Employing Cationic Kraft Lignin as Additive to Enhance Enzymatic Hydrolysis of Corn Stalk

A water-soluble cationic kraft lignin (named JLQKL50), synthesized by combining quaternization and crosslinking reactions, was used as an additive to enhance the enzymatic hydrolysis of dilute-alkali-pretreated corn stalk. The chemical constitution of JLQKL50 was investigated by Fourier transform infrared spectroscopy, 1H nuclear magnetic resonance (NMR) and 13C NMR spectroscopy, and elemental analysis. The enzymatic hydrolysis efficiency of corn stalk at solid content of 10% (w/v) was significantly improved from 70.67% to 78.88% after 24 h when JLQKL50 was added at a concentration of 2 g/L. Meanwhile, the enzymatic hydrolysis efficiency after 72 h reached 91.11% with 10 FPU/g of cellulase and 97.92% with 15 FPU/g of cellulase. In addition, JLQKL50 was found capable of extending the pH and temperature ranges of enzymatic hydrolysis to maintain high efficiency (higher than 70%). The decrease in cellulase activity under vigorous stirring with the addition of JLQKL50 was 17.4%, which was much lower than that (29.7%) without JLQKL50. The addition of JLQKL50 reduced the nonproductive adsorption of cellulase on the lignin substrate and improved the longevity, dispersity, and stability of the cellulase by enabling electrostatic repulsion. Therefore, the enzymatic hydrolysis of the corn stalk was enhanced. This study paves the way for the design of sustainable lignin-based additives to boost the enzymatic hydrolysis of lignocellulosic biomass.


Introduction
Over the past few decades, significant economic growth around the world has increased the demand for energy and chemicals derived from renewable resources because of the limited sources of fossil fuels and their serious environmental problems [1,2]. In this context, lignocellulosic biomass (LCB) has been regarded as the most promising source of renewable fuel and chemicals and a potential material to reduce the global reliance on fossil fuels [3,4]. LCB is the most abundant renewable non-grain feedstock for sugar production and contains essential platform molecules to produce a wide variety of fuels and chemicals by fermentation or chemical processing [5][6][7]. One of the mandatory steps in the biorefinery of LCB is the enzymatic hydrolysis of pretreated LCB to produce sugar syrups. The economic feasibility of the biorefinery of LCB is highly restricted by the efficiency of enzymatic hydrolysis [8].
Considerable effort has been devoted to improving the efficiency of enzymatic hydrolysis [9,10]. The following strategies are often used to enhance the efficiency of the enzymatic hydrolysis of lignocellulose: (1) using pretreatment methods to overcome the obstinacy of lignocellulose biomass [11]; (2) adding beneficial additives during enzymatic hydrolysis; (3) screening microorganisms with high cellulase production rates; (4) using enzymes prepared with activities complementary to cellulase; (5) regulating the composition 2.2. Synthesis of JLQKL 50 JLQKL 50 was synthesized by a two-step modification reaction of KL, in which the quaternization method as reported in the literature was used [25][26][27]. First, a quantitative 25% solution of KL was weighed in a four-necked flask and heated up to 85 • C in a water bath (HH-W0-5L, China), and CHPTMAC was added dropwise using a peristaltic pump, where the mass ratio of KL to CHPTMAC was 2:1. A quantitative 50% sodium hydroxide solution was added to maintain the pH of the reaction above 11 for 5 h. The obtained and cooled QKL 50 solution was weighed in a four-necked flask and heated up to 45 • C with a water bath. PEGDGE was added to the flask dropwise by using a peristaltic pump, where the mass ratio of QKL 50 to PEGDGE was 10:1 and the reaction was conducted for 4 h. The obtained JLQKL 50 solution was purified by dialysis using a dialysis bag with a cut-off molecular weight of 1000 Da, concentrated under reduced pressure and then freeze-dried. The reaction equation for the synthesis of JLQKL 50 is shown in Figure S1 (Supporting Information).

Enzymatic Hydrolysis of Corn Stalk
The pretreatment of corn stalk was performed according to the literature [28]. The corn stalk was accurately weighed into a four-necked flask, and 2% (w/v) NaOH solution was added to make the solid-liquid ratio 1:20, and it was placed in a water bath at 80 • C for 2 h. After pretreatment, the solid was separated from the liquid using a filtration method, which was performed with a ceramic Büchner funnel (200 mm), suction flask (Sichuan Shubo (Group) Co., Ltd., Chongzhou, China), and recirculating water vacuum pump (Zhengzhou Great Wall Technology Industry and Trade Co., Ltd., Zhengzhou, China). The residue was washed with deionized water to a neutral pH and dried in an oven at 60 • C. Component analysis of the pretreated corn stalk was performed according to the method of the National Renewable Energy Laboratory [29], and the cellulose content of the pretreated corn stalk was found to be 63.19%, hemicellulose content 11.17%, and acid insoluble lignin 6.15%.
Pretreated corn stalk (2 g) was placed in a 100 mL blue-capped bottle, and 20 mL of acetic acid-sodium acetate buffer at pH 4.8, cellulase with 10 FPU/g of substrate, and 2 g/L additive were added successively. No additive was added to the control group. The blue-capped bottles were placed in a shaker (IS-RDS6T, Suzhou Jiemei Electronic Co., Ltd., Suzhou, China) at 50 • C and 200 rpm for enzymatic hydrolysis. At different intervals, such as 6, 12, 24, 48, and 72 h, 200 µL of each sample was collected during the reaction, centrifuged at 10,000 r/min for 10 min, and diluted 10,000 times, and then the glucose Polymers 2023, 15, 1991 4 of 12 content was detected by ion chromatography. Enzymatic hydrolysis efficiency data were obtained from triplicate readings.

Analysis and Characterizations
The glucose concentrations in the enzymatic hydrolysis products were analyzed by ion chromatography on a Dionex™ CarboPac™ PA20 column with an injection volume of 25 µL and an eluent of 200 mmol/L sodium hydroxide solution and ultrapure water at a flow rate of 0.5 mL/min. The temperatures of the column and detector were maintained at 30 • C.
The enzymatic hydrolysis efficiency was calculated by the following equation: where Y C is the enzymatic hydrolysis efficiency, C g is the glucose concentration, V is the buffer volume, m c is the mass of cellulose in the pretreated corn stalk, and 0.9 is the conversion factor between cellulose and glucose. An organic elemental analyzer (Vario Micro, Elementar Analysensysteme GmbH, Frankfurt, Germany) was used in quantifying the percentages of carbon, hydrogen, nitrogen, and sulfur elements in lignin samples.
An FT-IR system (Tensor II, Bruker Optics, Ettlingen, Germany) was used to analyze the functional groups of lignin samples.
The zeta potential of lignin samples at different pH values was measured with a nanoparticle size and zeta potential analyzer (DLS) (Zetasizer Nano ZS90, Malvern Panalytical, Spectris, Shanghai, China). The measurement of the average size of cellulase in water with or without additive was also conducted on this instrument. The FT-IR analysis results of KL, PEGDGE, and JLQKL 50 are presented in Figure 1. Compared with the spectrum of KL, the spectrum of JLQKL 50 showed the characteristic peak of a C-N bond at 1416 cm −1 , and the stretching vibration peak of the alcoholic hydroxyl group at 1125 cm −1 was significantly enhanced. By contrast, the stretching vibration peak of the phenolic hydroxyl group at 1216 cm −1 was weakened [30]. These results suggested that the phenolic hydroxyl group in the lignin molecule was the reaction site for graft quaternization. The characteristic peaks at 753, 848, and 910 cm −1 corresponded to the epoxy group in PEGDGE and disappeared in JLQKL 50 [31]. In addition, a new C-O-C stretching vibration peak at 951 cm −1 appeared in JLQKL 50 [32], indicating the presence of the PEGDGE fragment in JLQKL 50 .

Results and Discussion
Table S1 (Supporting Information) shows the elemental compositions of KL and JLQKL 50 . The nitrogen content increased from 0.28% for KL to 2.165% for JLQKL 50 . The results indicated that quaternary ammonium groups were introduced to the lignin molecule, increasing the nitrogen content.

1 H NMR and 13 C NMR Analyses of KL and JLQKL 50
The 1 H-NMR spectra obtained for KL and JLQKL 50 are illustrated in Figure 2a. In the spectrum of KL, the signal peaks in the 8.0-6.0 ppm range could be attributed to the phenolic hydroxyl group proton on lignin and almost disappeared in the spectrum of JLQKL 50 , indicating the involvement of the phenolic hydroxyl group of the lignin molecule in the reaction [33]. The strong peaks between 3.8 and 3.5 ppm are attributed to the methyl proton (-CH 3 ) in lignin [33]. The chemical shifts of these two peaks were significantly enhanced Polymers 2023, 15, 1991 5 of 12 in the spectrum of JLQKL 50 after the introduction of quaternary ammonium groups on the lignin molecule. The sharp peak at 2.5 ppm was the solvent peak (DMSO-d6) [34,35].

1 H NMR and 13 C NMR Analyses of KL and JLQKL50
The 1 H-NMR spectra obtained for KL and JLQKL50 are illustrated in Figure 2a. In the spectrum of KL, the signal peaks in the 8.0-6.0 ppm range could be attributed to the phenolic hydroxyl group proton on lignin and almost disappeared in the spectrum of JLQKL50, indicating the involvement of the phenolic hydroxyl group of the lignin molecule in the reaction [33]. The strong peaks between 3.8 and 3.5 ppm are attributed to the methyl proton (-CH3) in lignin [33]. The chemical shifts of these two peaks were significantly enhanced in the spectrum of JLQKL50 after the introduction of quaternary ammonium groups on the lignin molecule. The sharp peak at 2.5 ppm was the solvent peak (DMSO-d6) [34,35]. Solid-state 13 C NMR is a widely used method for the investigation of the lignin structure. In this study, it was used to analyze the chemical structures of KL and JLQKL50. As seen in Figure 2b, all the characteristic peaks in the spectrum of KL were retained in the spectrum of JLQKL50. For example, a peak at 55 ppm was observed in both the KL and JLQKL50 spectra, which was the characteristic methoxy group of lignin [36]. In contrast to KL, JLQKL50 exhibited a strong peak at 70 ppm, which was the O-C-C-O repeating unit

1 H NMR and 13 C NMR Analyses of KL and JLQKL50
The 1 H-NMR spectra obtained for KL and JLQKL50 are illustrated in Figure 2a. In the spectrum of KL, the signal peaks in the 8.0-6.0 ppm range could be attributed to the phenolic hydroxyl group proton on lignin and almost disappeared in the spectrum of JLQKL50, indicating the involvement of the phenolic hydroxyl group of the lignin molecule in the reaction [33]. The strong peaks between 3.8 and 3.5 ppm are attributed to the methyl proton (-CH3) in lignin [33]. The chemical shifts of these two peaks were significantly enhanced in the spectrum of JLQKL50 after the introduction of quaternary ammonium groups on the lignin molecule. The sharp peak at 2.5 ppm was the solvent peak (DMSO-d6) [34,35]. Solid-state 13 C NMR is a widely used method for the investigation of the lignin structure. In this study, it was used to analyze the chemical structures of KL and JLQKL50. As seen in Figure 2b, all the characteristic peaks in the spectrum of KL were retained in the spectrum of JLQKL50. For example, a peak at 55 ppm was observed in both the KL and JLQKL50 spectra, which was the characteristic methoxy group of lignin [36]. In contrast to KL, JLQKL50 exhibited a strong peak at 70 ppm, which was the O-C-C-O repeating unit Solid-state 13 C NMR is a widely used method for the investigation of the lignin structure. In this study, it was used to analyze the chemical structures of KL and JLQKL 50 . As seen in Figure 2b, all the characteristic peaks in the spectrum of KL were retained in the spectrum of JLQKL 50 . For example, a peak at 55 ppm was observed in both the KL and JLQKL 50 spectra, which was the characteristic methoxy group of lignin [36]. In contrast to KL, JLQKL 50 exhibited a strong peak at 70 ppm, which was the O-C-C-O repeating unit contained in the PEGDGE crosslinker and indicated an effective crosslinking reaction between QKL 50 and PEGDGE [37]. These results confirmed the successful synthesis of JLQKL 50 .

Zeta Potential versus pH of KL and JLQKL 50
The zeta potential of KL and JLQKL 50 solutions under different pH conditions is presented in Figure S2 (Supporting Information). The zeta potential of KL was negative within the pH range of 3-12 because of the absence of positively charged functional groups in the molecule. In JLQKL 50 , an isoelectric point (pH = 7.5) was observed, which was attributed to the introduction of quaternary ammonium groups that could neutralize the original negatively charged groups in the KL molecule. When the pH increased from 3 to 7, the zeta potential of JLQKL 50 gradually decreased because the level of ionization of the carboxyl group was increasing [38]. At a pH range of 7-9, the zeta potential slowly decreased because of the ionization of the unreacted phenolic hydroxyl groups. At the pH range of 9-12, the zeta potential stabilized when the phenolic hydroxyl groups were completely ionized [39]. Figure 3a presents the influence of the JLQKL 50 concentration on the enzymatic hydrolysis efficiency of the corn stalk. The enzymatic hydrolysis efficiency increased with the additive concentration from 0 g/L to 2 g/L and then decreased. When the concentration of additive JLQKL 50 was 2 g/L, the maximum enzymatic hydrolysis efficiency reached 78.88%, which was increased by 11.62% compared to that without the additive. When the concentration increased beyond 2 g/L, the enzyme activity was inhibited by excessive JLQKL 50 , resulting in a decrease in enzymatic hydrolysis efficiency [40]. Therefore, 2 g/L of additive was found to be the optimum.

Effects of Different Concentrations of Additive on Enzymatic Hydrolysis
the carboxyl group was increasing [38]. At a pH range of 7-9, the zeta potential slowly decreased because of the ionization of the unreacted phenolic hydroxyl groups. At the pH range of 9-12, the zeta potential stabilized when the phenolic hydroxyl groups were completely ionized [39]. Figure 3a presents the influence of the JLQKL50 concentration on the enzymatic hydrolysis efficiency of the corn stalk. The enzymatic hydrolysis efficiency increased with the additive concentration from 0 g/L to 2 g/L and then decreased. When the concentration of additive JLQKL50 was 2 g/L, the maximum enzymatic hydrolysis efficiency reached 78.88%, which was increased by 11.62% compared to that without the additive. When the concentration increased beyond 2 g/L, the enzyme activity was inhibited by excessive JLQKL50, resulting in a decrease in enzymatic hydrolysis efficiency [40]. Therefore, 2 g/L of additive was found to be the optimum. Figure 3b depicts the enzymatic hydrolysis efficiency of the control and JLQKL50 from 6 to 72 h. The enzymatic hydrolysis efficiency of corn stalk at 6, 12, 24, 48, and 72 h increased to 57.10%, 70.94%, 78.88%, 85.13%, and 91.11% after the addition of 2 g/L of JLQKL50. The increase rate was 3.14%, 6.66%, 11.62%, 6.89%, and 4.56%, respectively. The enzymatic hydrolysis of corn stalk was obviously promoted at 24 h and the increase rate was the highest. Thus, we conducted subsequent experiments to check the environmental applicability of enzymatic hydrolysis with or without JLQKL50 based on the enzymatic hydrolysis efficiency at 24 h. This could help to improve the efficiency of experiments.   Figure 3b depicts the enzymatic hydrolysis efficiency of the control and JLQKL 50 from 6 to 72 h. The enzymatic hydrolysis efficiency of corn stalk at 6, 12, 24, 48, and 72 h increased to 57.10%, 70.94%, 78.88%, 85.13%, and 91.11% after the addition of 2 g/L of JLQKL 50 . The increase rate was 3.14%, 6.66%, 11.62%, 6.89%, and 4.56%, respectively. The enzymatic hydrolysis of corn stalk was obviously promoted at 24 h and the increase rate was the highest. Thus, we conducted subsequent experiments to check the environmental applicability of enzymatic hydrolysis with or without JLQKL 50 based on the enzymatic hydrolysis efficiency at 24 h. This could help to improve the efficiency of experiments.

Environmental Applicability of JLQKL 50 -Enhanced Enzymatic Hydrolysis
The effect of JLQKL 50 on the enzymatic hydrolysis efficiency of corn stalk under the different buffer pH conditions is presented in Figure 4a. The enzymatic hydrolysis efficiency of the corn stalk tended to be stable when the buffer pH was 4.5-5.0 without additive. A decrease in the enzymatic hydrolysis efficiency of corn stalk was observed as the pH increased from 5.0 to 6.0. As the pH increased to values over 6.0-6.5, the enzymatic hydrolysis efficiency of corn stalk decreased rapidly to 35.04% because of the partial inactivation of cellulase at high buffer pH values. The addition of JLQKL 50 did not change the trend of the enzymatic hydrolysis efficiency with the pH value. However, the enzymatic Polymers 2023, 15, 1991 7 of 12 hydrolysis efficiency of corn stalk with the addition of JLQKL 50 at pH 6.0 was even higher than that of the control at pH 4.8. This indicated that JLQKL 50 contributed to widening the pH range for enzymatic hydrolysis to maintain high efficiency. This is possibly because the addition of JLQKL 50 reduces the nonproductive adsorption of cellulase on substrate lignin by enabling electrostatic repulsion after JLQKL 50 adsorbs on the cellulase and substrate lignin. As shown in Figure 4a, the decrease in the enzymatic hydrolysis efficiency of the control experiment was slightly slower than that of the experiment with the addition of JLQKL 50 when the pH increased from 4.8 to 6.0. This demonstrated that the decrease in enzymatic hydrolysis efficiency with the addition of JLQKL 50 was not only due to the decrease in cellulase activity. In fact, the positive electricity of JLQKL 50 declined ( Figure S2, Supporting Information) when the pH increased from 4.8 to 6.0, resulting in a reduction in the electrostatic repulsion between JLQKL 50 -adsorbed cellulase and substrate lignin. Hence, the ability of JLQKL 50 in reducing the nonproductive adsorption of cellulase on substrate lignin dropped. These analyses indicated that the contribution of JLQKL 50 in widening the pH range for enzymatic hydrolysis might be highly related to the ability of JLQKL 50 in reducing the nonproductive adsorption.  Here, we do not compare the results of the increase rate with those in previously published papers. This is because the enzymatic hydrolysis efficiency of the control experiments in our study was high, as shown in Figure 3b. In this study, the enzymatic hydrolysis efficiency of dilute-alkali-pretreated corn stalk after 72 h reached 87.14% under the following conditions: substrate solid content of 10% (w/v), 10 FPU/g of cellulase, pH 4.8, 50 °C, 200 rpm, and no additives. Therefore, the maximum improvement was only 12.86%, regardless of the used additive. The addition of JLQKL50 strongly improved the enzymatic hydrolysis efficiency of dilute-alkali-pretreated corn stalk according to our results. The increase rate was not very significant, only due to the good enzymatic hydrolysis efficiency of the control experiments. It is possible that the JLQKL50 additive also can present remarkable improvements in the enzymatic hydrolysis efficiency in a system in which the enzymatic hydrolysis efficiency of the control experiments is not very high. The effect of JLQKL 50 on the enzymatic hydrolysis efficiency of corn stalk at different temperatures is presented in Figure 4b. After the addition of JLQKL 50 within a temperature range of 45-55 • C, the enzymatic hydrolysis efficiency significantly improved. The maximum enzymatic hydrolysis efficiency reached 78.88% at 50 • C with JLQKL 50 , which was much higher than that (70.67%) without the additive. The enzymatic hydrolysis efficiency was reduced significantly as the temperature increased above 55 • C, owing to the partial inactivation of cellulase under high temperatures. It could be seen that the enzymatic hydrolysis efficiency of corn stalk with the addition of JLQKL 50 at 45 • C was even higher Polymers 2023, 15, 1991 8 of 12 than that of the control at 50 • C. This implied that the addition of JLQKL 50 could broaden the temperature range for enzymatic hydrolysis to maintain high efficiency.
The effect of enzyme loading on the enzymatic hydrolysis efficiency of corn stalk after 24 h was investigated, as shown in Figure 4c. In the absence of additive, the enzymatic hydrolysis efficiency increased rapidly and then slowly with increasing enzyme loading. The enzymatic hydrolysis efficiency of corn stalk improved at different loadings of the enzyme in the presence of the additive (JLQKL 50 ). A 15 FPU/g of enzyme loading was required to increase the enzymatic hydrolysis efficiency of corn stalk without the additive to over 80%. Similar efficiency could be obtained by using 10 FPU/g enzyme loading and using JLQKL 50 as the additive. The results showed that when the enzymatic hydrolysis efficiency of corn stalk reached~80%, the addition of JLQKL 50 reduced the enzyme loading by 33.33%. There are some studies reporting the ability of additives to effectively reduce the enzyme loading during the enzymatic hydrolysis process [41][42][43][44]. In addition, it could be found that the enzymatic hydrolysis time of 24 h was not sufficient to reach higher enzymatic hydrolysis efficiency than 95%, although the enzyme loading increased to 30 FPU/g. Thus, we further studied the effect of enzyme loading on the enzymatic hydrolysis efficiency of corn stalk after 72 h. The results are shown in Figure 4d. An enzyme loading of 15 FPU/g should be used to obtain higher enzymatic hydrolysis efficiency than 95% after 72 h. The enzymatic hydrolysis efficiency at 72 h with the addition of JLQKL 50 reached 97.92%.
Here, we do not compare the results of the increase rate with those in previously published papers. This is because the enzymatic hydrolysis efficiency of the control experiments in our study was high, as shown in Figure 3b. In this study, the enzymatic hydrolysis efficiency of dilute-alkali-pretreated corn stalk after 72 h reached 87.14% under the following conditions: substrate solid content of 10% (w/v), 10 FPU/g of cellulase, pH 4.8, 50 • C, 200 rpm, and no additives. Therefore, the maximum improvement was only 12.86%, regardless of the used additive. The addition of JLQKL 50 strongly improved the enzymatic hydrolysis efficiency of dilute-alkali-pretreated corn stalk according to our results. The increase rate was not very significant, only due to the good enzymatic hydrolysis efficiency of the control experiments. It is possible that the JLQKL 50 additive also can present remarkable improvements in the enzymatic hydrolysis efficiency in a system in which the enzymatic hydrolysis efficiency of the control experiments is not very high.

Effect of Stirring on Cellulase Activity
The cellulase and additive were added sequentially to the buffer and subjected to a temperature of 50 • C and agitation at 200 rpm for 72 h. Then, corn stalk was added for 24 h of enzymatic hydrolysis. The effect of JLQKL 50 on cellulase activity after strong agitation was investigated. As shown in Figure 5, the enzymatic hydrolysis efficiency of cellulase without agitation and without an additive was 70.67%, whereas that of cellulase without an additive but with agitation was reduced to 49.70%. The decrease rate was 29.7%. Similarly, the efficiency of cellulase with the additive (JLQKL 50 ) but without agitation was 78.88% and it was reduced to 65.14% after the addition of JLQKL 50 and with agitation for 72 h. The decrease rate was 17.4%. The results showed that cellulase was easily deactivated after strong agitation when no additive was added and presented high activity when an additive (JLQKL 50 ) was added, which was beneficial to the recycling of cellulase with sufficient activity.

Effect of JLQKL 50 on the Aggregation and Dispersion of Cellulase
Dynamic light scattering (DLS) analysis was used to determine the average size of cellulase in water. The results of the mean diameter versus storage time are shown in Figure 6. The initial mean diameter of cellulase was~31 nm. With the increasing storage time, the mean diameter of cellulase increased gradually and approached~48 nm after storage for 24 h. This indicated that the aggregation of cellulase increased with storage time. Meanwhile, in the presence of JLQKL 50 , the initial mean diameter of cellulase decreased to

Effect of JLQKL50 on the Aggregation and Dispersion of Cellulase
Dynamic light scattering (DLS) analysis was used to determine the average size of cellulase in water. The results of the mean diameter versus storage time are shown in Figure 6. The initial mean diameter of cellulase was ~31 nm. With the increasing storage time, the mean diameter of cellulase increased gradually and approached ~48 nm after storage for 24 h. This indicated that the aggregation of cellulase increased with storage time. Meanwhile, in the presence of JLQKL50, the initial mean diameter of cellulase decreased to ~18 nm and remained stable with the storage time. This illustrated that JLQKL50 could act as a dispersant to prevent cellulase from aggregating. According to the above experimental results and analyses, a potential mechanism to enhance the enzymatic hydrolysis of corn stalk by adding JLQKL50 is proposed. JLQKL50 contains a crosslinked lignin backbone and branched cationic groups, which are hydrophobic and electropositive, respectively. It could adsorb on the hydrophobic and electronegative lignin in the substrate through hydrophobic interaction and electrostatic interaction to make the substrate hydrophilic and electropositive. Meanwhile, the cellulase also becomes electropositive because of the adsorption of JLQKL50 through hydrophobic interaction. Thus, the nonproductive adsorption of cellulase on lignin in the substrate is reduced by electrostatic repulsion. In addition, the dispersity and stability of cellulase are improved by JLQKL50. Due to the aforementioned reasons, the cellulase and cellulose in the substrate could have more opportunities to interact with each other so that the enzy-

Effect of JLQKL50 on the Aggregation and Dispersion of Cellulase
Dynamic light scattering (DLS) analysis was used to determine the average size of cellulase in water. The results of the mean diameter versus storage time are shown in Figure 6. The initial mean diameter of cellulase was ~31 nm. With the increasing storage time, the mean diameter of cellulase increased gradually and approached ~48 nm after storage for 24 h. This indicated that the aggregation of cellulase increased with storage time. Meanwhile, in the presence of JLQKL50, the initial mean diameter of cellulase decreased to ~18 nm and remained stable with the storage time. This illustrated that JLQKL50 could act as a dispersant to prevent cellulase from aggregating. According to the above experimental results and analyses, a potential mechanism to enhance the enzymatic hydrolysis of corn stalk by adding JLQKL50 is proposed. JLQKL50 contains a crosslinked lignin backbone and branched cationic groups, which are hydrophobic and electropositive, respectively. It could adsorb on the hydrophobic and electronegative lignin in the substrate through hydrophobic interaction and electrostatic interaction to make the substrate hydrophilic and electropositive. Meanwhile, the cellulase also becomes electropositive because of the adsorption of JLQKL50 through hydrophobic interaction. Thus, the nonproductive adsorption of cellulase on lignin in the substrate is reduced by electrostatic repulsion. In addition, the dispersity and stability of cellulase are improved by JLQKL50. Due to the aforementioned reasons, the cellulase and cellulose in the substrate could have more opportunities to interact with each other so that the enzymatic hydrolysis efficiency can be increased. According to the above experimental results and analyses, a potential mechanism to enhance the enzymatic hydrolysis of corn stalk by adding JLQKL 50 is proposed. JLQKL 50 contains a crosslinked lignin backbone and branched cationic groups, which are hydrophobic and electropositive, respectively. It could adsorb on the hydrophobic and electronegative lignin in the substrate through hydrophobic interaction and electrostatic interaction to make the substrate hydrophilic and electropositive. Meanwhile, the cellulase also becomes electropositive because of the adsorption of JLQKL 50 through hydrophobic interaction. Thus, the nonproductive adsorption of cellulase on lignin in the substrate is reduced by electrostatic repulsion. In addition, the dispersity and stability of cellulase are improved by JLQKL 50 . Due to the aforementioned reasons, the cellulase and cellulose in the substrate could have more opportunities to interact with each other so that the enzymatic hydrolysis efficiency can be increased.

Conclusions
In summary, new cationic kraft lignin (JLQKL 50 ) with good water solubility was successfully synthesized by quaternization combined with crosslinking using KL as a raw material, CHPTMAC as a cationic modifier, and PEGDGE as a crosslinker. There was a 11.62% increase rate in the enzymatic hydrolysis efficiency of corn stalk at solid content of 10% (w/v) after 24 h when the dosage of JLQKL 50 was fixed at a concentration of 2 g/L. With this dosage of JLQKL 50 , the enzymatic hydrolysis efficiency after 72 h reached 91.11% and 97.92% when the enzyme loading was 10 FPU/g and 15 FPU/g, respectively. The enzymatic hydrolysis system containing JLQKL 50 could present high efficiency (higher than 70%) at a wide pH range (at least 4.5-6.0) and temperature range (at least 45-55 • C). The ranges were wider than those of the control without JLQKL 50 . The cellulase activity with the protection of JLQKL 50 under intense agitation remained at 82.6%, which was much higher than that (70.3%) without JLQKL 50 . The promotion effect of JLQKL 50 on enzymatic hydrolysis is likely due to the reduction in the nonproductive adsorption of cellulase on substrate lignin and the improvement in the longevity, dispersity, and stability of cellulase.