Industrial cellulase performance in the simultaneous saccharification and co-fermentation (SSCF) of corn stover for high-titer ethanol production

Qiang Zhang , Jie Bao

Bioresources and Bioprocessing ›› 2017, Vol. 4 ›› Issue (1) : 17

PDF
Bioresources and Bioprocessing ›› 2017, Vol. 4 ›› Issue (1) : 17 DOI: 10.1186/s40643-017-0147-7
Research

Industrial cellulase performance in the simultaneous saccharification and co-fermentation (SSCF) of corn stover for high-titer ethanol production

Author information +
History +
PDF

Abstract

Background

Cellulase enzymes contribute to the largest portion of operation cost on production of cellulosic ethanol. The industrial cellulases available on the industrial enzyme market from different makers and sources vary significantly in hydrolysis and ethanol, and finally lead to the changes of enzyme cost. Therefore, the selection of the proper industrial cellulase enzymes for commercial-scale production of cellulosic ethanol is crucially important in terms of high performance and cost reduction.

Results

In this study, three major cellulase enzyme products available on the Chinese industrial enzyme market were selected and evaluated as the biocatalysts for the biorefining process of lignocellulose biomass into high-titer ethanol. The cellulase enzymes included Cellic CTec 2.0 from Novozymes (Beijing), and LLC 4 from Vland (Qingdao), as well as # 7 from an industrial enzyme maker. The detailed assays on the filter paper activity, the cellobiase activity, and the total protein contents of the enzymes were conducted according to the standard protocols. When the cellulase enzymes were applied to the practical hydrolysis and ethanol-fermentation operation under the conditions of high solids loading and low range of cellulase dosage, the hydrolysis yield shows the significant difference, and the difference was narrowed in the final ethanol yield.

Conclusions

The commercially available cellulase enzymes showed different performances in the activities, the cellulose hydrolysis yield, and the ethanol fermentation yields based on the protein dosage per gram of cellulose of corn stover. In general, the industrial cellulase products give satisfactory performance and can be applied for the practical cellulosic ethanol production on commercial scale.

Keywords

Industrial cellulase enzyme / Activity / Ethanol / Hydrolysis / Lignocellulose

Cite this article

Download citation ▾
Qiang Zhang, Jie Bao. Industrial cellulase performance in the simultaneous saccharification and co-fermentation (SSCF) of corn stover for high-titer ethanol production. Bioresources and Bioprocessing, 2017, 4(1): 17 DOI:10.1186/s40643-017-0147-7

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

Adney B, Baker J (1996) Measurement of cellulase activities. AP-006. NREL. Analytical Procedure. National Renewable Energy Laboratory, Golden CO

[2]

Bradford MM. A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. Anal Biochem, 1976, 72: 248-254.

[3]

Chen XW, Kuhn E, Jennings EW, Nelson R, Tao L, Zhang M. DMR (deacetylation and mechanical refining) processing of corn stover achieves high monomeric sugar concentrations (230 g/L) during enzymatic hydrolysis and high ethanol concentrations (>10% v/v) during fermentation without hydrolysate purification or concentration. Energy Environ Sci, 2016, 9: 1237-1245.

[4]

Chiaramonti D, Balan V, Kumar S. Review of US and EU initiatives toward development, demonstration, and commercialization of lignocellulosic biofuels. Biofuels Bioprod Bioref, 2013, 7: 732-759.

[5]

Gang L, Jian Z, Jie B. Cost evaluation of cellulase enzyme for industrial-scale cellulosic ethanol production based on rigorous aspen plus modeling. Bioprocess Biosyst Eng, 2016, 39: 133-140.

[6]

Ghose TK. Measurement of cellulase activities. Pure Appl Chem, 1987, 59: 257-268.

[7]

Gu HQ, Zhang J, Bao J. High tolerance and physiological mechanism of zymomonas mobilis to phenolic inhibitors in ethanol fermentation of corncob residue. Biotechnol Bioeng, 2015, 112: 1770-1782.

[8]

He Y, Zhang J, Bao J. Dry dilute acid pretreatment by co-currently feeding of corn stover feedstock and dilute acid solution without impregnation. Bioresour Technol, 2014, 158: 360-364.

[9]

He Y, Zhang J, Bao J. Acceleration of biodetoxification on dilute acid pretreated lignocellulose feedstock by aeration and the consequent ethanol fermentation evaluation. Biotechnol Biofuels, 2016, 9: 19.

[10]

Klein-Marcuschamer D, Oleskowicz-Popiel P, Simmons BA, Blanch HW. The challenge of enzyme cost in the production of lignocellulosic biofuels. Biotechnol Bioeng, 2012, 109: 1083-1087.

[11]

Lei C, Zhang J, Xiao L, Bao J. An alternative feedstock of corn meal for industrial fuel ethanol production: delignified corncob residue. Bioresour Technol, 2014, 167: 555-559.

[12]

Li H, Wu M, Xu L, Jin H, Guo T, Bao X. Evaluation of industrial saccharomyces cerevisiae strains as the chassis cell for second-generation bioethanol production. Microb Biotechnol, 2015, 82: 66.

[13]

Liu S, Wang Q. Response surface optimization of enzymatic hydrolysis process of wet oxidation pretreated wood pulp waste. Cellul Chem Technol, 2014, 50: 803-809.

[14]

Marcos M, González-Benito G, Coca M, Bolado S, Lucas S. Optimization of the enzymatic hydrolysis conditions of steam-exploded wheat straw for maximum glucose and xylose recovery. J Chem Technol Biotechnol, 2013, 88: 237-246.

[15]

Qureshi AS, Zhang J, Bao J. High ethanol fermentation performance of the dry dilute acid pretreated corn stover by an evolutionarily adapted saccharomyces cerevisiae, strain. Bioresour Technol, 2015, 189: 399-404.

[16]

Ramesh D. World’s first commercial scale cellulosic biofuels plant opens. Chem Week, 2013, 175: 39.

[17]

Sluiter A, Hames B, Ruiz R Scarlata C, Sluiter J Templeton D (2008) Determination of sugars, byproducts, and degradation products in liquid fraction process samples. NREL/TP-510-42623. National Renewable Energy Laboratory, Golden CO

[18]

Sluiter A, Hames B, Ruiz R, Scarlata C, Sluiter J, Templeton D, Crocker D (2012) Determination of structural carbohydrates and lignin in biomass. NREL/TP-510-42618. National Renewable Energy Laboratory, Golden CO

[19]

Zhang J, Bao J. A modified method for calculating practical ethanol yield at high lignocellulosic solids content and high ethanol titer. Bioresour Technol, 2012, 116: 74-79.

[20]

Zhang Y, Schell D, Mcmillan J. Methodological analysis for determination of enzymatic digestibility of cellulosic materials. Biotechnol Bioeng, 2007, 96: 188-194.

[21]

Zhang J, Zhu Z, Wang X, Wang N, Wang W, Bao J. Biodetoxification of toxins generated from lignocellulose pretreatment using a newly isolated fungus Amorphotheca resinae ZN1 and the consequent ethanol fermentation. Biotechnol Biofuels, 2010, 3: 26.

[22]

Zhang J, Chu D, Huang J, Yu Z, Dai G, Bao J. Simultaneous saccharification and ethanol fermentation at high corn stover solids loading in a helical stirring bioreactor. Biotechnol Bioeng, 2010, 105: 718-728.

[23]

Zhang J, Wang X, Chu D, He Y, Bao J. Dry pretreatment of lignocellulose with extremely low steam and water usage for bioethanol production. Bioresour Technol, 2011, 102: 4480-4488.

[24]

Zhang J, Shao S, Bao J. Long term storage of dilute acid pretreated corn stover feedstock and ethanol fermentability evaluation. Bioresour Technol, 2015, 201: 355-359.

[25]

Zhang H, Han X, Wei C, Bao J. Oxidative production of xylonic acid using xylose in distillation stillage of cellulosic ethanol fermentation broth by gluconobacter oxydans. Bioresour Technol, 2016, 224: 573-580.

Funding

High-Tech Program of China(2014AA021901)

AI Summary AI Mindmap
PDF

104

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/