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Two-stage biogas production by co-digesting molasses wastewater and sewage sludge
- 作者:Jung-Yeol Lee (1) (2)
Jeonghee Yun (2) Tae Gwan Kim (2) Daehyun Wee (1) (2) Kyung-Suk Cho (1) (2)
- 关键词:Co ; digestion ; Molasses ; Sewage sludge ; Hydrogen ; Methane
- 刊名:Bioprocess and Biosystems Engineering
- 出版年:2014
- 出版时间:December 2014
- 年:2014
- 卷:37
- 期:12
- 页码:2401-2413
- 全文大小:631 KB
- 参考文献:1. Heo JY, Yoo SH (2013) The public’s value of hydrogen fuel cell buses: a contingent valuation study. Int J Hydrogen Energy 38:4232-240 CrossRef
2. Chinellato G, Cavinato C, Bolzonella D, Heaven S, Banks CJ (2013) Biohydrogen production from food waste in batch and semi-continuous conditions: evaluation of a two-phase approach with digestate recirculation for pH control. Int J Hydrogen Energy 38:4351-360 CrossRef 3. Wang B, Li Y, Ren N (2013) Biohydrogen from molasses with ethanol-type fermentation: effects of hydraulic retention time. Int J Hydrogen Energy 38:4361-367 CrossRef 4. Kim M, Liu C, Noh JW, Yang Y, Oh S, Shimizu K, Lee DY, Zhang Z (2013) Hydrogen and methane production from untreated rice straw and raw sewage sludge under thermophilic anaerobic conditions. Int J Hydrogen Energy 38:8648-656 CrossRef 5. Li J, Li B, Zhu G, Ren N, Bo L, He J (2007) Hydrogen production from diluted molasses by anaerobic hydrogen producing bacteria in an anaerobic baffled reactor (ABR). Int J Hydrogen Energy 32:3274-283 CrossRef 6. Ren N, Li J, Li B, Wang Y, Liu S (2006) Biohydrogen production from molasses by anaerobic fermentation with a pilot-scale bioreactor system. Int J Hydrogen Energy 31:2147-157 CrossRef 7. Gue WQ, Ren NQ, Wang XJ, Xiang WS, Meng ZH, Ding J, Qu YY, Zhang LS (2008) Biohydrogen production from ethanol-type fermentation of molasses in an expanded granular sludge bed (EGSB) reactor. Int J Hydrogen Energy 33:4981-988 CrossRef 8. Aragaw T, Andargie M, Gessesse A (2013) Co-digestion of cattle manure with organic kitchen waste to increase biogas production using rumen fluid as inoculums. Int J Phys Sci 8:443-50 9. Dai X, Duan N, Dong B, Dai L (2013) High-solids anaerobic co-digestion of sewage sludge and food waste in comparison with mono digestions: stability and performance. Waste Manag 33:308-16 CrossRef 10. Lee M, Hidaka T, Hagiwara W, Tsuno H (2009) Comparative performance and microbial diversity of hyperthermophilic and thermophilic co-digestion of kitchen garbage and excess sludge. Bioresour Technol 100:578-85 CrossRef 11. Li M, Zhao YC, Guo Q, Qian XQ, Niu DJ (2008) Bio-hydrogen production from food waste and sewage sludge in the presence of aged refuse excavated from refuse landfill. Renew Energy 33:2573-579 CrossRef 12. Lee WS, Chua ASM, Yeoh HK, Ngoh GC (2014) A review of the production and applications of waste-derived volatile fatty acids. Chem Eng J 235:83-9 CrossRef 13. Kim MS, Lee D (2010) Fermentative hydrogen production from tofu-processing waste and anaerobic digester sludge using microbial consortium. Bioresour Technol 101:S48–S52 CrossRef 14. Zhu HG, Parker W, Basnar R, Proracki A, Falletta P, Beland M (2008) Biohydrogen production by anaerobic co-digestion of municipal food waste and sewage sludges. Int J Hydrogen Energy 33:3651-659 CrossRef 15. Kim SH, Han SK, Shin HS (2004) Feasibility of biohydrogen production by anaerobic co-digestion of food waste and sewage sludge. Int J Hydrogen Energy 74:280-87 16. Liu F, Rotaru AE, Shrestha PM, Malvankar NS, Nevin KP, Lovley DR (2012) Promoting direct interspecies electron transfer with activated carbon. Energy Environ Sci 5:8982-989
文摘
We evaluated the feasibility of co-digesting molasses wastewater and sewage sludge in a two-stage hydrogen- and methane-producing system. The highest energy was recovered at the 21-h hydraulic retention time (HRT) of the first hydrogenic reactor and at 56-h HRT of the secondary methanogenic reactor. Hence, the two-stage system recovered 1,822?kJ from 1?L of the mixed wastes (19.7: hydrogenic reactor plus, 1,802?kJ?L?: methanogenic reactor). Despite the overloaded VFA-run with a short HRT of 56?h, the GAC-CH4 reactor increased methane production rate and yields due to enhanced pH buffer capacity. An RNA-based community analysis showed that the Ethanoligenens and Methanosaeta dominated the hydrogen and methane bioreactor, respectively. The two-stage system of co-digesting molasses and sewage sludge is particularly cost-effective due to non-pretreatment of sewage sludge.
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