期刊文献+

Hydrogen energy recovery from high strength organic wastewater with ethanol type fermentation using acidogenic EGSB reactor 被引量:5

Hydrogen energy recovery from high strength organic wastewater with ethanol type fermentation using acidogenic EGSB reactor
下载PDF
导出
摘要 A lab-scale expanded granular sludge bed (EGSB) reactor was employed to evaluate the feasibility of the hydrogen energy recovery potential from high strength organic wastewater. The results showed that a maximum hydrogen production rate of 7.43 m^3 H2/m^3 reactor · d and an average hydrogen production rate of 6.44- ms H^2/ms reactor · d were achieved with the hydrogen content of 50% -56% in the biogas during the 90-day operation. At the acidogenic phase, COD removal rate was stable at about 15%. In the steady operation period, the main liquid end products were ethanol and acetic acid, which represented ethanol type fermentation. Among the liquid end products, the concentration percentage of ethanol and acetic acid amounted to 69.5% - 89. 8% and the concentration percentage of ethanol took prominent about 51.7% - 59. 1%, which is better than the utilization of substrate for the methanogenic bacteria. An ethanol type fermentation pathway was suggested in the operation of enlarged industrial continuous hydrogen bio-producing reactors. A lab-scale expanded granular sludge bed (EGSB) reactor was employed to evaluate the feasibility of the hydrogen energy recovery potential from high strength organic wastewater. The results showed that a maximum hydrogen production rate of 7.43 m3 H2/m3 reactor·d and an average hydrogen production rate of 6.44 m3 H2/m3 reactor·d were achieved with the hydrogen content of 50%~56% in the biogas during the 90-day operation. At the acidogenic phase, COD removal rate was stable at about 15%. In the steady operation period, the main liquid end products were ethanol and acetic acid, which represented ethanol type fermentation. Among the liquid end products, the concentration percentage of ethanol and acetic acid amounted to 69.5%~89.8% and the concentration percentage of ethanol took prominent about 51.7%~59.1%, which is better than the utilization of substrate for the methanogenic bacteria. An ethanol type fermentation pathway was suggested in the operation of enlarged industrial continuous hydrogen bio-producing reactors.
出处 《Journal of Harbin Institute of Technology(New Series)》 EI CAS 2005年第6期603-607,共5页 哈尔滨工业大学学报(英文版)
基金 Sponsoredbythe973FundamentalScienceProgramofChina(GrantNo.G2000026402),NationalNaturalScienceFundofChina(GrantNo.30470054)andNationalScienceFundforDistinguishedYoungScholars(GrantNo.50125823).
关键词 hydrogen production ethanol-acetate fermentation EGSB reactor acidogenic energy recovery 氢气生产 乙醇-乙酸盐发酵 粒状污泥床反应器 有机废水 氢能回收
  • 相关文献

参考文献2

二级参考文献17

  • 1speeceR E 著 李亚新译.工业废水的厌氧生物技术[M].北京:中国建筑工业出版社,2001.1-2.
  • 2贺延龄编著.废水的厌氧生物处理[M].北京:中国轻工业出版社,1999.125-126.
  • 3Chui-Yue Lin, Kazuaki Sato, Tatsuya Noike,Junichiro Matsumoto. Methanogenic digestion using mixed substrate of Acetic, Propionic and Butyric Acids. Water Reseach, 1986,20 : 385--394.
  • 4McCarty P L, Jeris J S,Mrudoch W. Individual volatile acids in anaerobic treatment. J. War. Pollut. Control Fed.,1963,35 : 1501-- 1516.
  • 5Gujer W, Zehnder A J B. Conversion processes in anaerobic digestion. Wat. Res., 1983,15: 127--167.
  • 6Demirer G N, R E Speece. Anaerobic bio-transformation of four 3-carbon compounds (acrolein, acrylic acid, allyl alcohol and N-propanol)in UASB reactor. Water Reseach, 1998,32:747-- 759.
  • 7ZAFAR IQBAL BHATTI, KENJI FURUKAWA,MASANORI FUJITA. Feasibility of methanolic waste treatment in UASB reactors. Water Reseach, 1996, 30 : 2559-2568.
  • 8Michael A Bull, Robert M Sterritt, John N Lester. The distribution of bacterial activity in an anaerobic fluidized bed reactor. Water Reseach, 1984, 18(8) :1017-- 1020.
  • 9May M Wu,Robert F Hickey. n-Propanol production during ethanol degradation using anaerobic granules. 1996,30(7) :1686--1694.
  • 10Nanqi Ren, Baozhen Wang. Ethanol-Type Fermentation form Carbohydrate in High Rate Acidogenic Reactor. Biotechnology and Bioengineering, 1997,54(5) :428--433.

共引文献92

同被引文献32

引证文献5

二级引证文献16

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部