Elsevier

Bioresource Technology

Volume 185, June 2015, Pages 165-170
Bioresource Technology

Lignin-based polyoxyethylene ether enhanced enzymatic hydrolysis of lignocelluloses by dispersing cellulase aggregates

https://doi.org/10.1016/j.biortech.2015.02.067Get rights and content

Highlights

  • Enzymatic hydrolysis lignin is used to prepare EHL–PEG.

  • EHL–PEG improved glucose yield of corn stover from16.7% to 70.1%.

  • EHL–PEG reduced cellulase non-productive adsorption on lignin by 88%.

  • EHL–PEG dispersed cellulase aggregates from 1220 nm to 420 nm.

Abstract

Water-soluble lignin-based polyoxyethylene ether (EHL–PEG), prepared from enzymatic hydrolysis lignin (EHL) and polyethylene glycol (PEG1000), was used to improve enzymatic hydrolysis efficiency of corn stover. The glucose yield of corn stover at 72 h was increased from 16.7% to 70.1% by EHL–PEG, while increase in yield with PEG4600 alone was 52.3%. With the increase of lignin content, EHL–PEG improved enzymatic hydrolysis of microcrystalline cellulose more obvious than PEG4600. EHL–PEG could reduce at least 88% of the adsorption of cellulase on the lignin film measured by quartz crystal microbalance with dissipation monitoring (QCM-D), while reduction with PEG4600 was 43%. Cellulase aggregated at 1220 nm in acetate buffer analyzed by dynamic light scattering. EHL–PEG dispersed cellulase aggregates and formed smaller aggregates with cellulase, thereby, reduced significantly nonproductive adsorption of cellulase on lignin and enhanced enzymatic hydrolysis of lignocelluloses.

Introduction

Lignocellulosic biomass is the most abundant and renewable source on earth and can be converted to value-add chemicals or bio-fuels through the sugar platform (Himmel et al., 2007, Ragauskas et al., 2006). A pretreatment to alter and/or remove lignin and hemicellulose is necessary prior to enzymatic hydrolysis because of the recalcitrance of lignocelluloses (Zhao et al., 2012). However, lignin is usually partially removed because of the high cost of the complete delignification according to the cost accounting of pulp and paper industry (Leu and Zhu, 2013). As a result, the residual lignin acts as a physical barrier and an attractant to cellulase to reduce the adsorption of cellulase on cellulose (Kumar et al., 2012, Li et al., 2014, Selig et al., 2007). Hence, lignin has a significant negative impact on the enzymatic hydrolysis efficiency of lignocelluloses (Nakagame et al., 2011, Pan, 2008, Yu et al., 2014, Zeng et al., 2014).

Addition of surfactant (Börjesson et al., 2007a, Börjesson et al., 2007b, Eriksson et al., 2002, Kristensen et al., 2007, Li et al., 2012, Ouyang et al., 2010, Ouyang et al., 2011) and protein (Yang and Wyman, 2006) could decrease the nonproductive adsorption of cellulase on the lignin and enhance the enzymatic hydrolysis efficiency of lignocelluloses. Small molecular anionic surfactants restrained the enzymatic hydrolysis (Eriksson et al., 2002), while anionic polymeric surfactants like lignosulfonate, a byproduct from pulping spent liquor, improved the enzymatic hydrolysis (Lou et al., 2013b, Lou et al., 2014, Wang et al., 2013, Zhou et al., 2013). Non-ionic surfactants, especially polyethylene glycol (PEG) based polymer, were found to be the most effective (Eriksson et al., 2002). It had been suggested that the mechanism of enhancing the enzymatic hydrolysis of lignocelluloses by PEG included improving the stability and activity of cellulase, changing the substrate structure and reducing the nonproductive adsorption of cellulase (Börjesson et al., 2007b, Li et al., 2012, Ouyang et al., 2010). But a convincing explanation is still lacking (Eriksson et al., 2002).

Lignin is the second most abundant and renewable carbon resource on earth after cellulose. A large amount of residual lignin, generated from lignocellulosic ethanol production, is usually burned to meet the internal energy use, that has not been efficient utilization (Ragauskas et al., 2014). If enzymatic hydrolysis lignin (EHL) could be transformed to value-added materials, chemicals or fuels through an energy-effective and cost-effective route, it would greatly improve the biorefinery viability (Ragauskas et al., 2014). Lignin needs to be modified before applying as a dispersant for cement slurry, coal water slurry, pesticide suspension concentrates and so on due to its poor solubility and reactivity (Lin et al., 2014, Lou et al., 2013a, Zhou et al., 2007).

Amphiphilic lignin derivatives, prepared from acetic acid lignin and PEG-epoxide, could significantly improve the enzymatic hydrolysis efficiency of unbleached cedar pulp, but the enhancement was slightly less than that by PEG4000 (Winarni et al., 2013). Besides, residual activity of cellulase after enzymatic hydrolysis was remained at higher level by lignin derivatives than PEG4000 (Winarni et al., 2013). A method to prepare a water-soluble lignin-based polyoxyethylene ether from kraft lignin and PEG was recently proposed by our group (Lin et al., 2014), and the product contained phenylpropane unit and branched PEG hydrophilic chains. The present study is aimed to implement the comprehensive utilization of lignocellulosic biomass, as shown in Fig. 1. The residual enzymatic hydrolysis lignin (EHL) was PEGylated in order to improve the enzymatic hydrolysis efficiency of lignocelluloses.

The objective of this study is to evaluate the effect of EHL-based polyoxyethylene ether (EHL–PEG) on the enzymatic hydrolysis efficiency of corn stover. The role of EHL–PEG on the enzymatic hydrolysis of microcrystalline cellulose with different lignin contents was discussed. In order to reveal the underlying mechanism of enhancing the enzymatic hydrolysis of lignocelluloses, the effect of EHL–PEG on the nonproductive adsorption of cellulase on the lignin film and the aggregation and dispersion of cellulase was further investigated by quartz crystal microbalance with dissipation monitoring (QCM-D) and dynamic light scattering (DLS) analysis, respectively.

Section snippets

Materials

Corn stover, which was prepared by steam explosion pretreatment at 180 °C for 5 min, was provided by Henan Tianguan Group Co., Ltd. (Nanyang, China). Prior to enzymatic hydrolysis, corn stover was treated at 121 °C for 1 h by autoclave for sterilization to reduce the growth of bacteria, then was washed by Milli-Q water to remove water soluble contents and dried at 50 °C for 48 h. The content of cellulose, acid-insoluble lignin, xylan and ash of the obtained corn stover was 30.8%, 27.6%, 14.2% and

Effect of EHL–PEG on the enzymatic hydrolysis of corn stover

The effect of EHL–PEG and PEG on the enzymatic hydrolysis of corn stover was investigated in Fig. 2a. The glucose yield of corn stover at 72 h was increased from 16.7% to 27.2%, 52.3% and 70.1%, respectively, by adding 1 g/L of PEG1000, PEG4600 and EHL–PEG. With the increase of molecular weight of PEG, the enhancement of the enzymatic hydrolysis of corn stover increased. EHL–PEG improved the enzymatic hydrolysis of corn stover more conspicuously than PEG4600.

Fig. 2b showed the effect of the

Conclusion

EHL–PEG was prepared from enzymatic hydrolysis lignin to improve enzymatic hydrolysis of lignocelluloses. While with the increase of lignin content, EHL–PEG improved enzymatic hydrolysis of microcrystalline cellulose more obviously than PEG4600. Glucose yield of corn stover was increased from 16.7% to 70.1% by EHL–PEG, while PEG4600 used alone was 52.3%. EHL–PEG reduced 88% of the non-productive adsorption of cellulase on lignin film measured by QCM-D, while reduction with PEG4600 was 43%.

Acknowledgements

The authors acknowledge the financial support of the National Natural Science Foundation of China (21376100, 21476092), International S&T Cooperation Program of China (2013DFA41670), the National Basic Research Program of China 973 (2012CB215302), Guangdong Province Science and Technology Plan (2013B051000011) and the Fundamental Research Funds for the Central Universities of China (2014ZG0022).

References (35)

  • D.W. Sammond et al.

    Predicting enzyme adsorption to lignin films by calculating enzyme surface hydrophobicity

    J. Biol. Chem.

    (2014)
  • Z.J. Wang et al.

    Lignosulfonate-mediated cellulase adsorption: enhanced enzymatic saccharification of lignocellulose through weakening nonproductive binding to lignin

    Biotechnol. Biofuels

    (2013)
  • T.M. Wood et al.

    Methods for measuring cellulase activities

    Methods Enzymol.

    (1988)
  • Y. Zeng et al.

    Lignin plays a negative role in the biochemical process for producing lignocellulosic biofuels

    Curr. Opin. Biotechnol.

    (2014)
  • M.S. Zhou et al.

    High-performance dispersant of coal-water slurry synthesized from wheat straw alkali lignin

    Fuel Process. Technol.

    (2007)
  • M.E. Himmel et al.

    Biomass recalcitrance: engineering plants and enzymes for biofuels production

    Science

    (2007)
  • S.Y. Leu et al.

    Substrate-related factors affecting enzymatic saccharification of lignocelluloses: our recent understanding

    Bioenergy Res.

    (2013)
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    These authors contributed equally to this work.

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