期刊论文详细信息
Sustainable Chemical Processes
Microwave assisted chemical pretreatment of Miscanthus under different temperature regimes
Zongyuan Zhu2  Duncan J. Macquarrie2  Rachael Simister1  Leonardo D. Gomez1  Simon J. McQueen-Mason1 
[1] Department of Biology, Centre for Novel Agricultural Products, University of York, Heslington, York YO10 5DD, UK
[2] Department of Chemistry, Green Chemistry Centre of Excellence, University of York, Heslington, York YO10 5DD, UK
关键词: SSF;    Digestibility;    Lignin;    Hemicellulose;    Crystalline cellulose percentage;    H2SO4;    NaOH;    Miscanthus;    Temperature dependence;    Microwave pretreatment;   
Others  :  1228235
DOI  :  10.1186/s40508-015-0041-6
 received in 2015-05-16, accepted in 2015-09-15,  发布年份 2015
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【 摘 要 】

Background

Miscanthus is a major bioenergy crop in Europe and a potential feedstock for second generation biofuels. The most efficient and realistic method to produce fermentable sugars from lignocellulosic biomass is by enzymatic hydrolysis, assisted by thermo-chemical pretreatment. Recently, microwave technology has drawn growing attention, because of its unique effects and performance on biomass.

Result

In this work, microwave energy was applied to facilitate NaOH and H 2 SO 4pretreatment for Miscanthus under different temperatures (130–200 °C) for 20 min. The yields of reducing sugars from Miscanthus during the pretreatment process increased up to 180 °C and then declined with increasing temperature. Out results here showed a remarkable sugar yield from available carbohydrate (73 %) at the temperature of 180 °C by using 0.2 M H 2 SO 4 . In comparison with conventional heating pretreatment studied at same temperature with same biomass material, the reducing sugar release in this study was 17 times higher within half the time. It was highlighted that the major sugar component could be tuned by changing pretreatment temperature or pretreatment media. Optimally, the glucose and xylose yield from available carbohydrate are 47 and 22 % by using 0.2 M H 2 SO 4and NaOH respectively when temperature was 180 °C. The digestibility of pretreated Miscanthus was 10 times higher than that of untreated biomass. 68–86 % of the lignin content was removed from biomass by 0.2 M NaOH. Simultaneous saccharification fermentation (SSF) results showed an ethanol production of 143–152 mg/g biomass by using H 2 SO 4 /NaOH microwave assisted pretreatment, which is 7 times higher than that of untreated Miscanthus. Biomass morphology was studied by SEM, showing temperature has a strong influence on lignin removal process, as different lignin deposits were observed. At the temperature of 180 °C, NaOH pretreated biomass presented highly exposed fibres, which is a very important biomass characteristic for improved enzymatic hydrolysis.

Conclusion

Compared to conventional pretreatment, microwave assisted pretreatment is more energy efficient and faster, due to its unique heating mechanism leading to direct interaction between the polar part of biomass and electromagnetic field. The results of this work present promising potential for using microwave to assist biomass thermo-chemical pretreatment.

【 授权许可】

   
2015 Zhu et al.

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【 参考文献 】
  • [1]Ragauskas AJ, Williams CK, Davison BH, Britovsek G, Cairney J, Eckert CA, Frederick WJ, Hallett JP, Leak DJ, Liotta CL, et al.: The path forward for biofuels and biomaterials. Science 2006, 311(5760):484-489.
  • [2]Arthur J, Ragauskas MN, Kim DH, Eckert Charles A, Hallett Jason P, Liotta CL: From wood to fuels: integrating biofuels and pulp production. Ind Biotechnol 2006, 2(1):55-65.
  • [3]Bensah EC, Mensah M: Chemical pretreatment methods for the production of cellulosic ethanol: technologies and innovations. Int J Chem Eng 2013, 2013:21.
  • [4]Rivers DB, Emert GH: Lignocellulose pretreatment—a comparison of wet and dry ball attrition. Biotechnol Lett 1987, 9(5):365-368.
  • [5]Sun Y, Cheng JY: Hydrolysis of lignocellulosic materials for ethanol production: a review. Bioresour Technol 2002, 83(1):1-11.
  • [6]Kovacs K, Macrelli S, Szakacs G, Zacchi G: Enzymatic hydrolysis of steam-pretreated lignocellulosic materials with Trichoderma atroviride enzymes produced in-house. Biotechnol Biofuels 2009, 2:14. BioMed Central Full Text
  • [7]Balat M, Balat H, Oz C: Progress in bioethanol processing. Prog Energ Combust 2008, 34(5):551-573.
  • [8]Alizadeh H, Teymouri F, Gilbert TI, Dale BE: Pretreatment of switchgrass by ammonia fiber explosion (AFEX). Appl Biochem Biotech 2005, 121:1133-1141.
  • [9]Wang W, Yuan TQ, Wang K, Cui BK, Dai YC: Combination of biological pretreatment with liquid hot water pretreatment to enhance enzymatic hydrolysis of Populus tomentosa. Bioresour Technol 2012, 107:282-286.
  • [10]Kim KH, Hong J: Supercritical CO 2 pretreatment of lignocellulose enhances enzymatic cellulose hydrolysis. Bioresour Technol 2001, 77(2):139-144.
  • [11]Schacht C, Zetzl C, Brunner G: From plant materials to ethanol by means of supercritical fluid technology. J Supercrit Fluids 2008, 46(3):299-321.
  • [12]Morais ARC, da Costa Lopes AM, Bogel-Łukasik R: Carbon dioxide in biomass processing: contributions to the green biorefinery concept. Chem Rev 2015, 115(1):3-27.
  • [13]Nikolic S, Mojovic L, Rakin M, Pejin D, Pejin J: Utilization of microwave and ultrasound pretreatments in the production of bioethanol from corn. Clean Techn Environ Policy 2011, 13(4):587-594.
  • [14]Xu N, Zhang W, Ren SF, Liu F, Zhao CQ, Liao HF, Xu ZD, Huang JF, Li Q, Tu YY, et al.: Hemicelluloses negatively affect lignocellulose crystallinity for high biomass digestibility under NaOH and H 2 SO 4 pretreatments in Miscanthus. Biotechnol Biofuels 2012, 5:58. BioMed Central Full Text
  • [15]Canilha L, Santos VTO, Rocha GJM, Silva JBAE, Giulietti M, Silva SS, Felipe MGA, Ferraz A, Milagres AMF, Carvalho W: A study on the pretreatment of a sugarcane bagasse sample with dilute sulfuric acid. J Ind Microbiol Biot 2011, 38(9):1467-1475.
  • [16]Kaar WE, Holtzapple MT: Using lime pretreatment to facilitate the enzymic hydrolysis of corn stover. Biomass Bioenergy 2000, 18(3):189-199.
  • [17]da Costa Lopes AM, Bogel-Łukasik R: Acidic ionic liquids as sustainable approach of cellulose and lignocellulosic biomass conversion without additional catalysts. Chemsuschem 2015, 8(6):947-965.
  • [18]da Costa Lopes A, Joao K, Morais AR, Bogel-Lukasik E, Bogel-Lukasik R: Ionic liquids as a tool for lignocellulosic biomass fractionation. Sustain Chem Process 2013, 1(1):3. BioMed Central Full Text
  • [19]Chen L, Sharifzadeh M, Mac Dowell N, Welton T, Shah N, Hallett JP: Inexpensive ionic liquids: [HSO4]–based solvent production at bulk scale. Green Chem 2014, 16(6):3098-3106.
  • [20]Agnieszka Brandt JG, Hallett JP, Welton T: Deconstruction of lignocellulosic biomass with ionic liquids. Green Chem 2012, 15:550-583.
  • [21]Ju Y-H, Huynh L-H, Kasim NS, Guo T-J, Wang J-H, Fazary AE: Analysis of soluble and insoluble fractions of alkali and subcritical water treated sugarcane bagasse. Carbohydr Polym 2011, 83(2):591-599.
  • [22]Rezende CA, de Lima MA, Maziero P, deAzevedo ER, Garcia W, Polikarpov I: Chemical and morphological characterization of sugarcane bagasse submitted to a delignification process for enhanced enzymatic digestibility. Biotechnol Biofuels 2011, 4:1-18. BioMed Central Full Text
  • [23]Hong B, Xue GX, Weng LQ, Guo X: Pretreatment of moso bamboo with dilute phosphoric acid. Bioresources 2012, 7(4):4902-4913.
  • [24]Chen W-H, Tu Y-J, Sheen H-K: Disruption of sugarcane bagasse lignocellulosic structure by means of dilute sulfuric acid pretreatment with microwave-assisted heating. Appl Energy 2011, 88(8):2726-2734.
  • [25]Jensen JR, Morinelly JE, Gossen KR, Brodeur-Campbell MJ, Shonnard DR: Effects of dilute acid pretreatment conditions on enzymatic hydrolysis monomer and oligomer sugar yields for aspen, balsam, and switchgrass. Bioresour Technol 2010, 101(7):2317-2325.
  • [26]Mittal A, Katahira R, Himmel ME, Johnson DK: Effects of alkaline or liquid-ammonia treatment on crystalline cellulose: changes in crystalline structure and effects on enzymatic digestibility. Biotechnol Biofuels 2011, 4:41. BioMed Central Full Text
  • [27]Banerjee G, Car S, Scott-Craig JS, Hodge DB, Walton JD: Alkaline peroxide pretreatment of corn stover: effects of biomass, peroxide, and enzyme loading and composition on yields of glucose and xylose. Biotechnol Biofuels 2011, 4:16. BioMed Central Full Text
  • [28]Keshwani DR, Cheng JJ: Microwave-based alkali pretreatment of switchgrass and coastal bermudagrass for bioethanol production. Biotechnol Progr 2010, 26(3):644-652.
  • [29]Gupta R, Lee YY: Investigation of biomass degradation mechanism in pretreatment of switchgrass by aqueous ammonia and sodium hydroxide. Bioresour Technol 2010, 101(21):8185-8191.
  • [30]Zhu S, Wu Y, Yu Z, Chen Q, Wu G, Yu F, Wang C, Jin S: Microwave-assisted alkali pre-treatment of wheat straw and its enzymatic hydrolysis. Biosyst Eng 2006, 94(3):437-442.
  • [31]de la Hoz A, Diaz-Ortiz A, Moreno A: Microwaves in organic synthesis. Thermal and non-thermal microwave effects. Chem Soc Rev 2005, 34(2):164-178.
  • [32]Lancaster M: Green chemistry: an introductory text. R Soc Chem, Cambridge; 2002.
  • [33]Macquarrie DJ, Clark JH, Fitzpatrick E: The microwave pyrolysis of biomass. Biofuels Bioprod Biorefin 2012, 6(5):549-560.
  • [34]Lu X, Xi B, Zhang Y, Angelidaki I: Microwave pretreatment of rape straw for bioethanol production: focus on energy efficiency. Bioresour Technol 2011, 102(17):7937-7940.
  • [35]Wu YY, Fu ZH, Yin DL, Xu Q, Liu FL, Lu CL, Mao LQ: Microwave-assisted hydrolysis of crystalline cellulose catalyzed by biomass char sulfonic acids. Green Chem 2010, 12(4):696-700.
  • [36]Ma H, Liu WW, Chen X, Wu YJ, Yu ZL: Enhanced enzymatic saccharification of rice straw by microwave pretreatment. Bioresour Technol 2009, 100(3):1279-1284.
  • [37]Lee W-C, Kuan W-C: Miscanthus as cellulosic biomass for bioethanol production. Biotechnol J 2015, 10(6):840-854.
  • [38]Zhu SD, Wu YX, Yu ZN, Zhang X, Li H, Gao M: The effect of microwave irradiation on enzymatic hydrolysis of rice straw. Bioresour Technol 2006, 97(15):1964-1968.
  • [39]Luo J, Cai M, Gu T: Pretreatment of lignocellulosic biomass using green ionic liquids. In Green biomass pretreatment for biofuels production. Edited by Gu T. Springer, Netherlands; 2013:127-153.
  • [40]Budarin VL, Clark JH, Lanigan BA, Shuttleworth P, Macquarrie DJ: Microwave assisted decomposition of cellulose: a new thermochemical route for biomass exploitation. Bioresour Technol 2010, 101(10):3776-3779.
  • [41]Fan JJ, De Bruyn M, Budarin VL, Gronnow MJ, Shuttleworth PS, Breeden S, Macquarrie DJ, Clark JH: Direct microwave-assisted hydrothermal depolymerization of cellulose. J Am Chem Soc 2013, 135(32):11728-11731.
  • [42]Ju YH, Huynh LH, Kasim NS, Guo TJ, Wang JH, Fazary AE: Analysis of soluble and insoluble fractions of alkali and subcritical water treated sugarcane bagasse. Carbohydr Polym 2011, 83(2):591-599.
  • [43]Lee YY, Iyer P, Torget RW: Dilute-acid hydrolysis of lignocellulosic biomass. In Recent progress in bioconversion of lignocellulosics. Edited by Tsao GT, Brainard AP, Bungay HR, Cao NJ, Cen P, Chen Z, Du J, Foody B, Gong CS, Hall P. Springer, Berlin; 1999:93-115.
  • [44]Jing Q, Lu XY: Kinetics of non-catalyzed decomposition of glucose in high-temperature liquid water. Chin J Chem Eng 2008, 16(6):890-894.
  • [45]Girisuta B, Janssen LPBM, Heeres HJ: Green chemicals: a kinetic study on the conversion of glucose to levulinic acid. Chem Eng Res Des 2006, 84(5):339-349.
  • [46]Moller M, Schroder U: Hydrothermal production of furfural from xylose and xylan as model compounds for hemicelluloses. Rsc Adv 2013, 3(44):22253-22260.
  • [47]Jing Q, Lü X: Kinetics of non-catalyzed decomposition of D-xylose in high temperature liquid water*. Chin J Chem Eng 2007, 15(5):666-669.
  • [48]Yu G, Afzal W, Yang F, Padmanabhan S, Liu Z, Xie H, Shafy MA, Bell AT, Prausnitz JM: Pretreatment of Miscanthus × giganteus using aqueous ammonia with hydrogen peroxide to increase enzymatic hydrolysis to sugars. J Chem Technol Biotechnol 2014, 89(5):698-706.
  • [49]Haverty D, Dussan K, Piterina AV, Leahy JJ, Hayes MHB: Autothermal, single-stage, performic acid pretreatment of Miscanthus x giganteus for the rapid fractionation of its biomass components into a lignin/hemicellulose-rich liquor and a cellulase-digestible pulp. Bioresour Technol 2012, 109:173-177.
  • [50]Gómez L, Vanholme R, Bird S, Goeminne G, Trindade L, Polikarpov I, Simister R, Morreel K, Boerjan W, McQueen-Mason S: Side by side comparison of chemical compounds generated by aqueous pretreatments of maize stover, Miscanthus and sugarcane bagasse. Bioenerg Res 2014, 7(4):1466-1480.
  • [51]Donohoe BS, Decker SR, Tucker MP, Himmel ME, Vinzant TB: Visualizing lignin coalescence and migration through maize cell walls following thermochemical pretreatment. Biotechnol Bioeng 2008, 101(5):913-925.
  • [52]Chang VS, Nagwani M, Kim CH, Holtzapple MT: Oxidative lime pretreatment of high-lignin biomass—poplar wood and newspaper. Appl Biochem Biotech 2001, 94(1):1-28.
  • [53]Mosier N, Wyman C, Dale B, Elander R, Lee YY, Holtzapple M, Ladisch M: Features of promising technologies for pretreatment of lignocellulosic biomass. Bioresour Technol 2005, 96(6):673-686.
  • [54]Li JB, Henriksson G, Gellerstedt G: Lignin depolymerization/repolymerization and its critical role for delignification of aspen wood by steam explosion. Bioresour Technol 2007, 98(16):3061-3068.
  • [55]Selig MJ, Viamajala S, Decker SR, Tucker MP, Himmel ME, Vinzant TB: Deposition of lignin droplets produced during dilute acid pretreatment of maize stems retards enzymatic hydrolysis of cellulose. Biotechnol Progr 2007, 23(6):1333-1339.
  • [56]Fan J, Debruyn M, Zhu Z, Budarin V, Gronnow M, Gomez LD, Macquarrie D, Clark J: Microwave-enhanced formation of glucose from cellulosic waste. Chem Eng Process Process Intensif 2013, 71:37-42.
  • [57]Titirici M-M, Antonietti M, Baccile N: Hydrothermal carbon from biomass: a comparison of the local structure from poly- to monosaccharides and pentoses/hexoses. Green Chem 2008, 10(11):1204-1212.
  • [58]Larsson S, Palmqvist E, Hahn-Hägerdal B, Tengborg C, Stenberg K, Zacchi G, Nilvebrant N-O: The generation of fermentation inhibitors during dilute acid hydrolysis of softwood. Enzyme Microb Tech 1999, 24(3–4):151-159.
  • [59]Jones L, Milne JL, Ashford D, McQueen-Mason SJ: Cell wall arabinan is essential for guard cell function. Proc Natl Acad Sci USA 2003, 100(20):11783-11788.
  • [60]Foster CE, Martin TM, Pauly M: Comprehensive compositional analysis of plant cell walls (lignocellulosic biomass) Part II: carbohydrates. J Vis Exp 2010, 37:e1837.
  • [61]Foster CE, Martin TM, Pauly M: Comprehensive compositional analysis of plant cell walls (lignocellulosic biomass) Part I: lignin. J Vis Exp 2010, 37:e1745.
  • [62]Gomez LD, Whitehead C, Barakate A, Halpin C, McQueen-Mason SJ: Automated saccharification assay for determination of digestibility in plant materials. Biotechnol Biofuels 2010, 3(1):23. BioMed Central Full Text
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