Production of Thermophilic Chitinase by Paenibacillus sp. TKU052 by Bioprocessing of Chitinous Fishery Wastes and Its Application in N-acetyl-D-glucosamine Production

The bioprocessing of chitinous fishery wastes (CFWs) to chitinases through fermentation approaches has gained importance owing to its great benefits in reducing the enzyme production cost, and utilizing chitin waste. In this work, our study of the chitinase production of Paenibacillus sp. TKU052 in the presence of different kinds of CFWs revealed a preference for demineralized crab shells powder (deCSP); furthermore, a 72 kDa chitinase was isolated from the 0.5% deCSP-containing medium. The Paenibacillus sp. TKU052 chitinase displayed maximum activity at 70 °C and pH 4–5, while Zn2+, Fe3+, Triton X-100, Tween 40, and SDS exerted a negative effect on its activity, whereas Mn2+ and 2-mercaptoethanol were found to potentially enhance the activity. Among various kinds of polysaccharide, Paenibacillus sp. TKU052 chitinase exhibited the best catalytic activity on colloidal chitin (CC) with Km = 9.75 mg/mL and Vmax = 2.43 μmol/min. The assessment of the hydrolysis of CC and N-acetyl chitooligosaccharides revealed that Paenibacillus sp. TKU052 chitinase possesses multiple catalytic functions, including exochitinase, endochitinase, and N-acetyl-β-D-glucosaminidase activities. Finally, the combination of Paenibacillus sp. TKU052 chitinase and Streptomyces speibonae TKU048 N-acetyl-β-D-glucosaminidase could efficiently convert CC to N-acetyl-D-glucosamine (GlcNAc) with a production yield of 94.35–98.60% in 12–24 h.


Introduction
Chitin is a linear polysaccharide made of N-acetyl-D-glucosamine (GlcNAc) units linked through the β-1,4-glycosidic linkages [1,2]. In nature, it is the second most abundant polysaccharide after cellulose, and is also a structural constituent of crustacean exoskeletons, squid pens, fungal cell walls, etc. [3,4]. In the fishery industry, a massive amount of chitinous fishery wastes (CFWs) are generated from shrimp shells, crab shells, and squid pens, and may cause serious environmental pollution if they are not utilized effectively [5]. The chitin extraction process from CFWs commonly involves chemical deproteinization (using strong alkalis), demineralization (using strong acids), and bleaching (using oxidants) [6], thereby potentially releasing hazardous and protein-rich wastewater. On the other hand, CFWs mainly contain chitin and proteins, which can directly serve as nutrient components for microbial fermentation [7][8][9][10]. This "green technique" has shown great potential owing to the capability of microbes in utilizing CFWs as appropriate C/N sources for producing various metabolites, such as enzymes [11][12][13][14], antioxidants [15], enzymes inhibitors [16,17], antimicrobial agents [18], etc. Concurrently, the bioremediation and chitin waste utilization aspects may be resolved through this technique [19].

Chitinase Assay
The activity of Paenibacillus sp. TKU052 chitinase was determined using CC (1%) as the substrate. Briefly, 200 µL of the reaction solution, consisting of 100 µL of CC (prepared in 100 mM sodium acetate buffer, pH = 5) and 100 µL of the enzyme, was incubated at 37 • C for 30 min. Then, 750 µL of DNS reagent was added to the reaction solution, and the mixture was heated at 100 • C for 10 min. The resulting solution was centrifuged at 13,000 rpm (10 min) to obtain a clear liquid. Then, 250 µL of the liquid was transferred to a 96-well plate and quantified by a microplate reader (Bio-Rad, Hercules, CA, USA) at 515 nm. GlcNAc was used as the reference to calculate the amount of reducing sugar in the sample solution. One chitinase unit is the amount of enzyme that catalyzes the degradation of CC to liberate 1 µM of reducing sugar at 37 • C in 1 min.

Chitinase Production and Purification
Paenibacillus sp. TKU052 was grown in a culture medium consisting of 0.05% MgSO 4 , 0.1% K 2 HPO 4 , and 1% of each CFW type (deCSP, SHP, deSSP, SSP, and SPP) or chitin at the following cultural conditions: culture temperature of 37 • C and shaking speed of 150 rpm. The culture medium was tested for its chitinase activity every 24 h. Different amounts of deCSP, from 0.25% to 3%, were also used to assess the suitable C/N concentration for chitinase production at 37 • C and 150 rpm.
One liter of Paenibacillus sp. TKU052 culture supernatant obtained from 5-day old culture medium was used for purifying the chitinase produced. (NH 4 ) 2 SO 4 was added to the supernatant for 60% saturation, and the mixture was kept at 4 • C overnight. The precipitate was obtained by centrifugation (4 • C, 13,000 rpm, 30 min), resuspended in 25 mM sodium phosphate buffer (pH = 5.8), dialyzed against a similar buffer, and loaded onto a Macro-Prep High S column. The elution was performed with the NaCl gradients of 0-0.1 M and 0.1-1 M. The activity fraction was concentrated by means of the freezedrying method and loaded into a Hitachi Chromaster HPLC (High-Performance Liquid Chromatography, Hitachi, Tokyo, Japan) apparatus coupled with KW-802.5 column under the following conditions: solvent: 25 mM sodium phosphate buffer (pH = 5.8); flow rate: 0.6 mL/min; sample volume: 50 µL; column temperature: 20 • C; ultraviolet detector at the wavelength of 280 nm. The molecular weight of the Paenibacillus sp. TKU052 chitinase was determined according to the Laemmli method using a 10% resolving gel [9]. Zymogram of Paenibacillus sp. TKU052 chitinase was performed on 0.05% chitin acrylamide gel and using 0.01% Congo Red as the staining solution [30].

Effect of Temperature and pH
The optimum temperature for Paenibacillus sp. TKU052 chitinase was assayed in the range of 30-80 • C. The optimum pH for the enzyme was assayed in the range of pH = 3-10 using various buffers at the same concentration of 50 mM. The buffers included Na 2 CO 3 -NaHCO 3 buffer (pH = 9-10), sodium phosphate buffer (pH = 6-8), sodium acetate buffer (pH = 4-5), and glycine-HCl buffer (pH = 3). The thermal and pH stabilities of Paenibacillus sp. TKU052 chitinase was based on the residual activity after treating the enzyme at different temperatures or pH for 1 h. The residual activity was measured at pH = 5 and 37 • C following the method described above.

The Pattern of Hydrolysis
CC and N-acetyl COSs with the degrees of polymerization (DP) = 2-6 were used as the enzyme substrates to explore the hydrolysis mechanism of Paenibacillus sp. TKU052 chitinase. At different time intervals, the reaction solution was analyzed by the HPLC process described in Section 2.9.

Production of GlcNAc
The reaction solution (20 mL), consisting of 1% CC, 100 mM sodium acetate buffer (pH 5), and 10 U/mL of Paenibacillus sp. TKU052 chitinase or 10 U/mL of S. speibonae TKU048 N-acetyl-β-D-glucosaminidase or 5 U/mL of Paenibacillus sp. TKU052 chitinase combined with 5 U/mL of S. speibonae TKU048 N-acetyl-β-D-glucosaminidase were incubated at 60 • C and a shaking speed of 150 rpm. At different time intervals, 0.2 mL of the solution was withdrawn to quantify the concentration of GlcNAc and N-acetyl COSs by the HPLC method (described in Section 2.9). The GlcNAc yield was calculated using the formula: GlcNAc yield = Amount of GlcNAc/Amount of substrate (%) (1)

HPLC Analysis
GlcNAc and N-acetyl COSs were analyzed by HPLC using a Hitachi Chromaster HPLC apparatus coupled with a KS-802 column under the following conditions: solvent: water; flow rate: 0.6 mL/min; sample volume: 20 µL; column temperature: 80 • C; ultraviolet detector at the wavelength of 205 nm.

Proton Nuclear Magnetic Resonance ( 1 H-NMR) Analysis
1 H-NMR analysis was performed using a Bruker 600 Ultrashield NMR spectrophotometer (Bruker, New Taipei City, Taiwan). The solvent used was D 2 O and the chemical shifts are shown in ppm (parts per million).

Chitinase Production
Paenibacillus sp. TKU052 was isolated from the soil of Tamkang University using SPP-containing medium and was found to be closely related to P. tyrfis MSt1 (99.3%) and P. elgii SD17 (99.3%) according to 16S rDNA partial base sequence analysis [9]. In the current work, Paenibacillus sp. TKU052 created a zone of hydrolysis on the CC plate after three days of incubation (Figure 1), indicating that this strain secretes extracellular chitinolytic enzymes to degrade the surrounding CC. The chitinase-producing ability of P. elgii and P. tyrfis species is rarely reported [32,33]. More so, none of these species have been evaluated for their chitinase production on a medium containing CFWs and the application of their enzymes in GlcNAc production. As such, this work may provide an insight into the conversion of CFWs to produce chitinase by Paenibacillus sp. TKU052 strain, as well as the biochemical properties and the application of the obtained chitinase in GlcNAc production.
for their chitinase production on a medium containing CFWs and the application of their enzymes in GlcNAc production. As such, this work may provide an insight into the conversion of CFWs to produce chitinase by Paenibacillus sp. TKU052 strain, as well as the biochemical properties and the application of the obtained chitinase in GlcNAc production. The chitinase production of Paenibacillus sp TKU052 on a medium containing CFWs as the unique C/N source was explored. The chitinous materials used were deCSP, deSSP, SPP, SHP, SSP, and chitin. In addition, nutrient broth, a non-chitinous medium, was also used to test the enzyme productivity of Paenibacillus sp TKU052. As shown in Figure 2a, the maximal chitinase activity of deCSP-supplemented medium was 0.53 (day 5), 0.55 (day 6), and 0.55 U/mL (day 7), that of deSSP-supplemented medium was 0.32 U/mL (day 7); that of SPP-supplemented medium was 0.29 U/mL (day 4); that of SHP-supplemented medium was 0.30 U/mL (day 4); that of SSP-supplemented medium was 0.29 U/mL (day 5); that of chitin-supplemented medium was 0.36 U/mL (day 7); and finally, that of nutrient broth medium was 0.07 (day 4) and 0.06 U/mL (day 5). According to the result, Paenibacillus sp. TKU052 exhibited higher chitinase productivity toward chitin-containing media, suggesting that chitin may be a key factor for chitinase production by Paenibacillus sp. TKU052. Among those, the highest chitinase productivity of Paenibacillus sp. TKU052 was found in the deCSP-supplemented medium. Chitin, especially in colloidal form, is a widely used supplement to the chitinase-producing medium as an inducer or a nutrient source. Chemical treatment is a mandatory step to produce chitin from chitinous materials, thereby possibly leading to environmental pollution and increased production cost of the processes using chitin [34,35]. Therefore, CFWs are being assessed as an effective alternative for the cost-effective production of microbial chitinases. In addition, the use of chitinous wastes for the production of microbial chitinases by various bioprocesses is regarded as being a significant part of the utilization of these waste sources. In this study, deCSP exhibited good results and was chosen as the best C/N source for chitinase production by Paenibacillus sp. TKU052 and further analyses. The chitinase production of Paenibacillus sp TKU052 on a medium containing CFWs as the unique C/N source was explored. The chitinous materials used were deCSP, deSSP, SPP, SHP, SSP, and chitin. In addition, nutrient broth, a non-chitinous medium, was also used to test the enzyme productivity of Paenibacillus sp TKU052. As shown in Figure 2a, the maximal chitinase activity of deCSP-supplemented medium was 0.53 (day 5), 0.55 (day 6), and 0.55 U/mL (day 7), that of deSSP-supplemented medium was 0.32 U/mL (day 7); that of SPP-supplemented medium was 0.29 U/mL (day 4); that of SHP-supplemented medium was 0.30 U/mL (day 4); that of SSP-supplemented medium was 0.29 U/mL (day 5); that of chitin-supplemented medium was 0.36 U/mL (day 7); and finally, that of nutrient broth medium was 0.07 (day 4) and 0.06 U/mL (day 5). According to the result, Paenibacillus sp. TKU052 exhibited higher chitinase productivity toward chitin-containing media, suggesting that chitin may be a key factor for chitinase production by Paenibacillus sp. TKU052. Among those, the highest chitinase productivity of Paenibacillus sp. TKU052 was found in the deCSP-supplemented medium. Chitin, especially in colloidal form, is a widely used supplement to the chitinase-producing medium as an inducer or a nutrient source. Chemical treatment is a mandatory step to produce chitin from chitinous materials, thereby possibly leading to environmental pollution and increased production cost of the processes using chitin [34,35]. Therefore, CFWs are being assessed as an effective alternative for the cost-effective production of microbial chitinases. In addition, the use of chitinous wastes for the production of microbial chitinases by various bioprocesses is regarded as being a significant part of the utilization of these waste sources. In this study, deCSP exhibited good results and was chosen as the best C/N source for chitinase production by Paenibacillus sp. TKU052 and further analyses.
The effect of the deCSP amount on chitinase productivity of Paenibacillus sp. TKU052 was examined over a range of 0.25-3%, and the results are shown in Figure 2b. The maximal chitinase activity of 0.25% deCSP-supplemented medium was 0.43 U/mL (day 5); of 0.5% deCSP-supplemented medium was 0.59 U/mL (day 5); that of 1% deCSP-supplemented medium was 0.54 U/mL (day 5); that of 2% deCSP-supplemented medium was 0.47 U/mL (day 7); and that of 3% deCSP-supplemented medium was 0.26 U/mL (day 6). The results indicate that 0.5% deCSP is the most appropriate C/N amount for chitinase production by Paenibacillus sp. TKU052.
With its abundance, wasted crab shell is of interest for the preparation of various bioactive compounds, such as chitin, protease, prodigiosin, antioxidant, antidiabetic and anticancer agents [9,36]. In this study, this kind of CFW was also found to be the best C/N source for chitinase production by Paenibacillus sp. TKU052. The effect of the deCSP amount on chitinase productivity of Paenibacillus sp. TKU052 was examined over a range of 0.25-3%, and the results are shown in Figure 2b. The maximal chitinase activity of 0.25% deCSP-supplemented medium was 0.43 U/mL (day 5); of 0.5% deCSP-supplemented medium was 0.59 U/mL (day 5); that of 1% deCSP-supplemented medium was 0.54 U/mL (day 5); that of 2% deCSP-supplemented medium was 0.47 U/mL (day 7); and that of 3% deCSP-supplemented medium was 0.26 U/mL (day 6).
The results indicate that 0.5% deCSP is the most appropriate C/N amount for chitinase production by Paenibacillus sp. TKU052.
With its abundance, wasted crab shell is of interest for the preparation of various bioactive compounds, such as chitin, protease, prodigiosin, antioxidant, antidiabetic and anticancer agents [9,36]. In this study, this kind of CFW was also found to be the best C/N source for chitinase production by Paenibacillus sp. TKU052.

Chitinase Purification
The supernatant of a 5-day old culture of Paenibacillus sp. TKU052 grown using 0.5% deCSP-supplemented medium was obtained by centrifugation. Chitinase in the supernatant was purified as follows: 60% (NH4)2SO4 precipitation, cation exchange chromatography using Macro-Prep High S resin, and size exclusion chromatography using HPLC coupling with KW-802.5 column. The crude enzyme was loaded onto a Macro-Prep High S column equilibrated by sodium phosphate buffer (25 mM, pH = 5.8). According to the enzyme elution profile, only one chitinase peak was eluted at 10-70 mM NaCl (fractions 129-166) (Figure 3a). The HPLC profile of the chitinase fraction obtained from cation exchange chromatography is shown in Figure 3b. The fraction containing the chitinase activity was eluted at a retention time of 13.3 min. The fractions that exhibited the chitinase activity were pooled and analyzed by the HPLC system using a KW-802.5 column. Accordingly, only one protein peak at a retention time of 13.3 min was observed, suggesting that the obtained chitinase was homogeneous ( Figure 3c). The result of the purification of Paenibacillus sp. TKU052 chitinase is summarized in Table 1. Enzyme purity was estimated to be 19.47-fold greater than that of the cultural supernatant. The purified chitinase had a specific activity of 2.55 U/mg, with a yield of about 4.01%.

Chitinase Purification
The supernatant of a 5-day old culture of Paenibacillus sp. TKU052 grown using 0.5% deCSP-supplemented medium was obtained by centrifugation. Chitinase in the supernatant was purified as follows: 60% (NH 4 ) 2 SO 4 precipitation, cation exchange chromatography using Macro-Prep High S resin, and size exclusion chromatography using HPLC coupling with KW-802.5 column. The crude enzyme was loaded onto a Macro-Prep High S column equilibrated by sodium phosphate buffer (25 mM, pH = 5.8). According to the enzyme elution profile, only one chitinase peak was eluted at 10-70 mM NaCl (fractions 129-166) (Figure 3a). The HPLC profile of the chitinase fraction obtained from cation exchange chromatography is shown in Figure 3b. The fraction containing the chitinase activity was eluted at a retention time of 13.3 min. The fractions that exhibited the chitinase activity were pooled and analyzed by the HPLC system using a KW-802.5 column. Accordingly, only one protein peak at a retention time of 13.3 min was observed, suggesting that the obtained chitinase was homogeneous (Figure 3c). The result of the purification of Paenibacillus sp. TKU052 chitinase is summarized in Table 1. Enzyme purity was estimated to be 19.47-fold greater than that of the cultural supernatant. The purified chitinase had a specific activity of 2.55 U/mg, with a yield of about 4.01%.

Effect of Temperature and pH
The temperature was applied in the range of 30-80 °C to explore the influence of temperature on Paenibacillus sp. TKU052 chitinase activity. The optimal temperature of Paenibacillus sp. TKU052 chitinase was found to be 70 °C and it was stable up to 60 °C (Figure 5a). Due to the outstanding functioning at temperatures ≥ 50 °C, Paenibacillus sp. TKU052 chitinase could be categorized as a thermophilic enzyme. By far, thermophilic chitinolytic enzymes have gained the most attention as they can tolerate and act at elevated temperatures. The reaction at a high temperature can provide the benefits of enhancing the solubility/dispersibility of compounds and preventing microbial contamination [44]. The thermophilic enzymes have been examined for various aspects, including the source of the enzyme, the hydrolysis mechanism of the enzyme at a high temperature, genetic engineering, and industrial applications. Accordingly, several Paenibacillus species strains have been found to be capable of producing thermophilic chitinolytic enzymes, with promising potential in the production of chitooligosaccharides and GlcNAc, such as P. barengoltzii chitinase [2], P. thermoaerphilus TC22-2b chitinase [40], P. mucilaginosus TKU032 chitosanase [45], and Paenibacillus sp. 1794 chitosanase [46]. In this study, Paenibacillus sp. TKU052 chitinase exhibited a comparable or even better thermal stability and thermal activity than most of Paenibacillus chitinases/chitosanases [1,33,40,46,47], indicating that this enzyme may be useful for applications in which a thermophilic chitinase is prioritized.

Effect of Temperature and pH
The temperature was applied in the range of 30-80 • C to explore the influence of temperature on Paenibacillus sp. TKU052 chitinase activity. The optimal temperature of Paenibacillus sp. TKU052 chitinase was found to be 70 • C and it was stable up to 60 • C (Figure 5a). Due to the outstanding functioning at temperatures ≥ 50 • C, Paenibacillus sp. TKU052 chitinase could be categorized as a thermophilic enzyme. By far, thermophilic chitinolytic enzymes have gained the most attention as they can tolerate and act at elevated temperatures. The reaction at a high temperature can provide the benefits of enhancing the solubility/dispersibility of compounds and preventing microbial contamination [44]. The thermophilic enzymes have been examined for various aspects, including the source of the enzyme, the hydrolysis mechanism of the enzyme at a high temperature, genetic engineering, and industrial applications. Accordingly, several Paenibacillus species strains have been found to be capable of producing thermophilic chitinolytic enzymes, with promising potential in the production of chitooligosaccharides and GlcNAc, such as P. barengoltzii chitinase [2], P. thermoaerphilus TC22-2b chitinase [40], P. mucilaginosus TKU032 chitosanase [45], and Paenibacillus sp. 1794 chitosanase [46]. In this study, Paenibacillus sp. TKU052 chitinase exhibited a comparable or even better thermal stability and thermal activity than most of Paenibacillus chitinases/chitosanases [1,33,40,46,47], indicating that this enzyme may be useful for applications in which a thermophilic chitinase is prioritized.

Effect of Various Ions and Chemicals
The activity of Paenibacillus sp. TKU052 chitinase incubated with various chemicals was examined, and the results are shown in Table 2. Among the metal ions, Fe 2+ , Ca 2+ , Ba 2+ , Mg 2+ , Cu 2+ did not significantly affect the activity of Paenibacillus sp. TKU052 chitinase, while Fe 3+ and Zn 2+ showed an inhibitory effect by reducing the enzyme activity to 26.72% and 59.51%, respectively, of its initial activity. The negative effect of heavy metal ions may be due to their ability to destroy the tertiary structure of the protein, thereby inactivating the enzyme [1]. In contrast, Mn 2+ showed an enhancing effect on the activity of Paenibacillus sp. TKU052 chitinase (relative activity of 142.57%), similar to its positive effect on P. chitinolyticus UMBR 0002 chitinase [1] and Paenibacillus sp. TKU047 chitosanase [30]. Surfactants such as SDS, Triton X-100, and Tween 40 showed a negative effect on Paenibacillus sp. TKU052 chitinase (relative activity of 28.84%, 78.96%, and 65.71%, respectively), whereas Tween 20 did not have a significant effect. Paenibacillus sp. TKU052 chitinase was not significantly affected by EDTA, a metal ion chelator, indicating that the activity of the enzyme is not dependent on metal ions. Interestingly, in the presence of 2-ME, the activity of Paenibacillus sp. TKU052 chitinase significantly increased to 129.70% of its initial activity, demonstrating that cysteine residues are not involved in the formation of its catalytic center [52]. Earlier studies have reported strong inhibition of several chitinases by 2-ME, such as ChiA-Pt70 from P. timonensis LK-DZ15 [38] and CHI from P. chitinolyticus UMBR 0002 [1].

Effect of Various Ions and Chemicals
The activity of Paenibacillus sp. TKU052 chitinase incubated with various chemicals was examined, and the results are shown in Table 2. Among the metal ions, Fe 2+ , Ca 2+ , Ba 2+ , Mg 2+ , Cu 2+ did not significantly affect the activity of Paenibacillus sp. TKU052 chitinase, while Fe 3+ and Zn 2+ showed an inhibitory effect by reducing the enzyme activity to 26.72% and 59.51%, respectively, of its initial activity. The negative effect of heavy metal ions may be due to their ability to destroy the tertiary structure of the protein, thereby inactivating the enzyme [1]. In contrast, Mn 2+ showed an enhancing effect on the activity of Paenibacillus sp. TKU052 chitinase (relative activity of 142.57%), similar to its positive effect on P. chitinolyticus UMBR 0002 chitinase [1] and Paenibacillus sp. TKU047 chitosanase [30]. Surfactants such as SDS, Triton X-100, and Tween 40 showed a negative effect on Paenibacillus sp. TKU052 chitinase (relative activity of 28.84%, 78.96%, and 65.71%, respectively), whereas Tween 20 did not have a significant effect. Paenibacillus sp. TKU052 chitinase was not significantly affected by EDTA, a metal ion chelator, indicating that the activity of the enzyme is not dependent on metal ions. Interestingly, in the presence of 2-ME, the activity of Paenibacillus sp. TKU052 chitinase significantly increased to 129.70% of its initial activity, demonstrating that cysteine residues are not involved in the formation of its catalytic center [52]. Earlier studies have reported strong inhibition of several chitinases by 2-ME, such as ChiA-Pt70 from P. timonensis LK-DZ15 [38] and CHI from P. chitinolyticus UMBR 0002 [1]. The data are presented as mean ± standard deviation.

GlcNAc Production
The synergy between chitinase with both exochitinase and endochitinase activities and N-acetyl-β-D-glucosaminidase may be required for the complete degradation of chitin to GlcNAc [20]. According to the previous experiment, Paenibacillus sp. TKU052 chitinase could rapidly degrade CC to form (GlcNAc)2 and GlcNAc. As a result, this enzyme

GlcNAc Production
The synergy between chitinase with both exochitinase and endochitinase activities and N-acetyl-β-D-glucosaminidase may be required for the complete degradation of chitin to GlcNAc [20]. According to the previous experiment, Paenibacillus sp. TKU052 chitinase could rapidly degrade CC to form (GlcNAc) 2 and GlcNAc. As a result, this enzyme can effectively assist the N-acetyl-β-D-glucosaminidases to hydrolyze chitin and produce GlcNAc. In this study, we used a combination of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase to assess the possibility of producing GlcNAc from CC. The products of the hydrolysis process were analyzed by the HPLC method, and the results are presented in Figure 7. In the first hour, GlcNAc and (GlcNAc) 2 were generated at the concentrations of 3.44 and 2.58 mg/mL, respectively. In the next few hours, the concentration of (GlcNAc) 2 significantly decreased and reduced to zero after 12 h, whereas the concentration of GlcNAc gradually increased over time and reached its maximum value after 24 h (9.86 mg/mL). According to the estimates, the GlcNAc production process could achieve a yield of 98.60% within a reaction time of 24 h. In addition, 9.44 mg/mL of GlcNAc, indicating a production yield of 94.35%, without Nacetyl COSs could be observed after a reaction time of 12 h. In addition, we also explored the hydrolysis processes of CC using Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase separately. Paenibacillus sp. TKU052 chitinase could not completely degrade (GlcNAc) 2 , and the reaction solution still contained both (GlcNAc) 2 and GlcNAc at 0.83 and 9.03 mg/mL concentrations, respectively, (after 240 h). In the case of S. speibonae TKU048 N-acetyl-β-D-glucosaminidase, 6.10 mg/mL of GlcNAc without N-acetyl COSs was obtained from the CC hydrolysis with a 60.99% yield after 96 h. This indicates that a novel combination of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase could efficiently improve the GlcNAc production from CC. The efficiency of the present process was compared with those in earlier reports (Table 4). Among them, the combination of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase reveals a comparable result with a short required reaction time (12-24 h) and high GlcNAc production yield (94. 35-98.60%). In addition, the absence of N-acetyl COSs in the final reaction solution could also simplify the GlcNAc purification step. In this study, GlcNAc was obtained from the chitin hydrolysate solution by one-step purification using HPLC coupled with a KS-802 column. The HPLC result revealed only one peak at a retention time of 14.7 min (Figure 8a), indicating that the molecular weight of the product is similar to that of the GlcNAc standard. The obtained GlcNAc was analyzed by 1 H-NMR spectroscopy, and as shown in Figure 8b, the obtained GlcNAc had a similar 1 H-NMR profile as that of the profile of commercial GlcNAc from Sigma (St. Louis, MO, USA), confirming the purity of the product. This result, therefore, provides a promising enzymatic method for the production of GlcNAc from CC. can effectively assist the N-acetyl-β-D-glucosaminidases to hydrolyze chitin and produce GlcNAc. In this study, we used a combination of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase to assess the possibility of producing GlcNAc from CC. The products of the hydrolysis process were analyzed by the HPLC method, and the results are presented in Figure 7. In the first hour, GlcNAc and (GlcNAc)2 were generated at the concentrations of 3.44 and 2.58 mg/mL, respectively. In the next few hours, the concentration of (GlcNAc)2 significantly decreased and reduced to zero after 12 h, whereas the concentration of GlcNAc gradually increased over time and reached its maximum value after 24 h (9.86 mg/mL). According to the estimates, the GlcNAc production process could achieve a yield of 98.60% within a reaction time of 24 h. In addition, 9.44 mg/mL of GlcNAc, indicating a production yield of 94.35%, without N-acetyl COSs could be observed after a reaction time of 12 h. In addition, we also explored the hydrolysis processes of CC using Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 Nacetyl-β-D-glucosaminidase separately. Paenibacillus sp. TKU052 chitinase could not completely degrade (GlcNAc)2, and the reaction solution still contained both (GlcNAc)2 and GlcNAc at 0.83 and 9.03 mg/mL concentrations, respectively, (after 240 h). In the case of S. speibonae TKU048 N-acetyl-β-D-glucosaminidase, 6.10 mg/mL of GlcNAc without Nacetyl COSs was obtained from the CC hydrolysis with a 60.99% yield after 96 h. This indicates that a novel combination of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase could efficiently improve the GlcNAc production from CC. The efficiency of the present process was compared with those in earlier reports (Table 4). Among them, the combination of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-D-glucosaminidase reveals a comparable result with a short required reaction time (12-24 h) and high GlcNAc production yield (94. 35-98.60%). In addition, the absence of N-acetyl COSs in the final reaction solution could also simplify the GlcNAc purification step. In this study, GlcNAc was obtained from the chitin hydrolysate solution by one-step purification using HPLC coupled with a KS-802 column. The HPLC result revealed only one peak at a retention time of 14.7 min (Figure 8a), indicating that the molecular weight of the product is similar to that of the GlcNAc standard. The obtained GlcNAc was analyzed by 1 H-NMR spectroscopy, and as shown in Figure 8b, the obtained GlcNAc had a similar 1 H-NMR profile as that of the profile of commercial Glc-NAc from Sigma (St. Louis, MO, USA), confirming the purity of the product. This result, therefore, provides a promising enzymatic method for the production of GlcNAc from CC.

Conclusions
The exploitation of CFWs to obtain high-quality products through microbial fermentation is increasing gradually. In this study, deCSP was found to be the best potential C/N source for chitinase production by Paenibacillus sp. TKU052 among several CFWs, and a chitinase with an MW of 72 kDa was purified from the 0.5% deCSP-containing medium. Interestingly, the pure chitinase exhibited some valuable properties, such as high catalytic function at acidic pH and elevated-temperature conditions (pH = 4-5, and 70 °C), and can also carry out multi-functional (exochitinase, endochitinase, and N-acetyl-β-D-glucosaminidase) activities. These characteristics make Paenibacillus sp. TKU052 chitinase a promising candidate for the saccharification of chitin under mild conditions. Remarkably, the coupling of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-Dglucosaminidase could efficiently improve the GlcNAc production from CC with a yield of 94.35-98.60% in 12-24 h. As a result, the bioprocessing of deCSP by Paenibacillus sp. TKU052 may be potentially useful in producing chitinase as a tool for the bioconversion of chitin to GlcNAc.

Conclusions
The exploitation of CFWs to obtain high-quality products through microbial fermentation is increasing gradually. In this study, deCSP was found to be the best potential C/N source for chitinase production by Paenibacillus sp. TKU052 among several CFWs, and a chitinase with an MW of 72 kDa was purified from the 0.5% deCSP-containing medium. Interestingly, the pure chitinase exhibited some valuable properties, such as high catalytic function at acidic pH and elevated-temperature conditions (pH = 4-5, and 70 • C), and can also carry out multi-functional (exochitinase, endochitinase, and N-acetyl-β-Dglucosaminidase) activities. These characteristics make Paenibacillus sp. TKU052 chitinase a promising candidate for the saccharification of chitin under mild conditions. Remarkably, the coupling of Paenibacillus sp. TKU052 chitinase and S. speibonae TKU048 N-acetyl-β-Dglucosaminidase could efficiently improve the GlcNAc production from CC with a yield of 94.35-98.60% in 12-24 h. As a result, the bioprocessing of deCSP by Paenibacillus sp. TKU052 may be potentially useful in producing chitinase as a tool for the bioconversion of chitin to GlcNAc.

Data Availability Statement:
The data presented in this study are available on request from the corresponding author.

Conflicts of Interest:
The authors declare no conflict of interest.