期刊文献+

生物滴滤法去除硫化氢与苯乙酸混合废气 被引量:5

Biotreatment of Mix Gas Including Hydrogen Sulfide and Phenylacetic Acid by Using Bio-trickling Filter
下载PDF
导出
摘要 采用填充ZX03型填料的生物滴滤塔处理H2S与C6H5CH2COOH的混合制药废气。主要考察了不同进气浓度比例下H2S与C6H5CH2COOH的去除效率,不同流量下的压力损失及气体停留时间对去除率的影响。结果表明:随着H2S与C6H5CH2COOH进气浓度比例的提高,H2S的去除率均保持在95%以上,C6H5CH2COOH的去除率逐渐下降。当H2S与C6H5CH2COOH的进气质量浓度分别为ρ(H2S)<400 mg/m3与ρ(C6H5CH2COOH)<800 mg/m3,其最佳气体停留时间为30 s。该生物滴滤塔压力损失小,无堵塞现象,可长期稳定运行。 The bio-trickling filter packed with ZX03 carrier is used to treat mix pharmaceutical gases containing HES and C6H5CH2COOH. The removal efficiency of HES and C6H5CH2COOH at various inlet concentration ratios, the pressure drop of the bioreactor at different gas flow rates and the effect of the gas retention time on removal efficiency are investigated in the experiment. The results show that the removal efficiency of H2S remains above 95% regardless of the ratio of H2S/C6H5 CH2COOH and the removal efficiency of C6H5 CH2 COOH decreases gradually with the elevation of inlet concentration ratio of H2S/C6H5CH2COOH. When the inlet concentration of H2S and C6H5CH2COOH is respectively less than 400 mg/m^3 and 800 mg/m^3, the optimal gas retention time is 30 s. The bio-trickling filter is not jammed and the resistance is maintained at low value during the operation. It doesn' t need to carry out back washing frequently and can be operated steadily for long time.
出处 《南京理工大学学报》 EI CAS CSCD 北大核心 2006年第3期371-374,共4页 Journal of Nanjing University of Science and Technology
基金 黑龙江省海外国际合作项目(WC03305) 哈尔滨市科学技术计划项目(2002AA4CS087)
关键词 生物滴滤塔 苯乙酸 硫化氢 填料 bio-trickling filter phenylacetic acid hydrogen sulfide carriers
  • 相关文献

参考文献11

  • 1Bouzaza A,Laplanche A,Marsteau S.Adsorption-oxi-dation of hydrogen sulfide on activated carbon fibers:Effect of the composition and the relative humidity of the gas phase[J].Chemosphere,2004,54:481-488. 被引量:1
  • 2Vissanu M,David L T.Adsorption-reaction processes for the removal of hydrogen sulphide from gas streams[J].J Chem Tech Biotechnol,1997,68:411-416. 被引量:1
  • 3Prepiorski J,Yoshida S,Oya A.Structure of K2CO3-loaded activated carbon filter and its deodorization ability against H2S gas[J].Carbon,1999,37:1 881-1 890. 被引量:1
  • 4Marie C D,Louise B,Nathalie B,et al.Biofiltration of air contaminated with toluene on acompost-based bed[J].Advances in Environmental Research,2002,6:239-254. 被引量:1
  • 5Madjid M,Allen D G.Biofiltration of mixtures of hydrophilic and hydrophobic volatile organic compounds[J].Chemical Engineering Science,2000,55:1 545-1 558. 被引量:1
  • 6Huub H J,Deshusses M A.Co-treatment of H2S and toluene in a biotrickling filter[J].Chemical Engineering Journal,2002,87:101-110. 被引量:1
  • 7Chung Y C,Huang C,Tseng C P,et al.Biotreatment of H2S and NH3 containing waste gases by co-immobilized cells biofilter[J].Chemosphere,2000,41:329-336. 被引量:1
  • 8Kim J O.Degradation of benzene and ethylene in biofilters[J].Process Biochemistry,2003,39:447-453. 被引量:1
  • 9邵立明,何品晶,傅钟,李国建.固定化微生物处理含H_2S气体的试验研究[J].环境科学,1999,20(1):19-22. 被引量:58
  • 10郭静,黄焱歆,王召,李敏.生物滤池与固定——悬浮填料复合式生物膜反应器脱臭[J].中国环境科学,1999,19(1):59-62. 被引量:20

二级参考文献17

共引文献87

同被引文献55

引证文献5

二级引证文献29

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