期刊论文详细信息
Biotechnology for Biofuels
Ethanol and biogas production after steam pretreatment of corn stover with or without the addition of sulphuric acid
Pia-Maria Bondesson1  Mats Galbe1  Guido Zacchi1 
[1] Department of Chemical Engineering, Lund University, P.O. Box 124, SE-221 00, Lund, Sweden
关键词: Sulphuric acid;    Methane;    Ethanol;    Steam pretreatment;    Corn stover;   
Others  :  798171
DOI  :  10.1186/1754-6834-6-11
 received in 2012-08-27, accepted in 2012-11-22,  发布年份 2013
PDF
【 摘 要 】

Background

Lignocellulosic biomass, such as corn stover, is a potential raw material for ethanol production. One step in the process of producing ethanol from lignocellulose is enzymatic hydrolysis, which produces fermentable sugars from carbohydrates present in the corn stover in the form of cellulose and hemicellulose. A pretreatment step is crucial to achieve efficient conversion of lignocellulosic biomass to soluble sugars, and later ethanol. This study has investigated steam pretreatment of corn stover, with and without sulphuric acid as catalyst, and examined the effect of residence time (5–10 min) and temperature (190–210°C) on glucose and xylose recovery. The pretreatment conditions with and without dilute acid that gave the highest glucose yield were then used in subsequent experiments. Materials pretreated at the optimal conditions were subjected to simultaneous saccharification and fermentation (SSF) to produce ethanol, and remaining organic compounds were used to produce biogas by anaerobic digestion (AD).

Results

The highest glucose yield achieved was 86%, obtained after pretreatment at 210°C for 10 minutes in the absence of catalyst, followed by enzymatic hydrolysis. The highest yield using sulphuric acid, 78%, was achieved using pretreatment at 200°C for 10 minutes. These two pretreatment conditions were investigated using two different process configurations. The highest ethanol and methane yields were obtained from the material pretreated in the presence of sulphuric acid. The slurry in this case was split into a solid fraction and a liquid fraction, where the solid fraction was used to produce ethanol and the liquid fraction to produce biogas. The total energy recovery in this case was 86% of the enthalpy of combustion energy in corn stover.

Conclusions

The highest yield, comprising ethanol, methane and solids, was achieved using pretreatment in the presence of sulphuric acid followed by a process configuration in which the slurry from the pretreatment was divided into a solid fraction and a liquid fraction. The solid fraction was subjected to SSF, while the liquid fraction, together with the filtered residual from SSF, was used in AD. Using sulphuric acid in AD did not inhibit the reaction, which may be due to the low concentration of sulphuric acid used. In contrast, a pretreatment step without sulphuric acid resulted not only in higher concentrations of inhibitors, which affected the ethanol yield, but also in lower methane production.

【 授权许可】

   
2013 Bondesson et al.; licensee BioMed Central Ltd.

【 预 览 】
附件列表
Files Size Format View
20140706103418386.pdf 482KB PDF download
Figure 7. 33KB Image download
Figure 6. 34KB Image download
Figure 5. 44KB Image download
Figure 4. 38KB Image download
Figure 3. 47KB Image download
Figure 2. 33KB Image download
Figure 1. 35KB Image download
【 图 表 】

Figure 1.

Figure 2.

Figure 3.

Figure 4.

Figure 5.

Figure 6.

Figure 7.

【 参考文献 】
  • [1]Hahn-Hagerdal B, Galbe M, Gorwa-Grauslund MF, Liden G, Zacchi G: Bio-ethanol—the fuel of tomorrow from the residues of today. Trends Biotechnol 2006, 24:549-556.
  • [2]Galbe M, Zacchi G: Pretreatment of lignocellulosic materials for efficient bioethanol production. Adv Biochem Eng Biotechnol 2007, 108:41-65.
  • [3]Galbe M, Zacchi G: Pretreatment: The key to efficient utilization of lignocellulosic materials. Biomass Bioenergyin press
  • [4]Galbe M, Liden G, Zacchi G: Production of ethanol from biomass — Research in Sweden. J Sci Ind Res 2005, 64:905-919.
  • [5]Lloyd TA, Wyman CE: Combined sugar yields for dilute sulfuric acid pretreatment of corn stover followed by enzymatic hydrolysis of the remaining solids. Bioresour Technol 2005, 96:1967-1977.
  • [6]Varga E, Reczey K, Zacchi G: Optimization of steam pretreatment of corn stover to enhance enzymatic digestibility. Appl Biochem Biotechnol 2004, 113:509-523.
  • [7]Tucker MP, Kim KH, Newman MM, Nguyen QA: Effects of temperature and moisture on dilute-acid steam explosion pretreatment of corn stover and cellulase enzyme digestibility. Appl Biochem Biotechnol 2003, 105:165-177.
  • [8]Ohgren K, Galbe M, Zacchi G: Optimization of steam pretreatment of SO2-impregnated corn stover for fuel ethanol production. Appl Biochem Biotechnol 2005, 121:1055-1067.
  • [9]Elander RT, Dale BE, Holtzapple M, Ladisch MR, Lee YY, Mitchinson C, Saddler JN, Wyman CE: Summary of findings from the Biomass Refining Consortium for Applied Fundamentals and Innovation (CAFI): corn stover pretreatment. Cellulose 2009, 16:649-659.
  • [10]Ohgren K, Bengtsson O, Gorwa-Grauslund MF, Galbe M, Hahn-Hagerdal B, Zacchi G: Simultaneous saccharification and co-fermentation of glucose and xylose in steam-pretreated corn stover at high fiber content with Saccharomyces cerevisiae TMB3400. J Biotechnol 2006, 126:488-498.
  • [11]Olofsson K, Rudolf A, Lidén G: Designing simultaneous saccharification and fermentation for improved xylose conversion by a recombinant strain of Saccharomyces cerevisiae. J Biotechnol 2008, 134:112-120.
  • [12]Kaparaju P, Serrano M, Thomsen AB, Kongjan P, Angelidaki I: Bioethanol, biohydrogen and biogas production from wheat straw in a biorefinery concept. Bioresour Technol 2009, 100:2562-2568.
  • [13]Cao G, Ren N, Wang A, Lee DJ, Guo W, Liu B, Feng Y, Zhao Q: Acid hydrolysis of corn stover for biohydrogenproduction using Thermoanaerobacteriumthermosaccharolyticum W16. Int J Hydrogen Energ 2008, 34:7182-7188.
  • [14]Bauer A, Bosch P, Friedl A, Amon T: Analysis of methane potentials of steam-exploded wheat straw and estimation of energy yields of combined ethanol and methane production. J Biotechnol 2009, 142:50-55.
  • [15]Kaparaju P, Serrano M, Angelidaki I: Effect of reactor configuration on biogas production from wheat straw hydrolysate. Bioresour Technol 2009, 100:6317-6323.
  • [16]Dererie DY, Trobro S, Momeni MH, Hansson H, Blomqvist J, Passoth V, Schnürer A, Sandgren M, Ståhlberg J: Improved bio-energy yields via sequential ethanol fermentation and biogas digestion of steam exploded oat straw. Bioresour Technol 2011, 102:4449-4455.
  • [17]Taherzadeh MJ, Karimi K: Pretreatment of lignocellulosic wastes to improve ethanol and biogas production: a review. Int J Mol Sci 2008, 9:1621-1651.
  • [18]Frigon JC, Guiot SR: Biomethane production from starch and lignocellulosic crops: a comparative review. Biofuels Bioproducts & Biorefining-Biofpr 2010, 4:447-458.
  • [19]Chen Y, Cheng JJ, Creamer KS: Inhibition of anaerobic digestion process: a review. Bioresour Technol 2008, 99:4044-4064.
  • [20]Ohgren K, Rudolf A, Galbe M, Zacchi G: Fuel ethanol production from steam-pretreated corn stover using SSF at higher dry matter content. Biomass Bioenergy 2006, 30:863-869.
  • [21]Pordesimo LO, Hames BR, Sokhansanj S, Edens WC: Variation in corn stover composition and energy content with crop maturity. Biomass Bioenergy 2005, 28:366-374.
  • [22]Sluiter A, Hames B, Ruiz R, Scarlata C, Sluiter J, Templeton D, Crocker D: Determination of Structual Carbohydrates and Lignin in Biomass. Golden, CO: NREL; 2008.
  • [23]Ehrman T: Determination of Starch in Biomass Samples by Chemical Solubilization and Enzymatic Digestion. Golden, CO: NREL; 1996.
  • [24]Sluiter A, Ruiz R, Scarlata C, Sluiter J, Templeton D: Determination of Extractives in Biomass. Golden, CO: NREL; 2005.
  • [25]Palmqvist E, Hahn-Hägerdal B, Galbe M, Larsson M, Stenberg K, Szengyel Z, Tengborg C, Zacchi G: Design and operation of a bench-scale process development unit for the production of ethanol from lignocellulosics. Bioresour Technol 1996, 58:171-179.
  • [26]Sluiter A, Hames B, Ruiz R, Scarlata C, Sluiter J, Templeton D: Determination of Sugars, Byproducts, and Degradation Products in Liquid Fraction Process Samples. Golden, CO: NREL; 2006.
  • [27]Weiss ND, Stickel JJ, Wolfe JL, Nguyen QA: A simplified method for the measurement of insoluble solids in pretreated biomass slurries. Appl Biochem Biotechnol 2010, 162:975-987.
  • [28]Taherzadeh MJ, Liden G, Gustafsson L, Niklasson C: The effects of pantothenate deficiency and acetate addition on anaerobic batch fermentation of glucose by Saccharomyces cerevisiae. Appl Microbiol Biotechnol 1996, 46:176-182.
  • [29]Hansen TL, Schmidt JE, Angelidaki I, Marca E, Jansen JC, Mosbæk H, Christensen TH: Method for determination of methane potentials of solid organic waste. Waste Manag 2004, 24:393-400.
  文献评价指标  
  下载次数:168次 浏览次数:40次