期刊论文详细信息
Biotechnology for Biofuels
Butanol production from food waste: a novel process for producing sustainable energy and reducing environmental pollution
Haibo Huang2  Vijay Singh2  Nasib Qureshi1 
[1] Bioenergy Research Unit, United States Department of Agriculture, ARS, National Center for Agricultural Utilization Research, 1815N. University Street, Peoria 61604, IL, USA
[2] Department of Agricultural and Biological Engineering, University of Illinois at Urbana Champaign, 1304W. Pennsylvania Avenue., Urbana 61801, IL, USA
关键词: Energy;    Process integration;    Vacuum stripping;    Fermentation;    Food waste;    Butanol;   
Others  :  1228131
DOI  :  10.1186/s13068-015-0332-x
 received in 2015-04-21, accepted in 2015-09-01,  发布年份 2015
PDF
【 摘 要 】

Background

Waste is currently a major problem in the world, both in the developing and the developed countries. Efficient utilization of food waste for fuel and chemical production can positively influence both the energy and environmental sustainability. This study investigated using food waste to produce acetone, butanol, and ethanol (ABE) by Clostridium beijerinckii P260.

Results

In control fermentation, 40.5 g/L of glucose (initial glucose 56.7 g/L) was used to produce 14.2 g/L of ABE with a fermentation productivity and a yield of 0.22 g/L/h and 0.35 g/g, respectively. In a similar fermentation 81 g/L of food waste (containing equivalent glucose of 60.1 g/L) was used as substrate, and the culture produced 18.9 g/L ABE with a high ABE productivity of 0.46 g/L/h and a yield of 0.38 g/g. Fermentation of food waste at higher concentrations (129, 181 and 228 g/L) did not remarkably increase ABE production but resulted in high residual glucose due to the culture butanol inhibition. An integrated vacuum stripping system was designed and applied to recover butanol from the fermentation broth simultaneously to relieve the culture butanol inhibition, thereby allowing the fermentation of food waste at high concentrations. ABE fermentation integrated with vacuum stripping successfully recovered the ABE from the fermentation broth and controlled the ABE concentrations below 10 g/L during fermentation when 129 g/L food waste was used. The ABE productivity with vacuum fermentation was 0.49 g/L/h, which was 109 % higher than the control fermentation (glucose based). More importantly, ABE vacuum recovery and fermentation allowed near-complete utilization of the sugars (~98 %) in the broth.

Conclusions

In these studies it was demonstrated that food waste is a superior feedstock for producing butanol using Clostridium beijerinckii. Compared to costly glucose, ABE fermentation of food waste has several advantages including lower feedstock cost, higher productivity, and less residual sugars.

【 授权许可】

   
2015 Huang et al.

【 预 览 】
附件列表
Files Size Format View
20151010000625474.pdf 1964KB PDF download
Fig.8. 33KB Image download
Fig.7. 70KB Image download
Fig.6. 15KB Image download
Fig.5. 53KB Image download
Fig.4. 89KB Image download
Fig.3. 35KB Image download
Fig.2. 72KB Image download
Fig.1. 30KB Image download
【 图 表 】

Fig.1.

Fig.2.

Fig.3.

Fig.4.

Fig.5.

Fig.6.

Fig.7.

Fig.8.

【 参考文献 】
  • [1]Zhang R, El-Mashad HM, Hartman K, Wang F, Liu G, Choate C, et al.: Characterization of food waste as feedstock for anaerobic digestion. Bioresour Technol 2007, 98:929-935.
  • [2]EPA. The Food Recovery Hierarchy. 2012. http://www.epa.gov/foodrecovery/. Accessed 22 Sep 2014.
  • [3]Cuéllar AD, Webber ME: Wasted food, wasted energy: the embedded energy in food waste in the United States. Environ Sci Technol 2010, 44:6464-6469.
  • [4]Lin CSK, Pfaltzgraff LA, Herrero-Davila L, Mubofu EB, Abderrahim S, Clark JH, et al.: Food waste as a valuable resource for the production of chemicals, materials and fuels. Current situation and global perspective. Energy. Environ Sci. 2013, 6:426-464.
  • [5]Moon HC, Song IS, Kim JC, Shirai Y, Lee DH, Kim JK, et al.: Enzymatic hydrolysis of food waste and ethanol fermentation. Int J Energ Res. 2009, 33:164-172.
  • [6]Uncu ON, Cekmecelioglu D: Cost-effective approach to ethanol production and optimization by response surface methodology. Waste Manage 2011, 31:636-643.
  • [7]Kim JK, Oh BR, Chun YN, Kim SW: Effects of temperature and hydraulic retention time on anaerobic digestion of food waste. J Biosci Bioeng 2006, 102:328-332.
  • [8]Lee D-Y, Ebie Y, Xu K-Q, Li Y-Y, Inamori Y: Continuous H 2 and CH 4 production from high-solid food waste in the two-stage thermophilic fermentation process with the recirculation of digester sludge. Bioresour Technol 2010, 101:S42-S47.
  • [9]Ma J, Duong TH, Smits M, Verstraete W, Carballa M: Enhanced biomethanation of kitchen waste by different pre-treatments. Bioresour Technol 2011, 102:592-599.
  • [10]Nakamura Y, Sawada T: Ethanol production from artificial domestic household waste solubilized by steam explosion. Biotechnol Bioprocess Eng 2003, 8:205-209.
  • [11]Kim JH, Lee JC, Pak D: Feasibility of producing ethanol from food waste. Waste Manage 2011, 31:2121-2125.
  • [12]Matsakas L, Kekos D, Loizidou M, Christakopoulos P: Utilization of household food waste for the production of ethanol at high dry material content. Biotechnol Biofuels 2014, 18:1-19.
  • [13]Huang H, Qureshi N, Chen MH, Liu W, Singh V: Ethanol production from food waste at high solids content with vacuum recovery technology. J Agric Food Chem 2015, 63:2760-2766.
  • [14]Tao L, He X, Tan EC, Zhang M, Aden A: Comparative techno-economic analysis and reviews of n-butanol production from corn grain and corn stover. Biofuels Bioprod Biorefin 2014, 8:342-361.
  • [15]Lan EI, Ro SY, Liao JC: Oxygen-tolerant coenzyme A-acylating aldehyde dehydrogenase facilitates efficient photosynthetic n-butanol biosynthesis in cyanobacteria. Energy Environ Sci 2013, 6:2672-2681.
  • [16]Qureshi N, Saha BC, Cotta MA: Butanol production from wheat straw hydrolysate using Clostridium beijerinckii. Bioprocess Biosyst Eng 2007, 30:419-427.
  • [17]Qureshi N, Saha BC, Hector RE, Hughes S, Cotta MA: Butanol production from wheat straw by simultaneous saccharification and fermentation using Clostridium beijerinckii part 1: batch fermentation. Biomass Bioenergy 2008, 32:168-175.
  • [18]Wang L, Chen H: Increased fermentability of enzymatically hydrolyzed steam-exploded corn stover for butanol production by removal of fermentation inhibitors. Process Biochem 2011, 46:604-607.
  • [19]Qureshi N, Singh V, Liu S, Ezeji TC, Saha BC, Cotta MA: Process integration for simultaneous sacchrification, fermentation, and recovery (SSFR): production of butanol from corn stover using Clostridium beijerinckii P260. Bioresour Technol 2014, 154:222-228.
  • [20]Qureshi N, Saha BC, Dien BS, Hector R, Cotta MA: Production of butanol from agricultural residues: use of barley straw hydrolysate. Biomass Bioenergy 2010, 34:559-565.
  • [21]Lu C, Zhao J, Yang S-T, Wei D: Fed-batch fermentation for n-butanol production from cassava bagasse hydrolysate in a fibrous bed bioreactor with continuous gas stripping. Bioresour Technol 2012, 104:380-387.
  • [22]Gao K, Boiano S, Marzocchella A, Rehmann L: Cellulosic butanol production from alkali-pretreated switchgrass (Panicum virgatum) and phragmites (Phragmites australis). Bioresour Technol 2014, 174:176-181.
  • [23]Zhang Y, Ezeji TC: Elucidating and alleviating impacts of lignocellulose-derived microbial inhibitors on Clostridium beijerinckii during fermentation of Miscanthus giganteus to butanol. J Ind Microbiol Biotechnol 2014, 41:1505-1516.
  • [24]Liu Z, Ying Y, Li F, Ma C, Xu P: Butanol production by Clostridium beijerinckii ATCC 55025 from wheat bran. J Ind Microbiol Biotechnol 2010, 37:495-501.
  • [25]Humbird D, Davis R, Tao L, Kinchin C, Hsu D, Aden A, Schoen P, Lukas J, Olthof B, Worley M, Sexton D, Dudgeon D. Process design and economics for biochemical conversion of lignocellulosic biomass to ethanol. Diluteacid pretreatment and enzymatic hydrolysis of corn stover. 2011.. http://www.nrel.gov/biomass/pdfs/47764.pdf webcite
  • [26]Maddox I, Qureshi N, Roberts-Thomson K: Production of acetone-butanol-ethanol from concentrated substrate using clostridium acetobutylicum in an integrated fermentation-product removal process. Process Biochem 1995, 30:209-215.
  • [27]Mariano AP, Qureshi N, Ezeji TC: Bioproduction of butanol in bioreactors: new insights from simultaneous in situ butanol recovery to eliminate product toxicity. Biotechnol Bioeng 2011, 108:1757-1765.
  • [28]Wang P, Singh V, Xue H, Johnston DB, Rausch KD, Tumbleson M: Comparison of raw starch hydrolyzing enzyme with conventional liquefaction and saccharification enzymes in dry-grind corn processing. Cereal Chem 2007, 84:10-14.
  • [29]Shihadeh JK, Huang H, Rausch KD, Tumbleson ME, Singh V: Design of a vacuum flashing system for high-solids fermentation of corn. Transac ASABE. 2013, 56:1441-1447.
  • [30]Shihadeh JK, Huang H, Rausch KD, Tumbleson ME, Singh V: Vacuum Stripping of ethanol during high solids fermentation of corn. Appl Biochem Biotechnol 2014, 173:486-500.
  • [31]Mariano AP, Qureshi N, Filho RM, Ezeji TC: Assessment of in situ butanol recovery by vacuum during acetone butanol ethanol (ABE) fermentation. J Chem Technol Biotechnol 2012, 87:334-340.
  • [32]Qureshi N, Blaschek H: Recovery of butanol from fermentation broth by gas stripping. Renew Energy 2001, 22:557-564.
  • [33]Ezeji TC, Qureshi N, Blaschek HP: Bioproduction of butanol from biomass: from genes to bioreactors. Curr Opin Biotechnol 2007, 18:220-227.
  • [34]Xue C, Zhao J, Lu C, Yang ST, Bai F, Tang I: High-titer n-butanol production by clostridium acetobutylicum JB200 in fed-batch fermentation with intermittent gas stripping. Biotechnol Bioeng 2012, 109:2746-2756.
  • [35]Ezeji TC, Qureshi N, Blaschek HP: Production of acetone, butanol and ethanol by Clostridium beijerinckii BA101 and in situ recovery by gas stripping. World J Microbiol Biotechnol 2003, 19:595-603.
  • [36]Phillips J, Humphrey A: Process technology for the biological conversion of lignocellulosic materials to fermentable sugars and alcohols. In Wood and agricultural residues: research on use for feed, fuels and chemicals. Edited by Soltes EJ. Academic Press, New York; 1983:503-528.
  • [37]Ennis B, Marshall C, Maddox I, Paterson A: Continuous product recovery by in situ gas stripping/condensation during solvent production from whey permeate using Clostridium acetobutylicum. Biotechnol Lett 1986, 8:725-730.
  • [38]Lu C, Dong J, Yang S-T: Butanol production from wood pulping hydrolysate in an integrated fermentation–gas stripping process. Bioresour Technol 2013, 143:467-475.
  • [39]Ezeji T, Qureshi N, Blaschek H: Acetone butanol ethanol (ABE) production from concentrated substrate: reduction in substrate inhibition by fed-batch technique and product inhibition by gas stripping. Appl Microbiol Biotechnol 2004, 63:653-658.
  • [40]Yan S, Li J, Chen X, Wu J, Wang P, Ye J, et al.: Enzymatical hydrolysis of food waste and ethanol production from the hydrolysate. Renew Energ. 2011, 36:1259-1265.
  • [41]AACC International: Approved methods of the American Association of Cereal Chemists. 10th edition. The Association, St Paul; 2000. (Methods 44-19)
  • [42]Vidal BC, Rausch KD, Tumbleson ME, Singh V: Determining corn germ and pericarp residual starch by acid hydrolysis. Cereal Chem 2009, 86:133-135.
  • [43]ANKOM Technology. Neutral detergent fiber in feeds—filter bag technique. 2003. http://www.johnmorriscomau/files/product/attachments/4469/68518_opt2.pdf. Accessed 22 Oct 2014.
  • [44]Ezeji TC, Qureshi N, Blaschek HP: Butanol fermentation research: upstream and downstream manipulations. Chem Rec 2004, 4:305-314.
  • [45]Huang H, Liu W, Singh V, Danao M-GC, Eckhoff SR: Effect of harvest moisture content on selected yellow dent corn: dry-grind fermentation characteristics and DDGS composition. Cereal Chem 2012, 89:217-221.
  文献评价指标  
  下载次数:164次 浏览次数:37次