Biotechnology for Biofuels | |
Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation | |
De-Shun Lin2  Hong-Wei Yen4  Wei-Chen Kao2  Chieh-Lun Cheng2  Wen-Ming Chen1  Chieh-Chen Huang5  Jo-Shu Chang3  | |
[1] Department of Seafood Science, National Kaohsiung Marine University, Kaohsiung 811, Taiwan | |
[2] Department of Chemical Engineering, National Cheng Kung University, Tainan, Taiwan | |
[3] Research Center for Energy Technology and Strategy, National Cheng Kung University, Tainan, Taiwan | |
[4] Department of Chemical and Materials Engineering, Tunghai University, Taichung, Taiwan | |
[5] Agricultural Biotechnology Center, National Chung Hsing University, Taichung, Taiwan | |
关键词: Glycerol; Butyrate addition; Vacuum membrane distillation (VMD); Clostridium pasteurianum; Bio-butanol; | |
Others : 1229684 DOI : 10.1186/s13068-015-0352-6 |
|
received in 2015-04-21, accepted in 2015-09-30, 发布年份 2015 |
【 摘 要 】
Background
Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration.
Results
Adding 6 g L −1butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol) −1 . Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g L −1 , while the yield was also improved to 0.39 mol butanol (mol glycerol) −1 . The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution.
Conclusions
The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective.
【 授权许可】
2015 Lin et al.
Files | Size | Format | View |
---|---|---|---|
Fig.6. | 34KB | Image | download |
Fig.5. | 69KB | Image | download |
Fig.4. | 78KB | Image | download |
Fig.3. | 69KB | Image | download |
Fig.2. | 69KB | Image | download |
Fig.1. | 46KB | Image | download |
Fig.6. | 34KB | Image | download |
Fig.5. | 69KB | Image | download |
Fig.4. | 78KB | Image | download |
Fig.3. | 69KB | Image | download |
Fig.2. | 69KB | Image | download |
Fig.1. | 46KB | Image | download |
【 图 表 】
Fig.1.
Fig.2.
Fig.3.
Fig.4.
Fig.5.
Fig.6.
Fig.1.
Fig.2.
Fig.3.
Fig.4.
Fig.5.
Fig.6.
【 参考文献 】
- [1]Ma FR, Hanna MA: Biodiesel production: a review. Bioresour Technol 1999, 70:1-15.
- [2]May YK, Tinia IMG: A review of biodiesel production from Jatropha curcas L. oil. Renew Sust Energ Rev. 2011, 15:2240-2251.
- [3]Lee SY, et al.: Fermentative butanol production by Clostridia. Biotechnol Bioeng 2008, 101:209-228.
- [4]Bellido C, et al.: Efficient acetone–butanol–ethanol production by Clostridium beijerinckii from sugar beet pulp. Bioresour Technol 2015, 190:332-338.
- [5]Cheng HH, et al.: Biological butanol production from microalgae-based biodiesel residues by Clostridium acetobutylicum. Bioresour Technol 2015, 184:379-385.
- [6]Biebl H: Fermentation of glycerol by Clostridium pasteurianum-batch and continuous culture studies. J Ind Microbiol Biotechnol 2001, 27:18-26.
- [7]Dabrock B, Bahl H, Gottschalk G: Parameters affecting solvent production by Clostridium pasteurianum. Appl Environ Microbiol 1992, 58:1233-1239.
- [8]Kao WC, et al.: Enhancing butanol production with Clostridium pasteurianum CH4 using sequential glucose-glycerol addition and simultaneous dual-substrate cultivation strategies. Bioresour Technol 2013, 135:324-330.
- [9]Taconi KA, Venkataramanan KP, Johnson DT: Growth and solvent production by Clostridium pasteurianum ATCC ® 6013TM utilizing biodiesel-derived crude glycerol as the sole carbon source. Environ Prog Sustain 2009, 28:100-110.
- [10]Maddox IS, Qureshi N, Thomson KR: Production of acetone–butanol–ethanol from concentrated substrate using Clostridium acetobutylicum in an integrated fermentation-product removal process. Process Biochem 1995, 30:209-215.
- [11]Qureshi N, Maddox IS: Reduction in butanol inhibition by perstraction: utilization of concentrated lactose/whey permeate by Clostridium acetobutylicum to enhance butanol fermentation economics. Food Bioprod Process 2005, 83:43-52.
- [12]Branduardi P, et al.: Microbial n-butanol production from Clostridia to non-Clostridial hosts. Eng Life Sci 2014, 14:16-26.
- [13]Jeon YJ, Lee YY: In situ product separation in butanol fermentation by membrane-assisted extraction. Enzyme Microbiol Technol 1989, 11:575-582.
- [14]Vane LM: Separation technologies for the recovery and dehydration of alcohols from fermentation broths. Biofuel Bioprod Biorefinery 2008, 2:553-588.
- [15]Yen H, Chen Z-H, Yang I-K: Use of the composite membrane of poly(ether-block-amide) and carbon nanotubes (CNTs) in a pervaporation system incorporated with fermentation for butanol production by Clostridium acetobutylicum. Bioresour Technol 2012, 109:105-109.
- [16]Saketa Y, et al.: Potable water recovery from As, U, and F contaminated ground waters by direct contact membrane distillation process. J Hazard Mater 2011, 192:1388-1394.
- [17]Alklaibi AM, Lior N: Membrane-distillation desalination: status and potential. Desalination 2004, 171:111-131.
- [18]Zheng YN, et al.: Problems with the microbial production of butanol. J Ind Microbiol Biotechnol 2009, 36:1127-1138.
- [19]Chiam C-K, Sarbatly R: Vacuum membrane distillation processes for aqueous solution treatment—a review. Chem Eng Process 2013, 74:27-54.
- [20]Regestein L, et al.: Impact of butyric acid on butanol formation by Clostridium pasteurianum. Bioresour Technol 2015, 196:153-159.
- [21]Van GS, Sung SW, Lay JJ: Biohydrogen production as a function of pH and substrate concentration. Environ Sci Technol 2001, 35:4726-4730.
- [22]Lin CY, Lay CH: Effects of carbonate and phosphate concentrations on hydrogen production using anaerobic sewage sludge microflora. Int J Hydrog Energy 2004, 29:275-281.
- [23]Mu Y, Yu HQ, Wang G: A kinetic approach to anaerobic hydrogen-producing process. Water Res 2007, 41:1152-1160.
- [24]Tashiro Y, et al.: High butanol production by Clostridium saccharoperbutylacetonicum N1-4 in fed-batch culture with pH-stat continuous butyric acid and glucose feeding method. J Boisci Bioeng 2004, 98:263-268.
- [25]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.
- [26]Lee KS, et al.: Anaerobic hydrogen production with an efficient carrier-induced granular sludge bed bioreactor. Biotechnol Bioeng 2004, 87:648-657.
- [27]Cheng CL, et al.: High yield biobutanol production by solvent-producing bacterial microflora. Bioresour Technol 2012, 113:58-64.
- [28]Ahn J-H, Sang B-I, Um Y: Butanol production from thin stillage using Clostridium pasteurianum. Bioresour Technol 2011, 102:4934-4937.
- [29]Qureshi N, et al.: Acetone butanol ethanol (ABE) recovery by pervaporation using silicalite-silicone composite membrane from fed-batch reactor of Clostridium acetobutylicum. J Membr Sci. 2001, 187:93-102.
- [30]Qureshi N, et al.: Removal of fermentation inhibitors from alkaline peroxide pretreated and enzymatically hydrolyzed wheat straw: production of butanol from hydrolysate using Clostridium beijerinckii in batch reactors. Biomass Bioenerg 2008, 32:1353-1358.
- [31]Xue C, et al.: High-titer n-butanol production by Clostridium acetobutylicum JB200 in fed-batch fermentation with intermittent gas stripping. Biotechnol Bioeng 2012, 109:2746-2756.
- [32]Minier M, et al.: Extractive acetonobutylic fermentation by coupling ultrafiltration and distillation. Biotechnol Bioeng 1990, 35:861-869.