in
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0.2 M sodium acetate buffer, pH 6.0.
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Immobilization efficiency of fusion protein onto curdlan
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Food grade curdlan, washed three times by sodium acetate buffer (50 mM, pH 6.0),
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was employed as the carrier for immobilization. The curdlan (1 g) was dispersed in 20
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mL sodium acetate buffer (50 mM, pH 6.0), to which 5 mL diluted cell-free crude
190
extracts (containing 1000 U of the fusion chitosanases) was added. The immobilization
191
experiment was carried out at 20 °C with gentle agitation for 10 min. The amount of
192
the immobilized chitosanases was calculated according to the residual chitosanase
193
activity in the supernatant after treating with curdlan. After affinity sorption, the curdlan
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carrier was washed three times with 50 mM sodium acetate buffer (pH 6.0) and eluted
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with 1 mL of SDS-PAGE solubilizing buffer (100 mM Tris-HCl buffer pH 8.8
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containing 1% SDS, 1% β-mercaptoethanol, 30% glycerol, and 0.01% bromphenol blue)
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at boiling temperature for 5 min. The curdlan beads were removed by centrifugation,
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and the supernatant was subjected to SDS-PAGE under reducing conditions.
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Reuse of the immobilized enzyme
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In order to evaluating the reuse of the immobilized enzyme, 5 mL of suspended
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immobilized enzyme (chitosanase activity 100 U/mL) were incubated with 100 mL
202
chitosan substrate solution (100 mg/mL, pH 5.5) for 3 hours at 45 °C. Supernatant
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samples withdrawn at different times were immediately analyzed by DNS method to
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evaluate the reducing sugar content of chitooligosaccharides products. The relative
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reducing sugar content of the products represents the catalytic activity of the
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immobilized enzyme resin. After each reaction, the immobilized enzyme was washed
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with 50 mL 0.1 M sodium acetate buffer pH 5.5 to remove residual substrate, then
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stored at 4°C until the next repetition of the batch reaction. The final concentration of
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reducing sugar in the first cycle reaction was defined as 100 % relative reducing sugar
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content. The immobilized enzyme reuse experiment was repeated six times.
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Application of immobilized chitosanase in packed-bed reactor
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In order to achieve control in the preparation of chitooligosaccharides with different
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DPs, a packed-bed reactor was built to evaluate the application of the immobilized
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chitosanase. In consideration of the catalytic efficiency and stability of the immobilized
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chitosanase, CBM56-BaCsn46A was selected for further research into the controllable
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preparation of chitooligosaccharides. Briefly, 10 g curdlan was dispersed in 100 mL
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sodium acetate buffer (50 mM, pH 6.0), incubated with 25 mL cell-free crude extracts
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at 20 °C with gentle agitation for 20 min. After affinity sorption, the curdlan carrier was
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washed three times with 50 mM sodium acetate buffer (pH 6.0). The curdlan-
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immobilized enzyme was separated from the supernatant by centrifugation and
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resuspended in 250 mL sodium acetate buffer (50 mM, pH 6.0). The immobilized
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chitosanase activity was determined using suspension by the standard enzyme assay
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conditions mentioned above.
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The resuspended curdlan immobilized enzyme was placed in a water-jacketed glass
225
column (diameter: 45 mm, height: 300 mm) and silica sand (5 g, particle size 100–150
226
μm) was mixed with the curdlan powder to ensure flux. The enzyme amount, flow rate
227
and concentration of the chitosan substrate were all optimized as follows to regulate the
228
chitosan hydrolysis reaction process:
229
(1) The effect of the enzyme amount: Different amounts (immobilized chitosanase
230
range from 50 U to 1000 U) of the abovementioned resuspended curdlan (containing
231
3888 U protein/g) were placed into the column. The substrate solution (1 % (w/v)
232
chitosan, 50 mM sodium acetate buffer, pH 5.0) was pumped into the packed-bed
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reactor from top to bottom by peristaltic pump at a flow rate of 2.0 mL/min.
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(2) The effect of the flow rate: Resuspended curdlan (immobilized 250 U chitosanase)
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and silica sand were placed into the column. The substrate solution (containing 1 %
236
(w/v) chitosan and 50 mM sodium acetate buffer, pH 5.0) was pumped into the column
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at different flow rates (0.5 to 4 mL/min) to control the reaction times.
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(3) The effect of the concentration of chitosan: In order to evaluate the influence of
239
substrate solution concentrations on chitooligosaccharide production, four different
240
concentrations of chitosan solution (ranging from 0.5 % to 2.0 %, w/v) were used for
241
the chitosan hydrolysis.
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All abovementioned reaction temperature was stabilized at 45 °C by circulating
243
thermostated water in the jackets surrounding the enzyme columns. The reaction
244
product was collected for further analysis.
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Chitooligosaccharide analysis methods
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The relative average molecular weight of chitosan hydrolysate is measured using
247
the acetylacetone method 28. The acetylacetone solution was prepared by transferring
248
3.5 mL of acetylacetone into 46.5 mL buffer solution (1 M sodium carbonate). A
249
dimethyl benzaldehyde solution was prepared using 0.8 g dimethyl benzaldehyde
250
mixed with 15 mL ethanol (AR, 100 %) and 15 mL hydrochloric acid (AR, 37 %). To
251
determine the relative average molecular weight of the reaction product, 1 mL
252
acetylacetone solution was added to the 5 mL chitooligosaccharide sample (1 mg/mL),
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following by a boiling water bath for 25 min. After cooling to room temperature, 1 mL
254
dimethyl benzaldehyde solution and 3 mL ethanol (100 %) were added to the reaction
255
mixture. The mixture was incubated in a 60°C water bath for 1 h, then rapidly cooled
256
to room temperature. The relative average molecular weight was determined by
257
measuring OD at 525 nm using D-glucosamine as standards.
258
The reaction products withdrawn at different times were immediately boiled for 5
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min, and then analyzed by thin-layer chromatography (TLC). Samples (1 μL) were
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spotted and developed on a silica gel plate (TLC aluminum sheets silica gel 60; Merck,
261
Darmstadt, Germany) with an isopropanol-water-28 % ammonia (75:10:15) mixture as
262
the developing solvent. The hydrolysis products were visualized by spraying them with
263
alcohol: p-anisaldehyde: sulfuric acid: acetic acid (89:5:5:1, v/v) and then heating the
264
plate at 130 °C in an oven for a few minutes.
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The molecular weight distribution of the chitooligosaccharide products was
266
determined by gel permeation chromatography (GPC) (P230; Elite, Dalian, China).
267
Separation of chitooligosaccharides was achieved by PL aquagel-OH MIXED-H 8 μm
268
(7.5 mm×30 cm; Agilent, Santa Clara, California) at 40 °C. The sodium nitrate (0.5 M)
269
was used as mobile phase, with a flow rate of 1.0 mL/min.
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RESULTS AND DISCUSSION
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Plasmid construction and expression of fusion protein
273
In order to evaluate the novel carbohydrate binding domain (CBM56) for fusion,
274
two GH family 46 chitosanases with different characterization were selected to be fused
275
with the CBM56. The CBM56 was linked at the N-terminus of chitosanases, and a
276
nearby natural loop linker ‘-SGQPDPEPS-’ was inserted between it and the target
277
chitosanases in the fusion protein. The two fusion proteins (CBM56-GsCsn46A and
278
CBM56-BaCsn46A) were constructed in the plasmid pET28a(+) (Fig. 1), respectively,
279
and transformed into E. coli BL21 (DE3). The CBM56 encoding gene and the two
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chitosanases genes were 255 bp (CBM56), 729 bp (GsCsn46A) and 729 bp
281
(BaCsn46A), respectively.
282
Results showed that the recombinant fusion enzymes were both expressed in the
283
soluble fraction. Two recombinant fusion enzymes were purified by one step of affinity
284
chromatography to electrophoretic homogeneity (Fig. 2). The molecular mass of
285
CBM56-GsCsn46A and CBM56-BaCsn46A were estimated to be about 37 kDa by
286
SDS-PAGE (Fig. 2), which matched its predicted molecular mass (37.5 kDa and 37.8
287
kDa).
288
Catalytic properties of native enzymes and fusion enzymes
289
In order to reveal the effect of the fusion CBM56 tag on the catalytic activity of the
290
native protein, the catalytic properties of the two fusion proteins were determined. The
291
fusion protein CBM56-GsCsn46A exhibited specific activity towards chitosan (303
292
U/mg) at 30 °C in 50 mM sodium acetate buffer, pH 5.5, which is slightly higher than
293
the specific activity of native GsCsn46A (260.87 U/mg)
294
conditions. CBM56-BaCsn46A exhibited highly specific activity towards chitosan
295
(1156.54 U/mg) at 50 °C in 50 mM sodium acetate buffer pH 6.0, which is slightly
296
higher than that of the native BaCsn46A (1031.2 U/mg)
297
conditions. Furthermore, the effects of pH and temperature on the chitosanase activity
298
of two fusion enzymes were examined. The range of optimal pH for the activity of
299
fusion chitosanase was found to be comparable to that of the original enzymes
300
expressed in the same host. CBM56-GsCsn46A displayed maximal chitosanase activity
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27
29
under the same reaction
under the same reaction
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at pH 6.5 in 50 mM phosphate buffer (Fig. 3A) and exhibited good pH stability within
302
the range of pH 3.5–10.5, retaining over 95 % of its activity (Fig. 3B), while the native
303
chitosanase GsCsn46A showed an optimum pH at 5.5, and exhibited good pH stability
304
within the range of 4.0–8.5 27. CBM56-BaCsn46A also displayed maximal chitosanase
305
activity at pH 6.5 in 50 mM phosphate buffer (Fig. 4A) and exhibited good pH stability
306
within the range of pH 3.0–10.5, retaining over 95 % of its activity (Fig. 4B). The native
307
chitosanase BaCsn46A showed an optimum pH at 6.0, and exhibited good pH stability
308
within the range of 4.0–9.5
309
determined to be 40 °C (Fig. 3C). The fusion enzyme was stable up to 35 °C, with more
310
than 90 % of its activity remaining (Fig. 3D), while the native chitosanase GsCsn46A
311
showed an optimum temperature at 30 °C and maintained stability up to 35 °C, with
312
more than 80 % its activity remaining
313
BaCsn46A was determined to be 50 °C (Fig. 4C). The fusion enzyme was stable up to
314
55 °C, with more than 80 % of its activity remaining (Fig. 3D), while the native
315
chitosanase BaCsn46A showed an optimum temperature at 50 °C and was stable up to
316
45 °C, with more than 80 % of its activity remaining 29.
29.
The optimal temperature for CBM56-GsCsn46A was
27.
The optimal temperature for CBM56-
317
Fusion protein is a common protein engineering approach to improve the
318
performance of target proteins 30. Previous studies showed that the fusion of a small
319
domain can not only improve the thermal stability31-32, but also affect the optimal
320
temperature of target proteins
321
chemical reactions. Thus, increased stability helps the enzyme to catalyze at higher
322
reaction temperatures. The fusion of a small domain could enhance the rigidity of target
33.
In general, higher temperatures increase the rate of
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protein, and reduce the flexibility of the highly flexible terminal loop, thus increase the
324
protein stability
325
stability, rigidity and activity of target enzymes 31, 34. In this study, the CBM56 domain
326
may increase the rigidity of the fusion protein and stabilize the terminus of the target
327
protein. Thus, the stability of the target chitosanases has been enhanced. However, in
328
other cases, the addition of a fusion protein to a CBM domain at the N- or C-terminus
329
of the enzymes produced a lower catalytic effect than that of the native enzyme 31, 35-36,
330
which suggests that only a specifically suitable CBM can produce synergistic
331
interactions with the catalytic module to enhance the activity and stability of an enzyme
332
31.
333
these two chitosanases.
334
Immobilization of fusion chitosanases on curdlan
30, 33.
Fusion of the CBM domain may, in some cases, enhance the
Thus, CBM56 could be the suitable module to improve the catalytic properties of
335
The immobilization of proteins generally requires time-consuming, multi-step
336
protocols, so there is a clear need for one-step methods to enable the purification and
337
immobilization of enzymes at a low cost. In this study, the CBM56 domain displayed
338
a specific affinity for β-1,3-glucan. One-step immobilization-purification of enzymes
339
may, therefore, be achieved by fusing the CBM56 domain in the recombinant protein,
340
thereby enabling the direct purification and immobilization of enzymes from E. coli
341
crude cell extracts using β-1,3-glucan carrier materials. Here, the suitability of
342
commercially available β-1,3-glucan (curdlan) was chosen for further study (Fig. 5).
343
The fusion proteins crude cell extracts were used in equal volume to study their affinity
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344
to curdlan. SDS-PAGE showed that both CBM56-BaCsn46A and CBM56-GsCsn46A
345
were specifically absorbed on curdlan (Fig. 5C and 5D), indicating that this insoluble
346
polysaccharide is able to immobilize and purify enzymes from crude cell extracts.
347
Immobilized efficiency results showed that 896.94 U of CBM56-GsCsn46A and 901.25
348
U of CBM56-BaCsn46A fusion proteins bound to 1 g of curdlan powder from 1000 U
349
crude cell extracts after 20 minutes of incubation at 20 °C, indicating that the loading
350
efficiency of the CBM56-GsCsn46A and CBM56-GsCsn46A was 89.7% and 90.1 %,
351
respectively. This strategy utilizes a natural polysaccharide as the immobilized support
352
without any treatment, making it convenient to use and low cost as well as avoiding the
353
environmental effects of chemically modified supports. In order to evaluating the reuse
354
of the immobilized enzyme, reusability of the immobilized CBM56-BaCsn46A was
355
then investigated by batch hydrolysis of chitosan substrate. The catalytic activity of the
356
reused immobilized enzyme was characterized by the reducing sugars contents during
357
the reaction process. Result showed that immobilized CBM56-BaCsn46A could be
358
used to hydrolyze chitosan for at least six times, with retaining 77.5% of its initial
359
catalytic activity (Figure 5E). This means that the immobilized chitosanase could be
360
reused in batch reactions.
361
Many previous studies have used CBM-fused proteins for immobilization onto an
362
insoluble polysaccharide (mostly, cellulose and chitin). This study provided a novel
363
CBM56 domain for immobilizing enzymes onto curdlan (β-1,3-glucan), a naturally
364
insoluble polysaccharide, which can be used directly as an immobilization carrier.
365
Furthermore, curdlan is edible and, therefore, suitable for use in purifying and
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immobilizing food enzymes, which can then be used directly for food processing.
367
Although the enzyme immobilization for the preparation of functional oligosaccharides
368
does have some advantages, the complicated process and high-cost immobilization
369
techniques limit their use in industrial application. Among the methods of chitosanase
370
immobilization, the fusion of a CBM56 domain to immobilize enzymes on a curdlan
371
carrier would be a simple, cost-effective strategy, which is worth a further investigate.
372
Controllable preparation of chitooligosaccharides by immobilized BaCsn46A
373
In order to control the enzymatic hydrolysis of chitosan, a continuous packed-bed
374
reactor with chitosanase immobilized on a curdlan carrier was constructed for the
375
controllable preparation of chitooligosaccharides with different DPs. We found that the
376
hydrolysis products and hydrolysis processes of the two chitosanases are similar in the
377
pre-experiment. The use of two enzymes in the experiment does not help to prepare
378
chitooligosaccharides with different degrees of polymerization. In consideration of the
379
catalytic efficiency and stability of the immobilized chitosanase, CBM56-BaCsn46A
380
was selected for the further research about the controllable preparation of
381
chitooligosaccharides. The amount and flow rate of the enzyme and the concentration
382
of chitosan substrate were optimized to regulate the reaction process of chitosan
383
hydrolysis. The DP/average molecular weight of different chitooligosaccharide
384
products obtained by various conditions were analyzed by TLC and the acetylacetone
385
method. Results showed that the ratio of the lower DP chitooligosaccharide product
386
increases as the amount of chitosanase increases (Fig. 6). Here, the relative average
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387
weight of chitooligosaccharide product decreased from 4944 Da to 1211 Da along with
388
the increasing amount of chitosanase (Table S2). In contrast, higher DP
389
chitooligosaccharide products were accumulated during the increase in flow rate of the
390
chitosan substrate (Fig. 6) and, with an increase in the substrate pumping rate, a higher
391
molecular weight of COS was gradually accumulated. The relative average weight of
392
chitooligosaccharide product increased from 1156 Da to 2327 Da (Table S2). Thus,
393
changing the flow rate of the chitosan substrate could enable control of the contact times
394
between substrate and enzyme. Increasing the concentration of chitosan slightly
395
increased the average weight of the products (Table S2).
396
The optimized preparation conditions were then utilized in the packed-bed reactor.
397
According to the aforementioned results of the average weight of products, three
398
conditions were selected for the production of different DPs chitooligosaccharides: (1)
399
low molecular weight: 1000 U of immobilized chitosanase, 1 % (w/v) chitosan solution,
400
0.5 mL/min substrate pumping rate; (2) medium molecular weight: 250 U of
401
immobilized chitosanase, 1 % (w/v) chitosan solution, 2 mL/min substrate pumping
402
rate; and (3) high molecular weight: 250 U of immobilized chitosanase, 1 % (w/v)
403
chitosan
404
chitooligosaccharides produced under these three conditions were qualitatively
405
analyzed by means of TLC and HPLC (Fig. 7A and supplementary Fig. S2). As
406
expected, a higher enzyme activity or lower substrate pumping rate led to complete
407
chitosan hydrolysis. Under the first condition, mainly lower DP chitooligosaccharides
408
(DP 2–4) were produced in the continuous hydrolytic process, while higher DP
solution,
4
mL/min
substrate
pumping
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rate.
The
different
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409
chitooligosaccharides (DP 4–6) were accumulated under the second condition. Under
410
the third condition, chitooligosaccharides with high DPs were the main products. The
411
average molecular weight of the three products was subsequently analyzed by GPC (Fig.
412
7). Chitooligosaccharides products with three different average molecular weights (Mw:
413
7050, 33500 and 79100) were prepared under optimized reaction conditions. Thus,
414
based on the abovementioned immobilized chitosanase (CBM56-BaCsn46A), the
415
continuous packed-bed reactor was able to control the enzymatic hydrolysis of chitosan.
416
Numerous previous studies have reported the value of chitosanases in the
417
preparation of chitooligosaccharides. However, only a few subsequent studies have
418
investigated processes suitable for controllable chitooligosaccharides production.
419
Industrial scale enzymatic preparation of chitooligosaccharides with different desired
420
DPs is still complicated. As the biological activities of chitooligosaccharides are related
421
to their DP, a low-cost method for the preparation of specific DP chitooligosaccharides
422
should be urgently explored. Enzyme membrane reactor is a proven effective method
423
for separating high DP chitooligosaccharides
424
pressurized membrane reactor limits its application on an industrial scale. Protein-
425
engineering of the product specificity of the chitosanase is another successful approach
426
to control the DP of chitooligosaccharide products
427
chitooligosaccharides are still hard to obtain due to the structure of the catalytic groove
428
of chitosanase. In immobilized forms, enzymes are easy to facilitate in continuous
429
production. In this study, a packed-bed reactor was constructed to enable the easy
430
monitoring and termination of the chitosan hydrolytic reaction, though its application
29, 37-38,
nevertheless, the high cost of a
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39,
however, high DP
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431
is currently limited by preparation of chitooligosaccharides mixtures with definite DP.
432
Three types of chitooligosaccharide products with different ranges of DP were obtained
433
by controlling the reaction conditions, making this approach suitable for the separation
434
and purification of specific chitooligosaccharides in further studies.
435
In conclusion, this work describes an efficient method for immobilizing
436
chitosanases onto curdlan (insoluble β-1,3-glucan) via a β-1,3-glucan-binding domain
437
(CBM56) and using the immobilized enzyme for the controllable preparation of
438
chitooligosaccharides. Two fusion enzymes (CBM56-GsCsn46A and CBM56-
439
BaCsn46A) exhibited improved pH levels and temperature stability after CBM56
440
domain fusion. With respect to the specific sorption of the CBM56 domain, the
441
immobilization process incubated fusion chitosanases onto curdlan under mild
442
conditions, with no additional purification. Based on the above immobilized
443
chitosanase (CBM56-BaCsn46A), a continuous packed-bed reactor was constructed to
444
control the enzymatic hydrolysis of chitosan. Chitooligosaccharide products with
445
different DPs (Mw: 7050, 33500 and 79100) were prepared by optimizing the reaction
446
conditions. This study provides a promising and easy-control approach for controllable
447
chitosan hydrolysis the production of chitooligosaccharides with different DPs on an
448
industrial scale.
449 450
Funding
451
This work was financially supported by the National Natural Science Foundation of
452
China (31701537), “Shu Guang” (15SG28) and “Chen Guang” (17CG28) Project of
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453
Shanghai Municipal Education Commission and Shanghai Education Development
454
Foundation, Shanghai Sailing Program (17YF1403500), Fundamental Research Funds
455
for the Central Universities (222201814031, 22221818014), The National Key
456
Research and Development Program of China (2018YFC0311200) and the 111 Project
457
(B18022).
458 459
Supporting Information
460
The Supporting Information is available free of charge on the ACS Publications website.
461 462
References
463 464 465 466 467 468 469 470 471 472 473 474 475 476 477 478 479 480 481 482 483 484 485 486 487
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of chitosanase from Bacillus sp. MN to alter its substrate specificity. Biotechnol. Bioeng. 2018, 115 (4), 863-873.
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Figure legends
581
Figure 1 Schematic presentation of the construction of vectors for the expression of
582
the fusion enzymes (left); schematic presentation of the fusion of CBM56 with
583
chitosanases.
584
Figure 2 SDS-PAGE analysis of purified fusion enzymes. Recombinant proteins were
585
purified by Ni-IDA column. (M) protein marker, (1) purified CBM56-GsCsn46A, (2)
586
purified CBM56-BaCsn46A.
587
Figure 3 The effects of temperature and pH on the activity of the purified native
588
GsCsn46A (black) and CBM56-GsCsn46A (red). (A) optimum pH; (B) pH stability;
589
(C) optimum temperature; (D) thermostability. For thermostability, the residual activity
590
was measured after incubating the enzyme at different temperatures for 30 min in 50
591
mM acetate buffer (pH5.5). The experiments were done in triplicate and their mean and
592
standard deviation values were used for analysis.
593
Figure 4 The effects of temperature and pH on the activity of the purified native
594
BaCsn46A (black) and CBM56-BaCsn46ACsn46A (red). (A) optimum pH; (B) pH
595
stability; (C) optimum temperature; (D) thermostability. For thermostability, the
596
residual activity was measured after incubating the enzyme at different temperatures
597
for 30 min in 50 mM acetate buffer (pH6.0). The experiments were done in triplicate
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598
and their mean and standard deviation values were used for analysis.
599
Figure 5 The properties of the immobilized chitosanases. (A) photograph of curdlan
600
powder; (B) photograph of immobilized enzyme; (C) and (D) SDS-PAGE analysis of
601
one step immobilized CBM56-GsCsn46A (C) and CBM56-BaCsn46A (D) from E. coli
602
crude cell extracts. M: protein marker, 1: crude cell extract; 2: protein adsorbed by
603
curdlan carrier. (E) The reuse of the immobilized CBM56-BaCsn46A. The relative
604
reducing sugar content of the products represents the catalytic activity of the
605
immobilized enzyme resin.
606
Figure 6. TLC analysis of hydrolysates. (A) the effect of the enzyme amount; (B) the
607
effect of the flow rate; (C) the effect of the concentration of chitosan.
608
Figure 7 (A) TLC analysis of the three optimized different chitooligosaccharide
609
products; (M) chitooligosaccharide marker; (1) hydrolysis condition: 1000 U of
610
immobilized enzyme, 1 % (w/v) chitosan solution, 0.5 mL/min substrate pumping rate;
611
(2) hydrolysis condition: 250 U of immobilized enzyme, 1 % (w/v) chitosan solution,
612
2 mL/min substrate pumping rate; (3) hydrolysis condition: 250 U of immobilized
613
enzyme, 1 % (w/v) chitosan solution, 4 mL/min substrate pumping rate. B-D: GPC
614
analysis of three different chitooligosaccharide products. (B) the low molecular weight
615
chitooligosaccharide; (C) the medium molecular weight chitooligosaccharide; (D) the
616
high molecular weight chitooligosaccharide. Horizontal axis: molecular weight
617
logarithm; Vertical axis: the value of the vertical axis at a point on the curve is related
618
to the content of the sample molecules at each molecular weight.
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Table 1 Gene sources in this study gene
gene source
reference
GsCsn46A
chitosanase (GsCsn46A) from G. sunshinyii YC6258
27
BaCsn46A
chitosanase (BaCsn46A) from B. amyloliquefaciens YX-01
29
CBM56
β-1,3-glucan binding module (CBM56) from P. barengoltzii
26
CAU904
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Table 2 Primers used in this study Target gene
Prime
Sequence (5’-3’)
r CBM56
F1
CGCCATATGTTAGCTGATTTCACTCAAGGAGCGGA
R1-Gs
CTGCTGAGCGGTCAGCTGAGCCGAAGGTTCCGGATCGGGT T
GsCsn46
F2-Gs
A
CGAAGGTTCCGGATCGGGTTGGCTCAGCTGACCGCTCAGC A
R2-Gs
CCGCTCGAGTTAACGGATCGGCAGGATGAAAA
CBM56
R3-Ba
CGGCCCGACTTATTCCTAGTCCGAAGGTTCCGGATCGGGTT
BaCsn46
F4-Ba
CGAAGGTTCCGGATCGGGTTGCCGGGCTGAATAAGGATC
R4-Ba
CCGCTCGAGTTATTGAATAGTGAAATTACCGTATTCGC
A
The restriction sites of Nde I and Xho I are highlighted in the box, while the overlapping regions are underlined.
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