期刊文献+

CSTR反应器鸡粪厌氧消化中试启动研究 被引量:8

Start-up performance evaluation of pilot-scale anaerobic digestion of chicken manure in CSTR
下载PDF
导出
摘要 在中温(37℃)条件下,利用全混式厌氧(CSTR)反应器进行鸡粪废水厌氧消化启动的实验室模拟,将试验分为4个阶段(Ⅰ,Ⅱ,Ⅲ,Ⅳ),逐级增加进料负荷量,研究分析各阶段影响因素。结果表明:CSTR反应器能够正常启动鸡粪废水厌氧消化,当试验各阶段(Ⅰ∶Ⅱ∶Ⅲ∶Ⅳ)进料比为1∶2∶2.67∶3.33时,相应的最高产气速率之比约为1∶1.76∶2.04∶2.46;在进料COD为25 496 mg/L,HRT为31 d时,氨氮最高浓度为2 122 mg/L左右,COD去除率为(57.5±1.93)%,每日甲烷产量(单位质量VS)为(301±6)mL/g。试验4 d后,CSTR反应器产生的沼气中CH4含量稳定在61.8%~70.1%。 Under mesophilic conditions(37 ℃),a pilot-scale experiment based on anaerobic digestion of chicken manure was conducted in CSTR.The experiments were divided into 4 stages.The results showed that CSTR could be successfully started up for anaerobic digestion of chicken manure.When the feeding ratio of stages(Ⅰ∶Ⅱ∶Ⅲ∶Ⅳ) was 1∶2∶2.67∶3.33,the corresponding ratio of the maximum gas production rate was about 1∶1.76∶2.04∶2.46.Under the conditions of 25 496 mg/L COD and 31 d HRT,about(57.5±1.93)% COD was removed,and the methane production/gram volatile solidsadded(CH4/gVS) reached(301±6) mL/gVS.The concentration of CH4 in biogas was stable at 61.8%~70.1% after 4 days later in the experiments.
出处 《可再生能源》 CAS 北大核心 2012年第4期89-92,96,共5页 Renewable Energy Resources
基金 沈阳市科技计划项目(F10133900)
关键词 CSTR 鸡粪 厌氧消化 启动 中试 CSTR chicken manure anaerobic digestion start-up pilot-scale
  • 相关文献

参考文献16

  • 1冯磊,Bernhard Raninger,李润东,李延吉.有机垃圾单级高固体厌氧消化的中试实验[J].环境科学学报,2009,29(3):584-588. 被引量:7
  • 2李荣平,李秀金,Shulin Chen.用于牛粪液厌氧消化的推流式和完全混合式反应器性能研究[J].农业工程学报,2007,23(9):186-190. 被引量:13
  • 3隋继超,蒋建国,吴时要,赵振振.有机垃圾单级高固体厌氧消化启动实验研究[J].环境科学,2007,28(3):684-688. 被引量:14
  • 4孙振钧.中国生物质产业及发展取向[J].农业工程学报,2004,20(5):1-5. 被引量:170
  • 5Hugo Oscar Méndez-Acosta,Raúl Snell-Castro,Víctor Alcaraz-González,Víctor González-álvarez,Carlos Pelayo-Ortiz.Anaerobic treatment of Tequila vinasses in a CSTR-type digester[J].Biodegradation.2010(3)
  • 6Jens Ejbye Schmidt,Zusana Mladenovska,Marianne Lange,Birgitte Ki?r Ahring.Acetate conversion in anaerobic biogas reactors: Traditional and molecular tools for studying this important group of anaerobic microorganisms[J].Biodegradation.2000(6)
  • 7Birgit Heppner,Gerhard Zellner,Hans Diekmann.Start-up and operation of a propionate-degrading fluidized-bed reactor[J].Applied Microbiology and Biotechnology.1992(6)
  • 8KIM M,SPEECE R E.Aerobic waste activated sludge (WAS)for start-up seed of mesophilic and thermophilicanaerobic digestion[].Water Research.2002
  • 9ZARKADAS I S,PILIDIS G A.Anaerobic Co-Digestionof table olive debittering&washing Effluent,cattlemanure and pig manure in batch and high volumelaboratory anaerobic digesters:Effect of temperature[].Bioresource Technology.2011
  • 10CHELLIAPAN S,WILBY T,SALLIS P J.Effect of hy-draulic retention time on up-flow anaerobic stage reac-tor performance at constant loading in the presence ofantibiotic tylosin[].Brazilian Journal of ChemicalEngineering.2011

二级参考文献66

  • 1赵杰红,张波,蔡伟民.厌氧消化系统中丙酸积累及控制研究进展[J].中国给水排水,2005,21(3):25-27. 被引量:37
  • 2赵庆良,王宝贞,G.库格尔.厌氧消化中的重要中间产物──有机酸[J].哈尔滨建筑大学学报,1996,29(5):32-38. 被引量:9
  • 3隋继超,蒋建国,吴时要,赵振振.有机垃圾单级高固体厌氧消化启动实验研究[J].环境科学,2007,28(3):684-688. 被引量:14
  • 4朱清时.生物质洁净能源[M].北京:化学工业出版社,2001..
  • 5Gross R, Leach M, Bauen A. Progress in renewable energy[J]. Environment International, 2003,29 (1): 105-122.
  • 6Yokoyama S Y, Ogi T, Nalampoon A, et al. Biomass energy potential in Thailand[J]. Biomass and Bioenergy,2000,18(5) :405-410.
  • 7Cook J, Beyea J. Bioenergy in the United States:progress and possibilities [J]. Biomass and Bioenergy,2000,18(6) : 441.
  • 8Steininger K W, Voraberger H. Exploiting the medium term biomass energy potentials in Austria [J].Environmental and Resource-Economics, 2003,24 (4): 359-377.
  • 9Dai Lin. The development and prospective of bioenergy technology in China[J]. Biomass and Bioenergy, 1998,15(2):181-186.
  • 10Demirbas A, Energy balance, energy sources, energy policy, future developments and energy investments in Turkey[J]. Energy Conversion and Management. 2001,42 (10): 1239- 1258.

共引文献198

同被引文献120

引证文献8

二级引证文献24

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