期刊论文详细信息
Biotechnology for Biofuels
Bioelectricity versus bioethanol from sugarcane bagasse: is it worth being flexible?
Roberto C Giordano1  Raquel LC Giordano1  Antonio JG Cruz1  Caliane BB Costa1  Fabio HPB Pinto2  Renato Tonon Filho2  Felipe F Furlan2 
[1]Department of Chemical Engineering, Federal University of São Carlos, DEQ/UFSCar Via Washington Luis, km 235, São Carlos, SP, Brazil
[2]Chemical Engineering Graduate Program, Federal University of São Carlos, PPGEQ/UFSCar Via Washington Luis, km 235, São Carlos, SP, Brazil
关键词: Process simulation;    Bagasse;    Sugarcane;    Lignocellulose;    Techno-economic evaluation;    Second generation ethanol production;   
Others  :  797884
DOI  :  10.1186/1754-6834-6-142
 received in 2013-05-01, accepted in 2013-09-24,  发布年份 2013
PDF
【 摘 要 】

Background

Sugarcane is the most efficient crop for production of (1G) ethanol. Additionally, sugarcane bagasse can be used to produce (2G) ethanol. However, the manufacture of 2G ethanol in large scale is not a consolidated process yet. Thus, a detailed economic analysis, based on consistent simulations of the process, is worthwhile. Moreover, both ethanol and electric energy markets have been extremely volatile in Brazil, which suggests that a flexible biorefinery, able to switch between 2G ethanol and electric energy production, could be an option to absorb fluctuations in relative prices. Simulations of three cases were run using the software EMSO: production of 1G ethanol + electric energy, of 1G + 2G ethanol and a flexible biorefinery. Bagasse for 2G ethanol was pretreated with a weak acid solution, followed by enzymatic hydrolysis, while 50% of sugarcane trash (mostly leaves) was used as surplus fuel.

Results

With maximum diversion of bagasse to 2G ethanol (74% of the total), an increase of 25.8% in ethanol production (reaching 115.2 L/tonne of sugarcane) was achieved. An increase of 21.1% in the current ethanol price would be enough to make all three biorefineries economically viable (11.5% for the 1G + 2G dedicated biorefinery). For 2012 prices, the flexible biorefinery presented a lower Internal Rate of Return (IRR) than the 1G + 2G dedicated biorefinery. The impact of electric energy prices (auction and spot market) and of enzyme costs on the IRR was not as significant as it would be expected.

Conclusions

For current market prices in Brazil, not even production of 1G bioethanol is economically feasible. However, the 1G + 2G dedicated biorefinery is closer to feasibility than the conventional 1G + electric energy industrial plant. Besides, the IRR of the 1G + 2G biorefinery is more sensitive with respect to the price of ethanol, and an increase of 11.5% in this value would be enough to achieve feasibility. The ability of the flexible biorefinery to take advantage of seasonal fluctuations does not make up for its higher investment cost, in the present scenario.

【 授权许可】

   
2013 Furlan et al.; licensee BioMed Central Ltd.

【 预 览 】
附件列表
Files Size Format View
20140706083534698.pdf 537KB PDF download
Figure 7. 51KB Image download
Figure 6. 39KB Image download
Figure 5. 55KB Image download
Figure 4. 36KB Image download
Figure 3. 55KB Image download
Figure 2. 19KB Image download
Figure 1. 27KB Image download
【 图 表 】

Figure 1.

Figure 2.

Figure 3.

Figure 4.

Figure 5.

Figure 6.

Figure 7.

【 参考文献 】
  • [1]Macedo IC, Seabra JEA, Silva JEAR: Green house gases emissions in the production and use of ethanol from sugarcane in Brazil: The 2005/2006 averages and a prediction for 2020. Biomass Bioenergy 2008, 32:582-595.
  • [2]Zanin GM, Santana CC, Bon EPS, Giordano RLC, Moraes FF, Andrietta SR, Neto CCC, Macedo IC, Fo DL, Ramos LP, Fontana J: Brazilian bioethanol program. Appl Biochem Biotechnol 2000, 84:1147-1163.
  • [3]National Association of Motor Vehicles (ANFAVEA): Brazilian automotive industry yearbook. Tech. rep., São Paulo, 2012
  • [4]Gnansounou E: Production and use of lignocellulosic bioethanol in Europe: Current situation and perspectives. Bioresour Technol 2010, 101:4842-4850.
  • [5]Hassuani SJ, Leal MRLV, Macedo IC: Biomass power generation: Sugarcane bagasse and trash. Piracicaba: United Nations Development Programme and Sugarcane Technology Centre; 2005.
  • [6]Electric Energy National Agency – ANEEL (in portuguese) http://www.aneel.gov.br webcite
  • [7]Electric Energy Commercialization Chamber – CCEE (acronym in portuguese) http://www.ccee.org.br/ webcite
  • [8]Center of Advanced Studies in Applied Economy – CEPEA/ESALQ/USP (in portuguese) http://www.cepea.esalq.usp.br webcite
  • [9]Seabra JE, Macedo IC: Comparative analysis for power generation and ethanol production from sugarcane residual biomass in Brazil. Energy Policy 2011, 39:421-428. http://www.sciencedirect.com/science/article/pii/S0301421510007706 webcite
  • [10]Dias MO, Cunha MP, Jesus CD, Rocha GJ, Pradella JGC, Rossell CE, Maciel Filho R, Bonomi A: Second generation ethanol in Brazil: Can it compete with electricity production? Bioresour Technol 2011, 102(19):8964-8971.
  • [11]Macrelli S, Mogensen J, Zacchi G, et al.: Techno-economic evaluation of 2 nd generation bioethanol production from sugar cane bagasse and leaves integrated with the sugar-based ethanol process. Biotechnol Biofuels 2012, 5:22. BioMed Central Full Text
  • [12]Dias M, Junqueira T, Cavalett O, Cunha MP, Jesus C, Rossell C, Filho R, Bonomi A: Integrated versus stand-alone second generation ethanol production from sugarcane bagasse and trash. Bioresour Technol 2012, 103:152-161.
  • [13]Soares RP, Secchi AR: EMSO: A new environment for modelling, simulation and optimisation. Comput Aided Chem Eng 2003, 14:947-952.
  • [14]Agblevor F, Rejai B, Wang D, Wiselogel A, Chum H: blueInfluence of storage conditions on the production of hydrocarbons from herbaceous biomass. Biomass Bioenergy 1994, 7:213-222.
  • [15]Eggeman T, Elander RT: Process and economic analysis of pretreatment technologies. Bioresource Technol 2005, 96(18):2019-2025.
  • [16]Furlan FF, Costa CBB, Fonseca GC, Soares RP, Secchi AR, Cruz AJG, Giordano RC: Assessing the production of first and second generation bioethanol from sugarcane through the integration of global optimization and process detailed modeling. Comput Chem Eng 2012, 43:1-9.
  • [17]Canilha L, Chandel AK, Suzane dos Santos Milessi T, Antunes FAF, Luiz da Costa Freitas W, das Graças Almeida Felipe M, da Silva SS: Bioconversion of sugarcane biomass into ethanol: An overview about composition, pretreatment methods, detoxification of hydrolysates, enzymatic saccharification, and ethanol fermentation. J Biomed Biotechnol 2012, 2012:1-15.
  • [18]Wooley R, Putsche V: Development of an ASPEN PLUS physical property database for biofuels components. NREL,Tech. rep., Report MP-425-20685 1996, 38
  • [19]Silva C, Zangirolami T, Rodrigues J, Matugi K, Giordano R, Giordano R: An innovative biocatalyst for production of ethanol from xylose in a continuous bioreactor. Enzyme Microb Technol 2012, 50:35-42.
  • [20]Pereira LTC, Pereira LTC, Teixeira RSS, Bon EPS, Freitas SP: Sugarcane bagasse enzymatic hydrolysis: rheological data as criteria for impeller selection. J Ind Microbiol Biotechnol 2011, 38(8):901-907.
  • [21]Rodrigues R, Soares RP, Secchi AR: Teaching chemical reaction engineering using EMSO simulator. Comput Appl Eng Educ 2010, 18(4):607-618.
  文献评价指标  
  下载次数:86次 浏览次数:24次