期刊文献+

序批式气提生物反应器(SABR)处理氯苯胺类有机废水好氧污泥颗粒化研究 被引量:18

Granulation of aerobic sludges in sequencing airlift bioreactor(SABR) for the treatment of chloroanilines-containing organic wastewater
下载PDF
导出
摘要 研究了序批式气提生物反应器(SABR)处理氯苯胺类(CAs)有机废水过程中好氧污泥的颗粒化.SABR运行15d后,反应器内出现细小污泥颗粒,通过缩短循环时间与污泥沉降时间,并逐步提高COD与CAs进水负荷,SABR运行48 d后污泥颗粒化明显;反应器在循环时间为12 h、污泥沉降时间为6 min、表面气速为2 4 cm·s-1、COD负荷为1.0~3.6 kg·m-3·d-1、CAs负荷逐步提升至800 g·m-3·d-1的条件下继续运行50d,SABR污泥颗粒化趋于成熟,COD、CAs去除率稳定在90%、99.9%以上.根据污泥形态、最小沉降速率、SVI和目标污染物降解性能的变化,好氧污泥颗粒化过程可分为启动期、颗粒污泥形成期、生长期和成熟期.成熟好氧颗粒污泥粒径为0.9~2.5 mm,平均颗粒密度为64 g·L-1(以MLVSS计),污泥最小沉降速率为68.4 m·h-1,SOUR为167 mg·g-1·h-1;颗粒污泥外形为圆形或椭圆形,呈橙黄色,结构较致密,颗粒内外分布有丰富的类球菌、类短杆菌,与胞外多聚物交织共存. The granulation of aerobic sludges in Sequencing Airlift Bioreactor (SABR) for the treatment of chloranilines( CAs)-containing organic wastewater was investigated. Aerobic granules were observed after start-up for 15 days. The granulation of aerobic sludges was apparently developed after 48 days of operation along with gradual increases COD and CAs loadings, as well as the decreases of cycle time and settling time. Since then and within the subsequent 50 days, the granulation of aerobic sludge tended to mature while the removal efficiencies of COD and CAs were maintained around 90% and 99.9%, respectively. When SABR was continuously operated in 12h cycle time with settling time of 6 min, superficial air velocity of 2.4 cm·s^-1 , COD loadings of 1.0 - 3.6 kg·m^- 3·d^- 1 and CAs loadings increased from 560 to 800 g·m^- 3· d^- 1 . The process of sludge granulation could be divided into four different stages such as startup, granules formation, growth and maturation, based on the changes of sludge morphology, minimal settling velocity, SVI and CAs-degrading performance. Mature granules in this study featured with diameter of 0.9 - 2.5 mm, average biomass density of 64 gMLVSS·l^-1 , minimal settling velocity of 68.4 m· h^-1 and SOUR of 167 mgDO· gMLVSS^-1 · h^-1 . The aerobic granules were found in shape of rotundity and/or ellipse with colour of orange and comparably dense structure, which consisted of a wide variety of heterotrophic bacteria (including rods-like and cocci-like), interlacing with extraeelluar polymers. Results demonstrated that aerobic sludge granulation was feasible in SABR for treatment of CAs-containing organic wastewater, and could be exploited to increase stability and efficiency of bioreactors.
出处 《环境科学学报》 CAS CSCD 北大核心 2005年第11期1448-1456,共9页 Acta Scientiae Circumstantiae
基金 国家自然科学基金资助项目(No.50378082) 浙江省重点科研项目(No.2004C2302)~~
关键词 序批式气提生物反应器 氯苯胺 有机废水 好氧污泥颗粒化 sequential airlift bioreactor(SABR) chloroanilines organic wastewater aerobic sludge granulation
  • 相关文献

参考文献31

  • 1American Public Health Association. 1998. Standard methods for the examination of water and wastewater[M]. Washington D C.
  • 2Belen A, Anuska M C, Juan M G, et al. 2004. Aerobic granulation with industrial wastewater in sequencing batch reactors[ J]. Water Research,(38): 3389-3399.
  • 3Bell L S, Devlin J F, Gillham R W, et al. 2003. A sequential zero valent iron and aerobic biodegradation treatment system for nitrobenzene [ J].Journal of Contaminant Hydrology,66:201-217.
  • 4Beun J J, Hendeiks A. 1999. Aerobic Granulation in a Sequencing batch reactor[J]. Water Research, 33(10): 2283-2290.
  • 5Beun J J, van Loosdrecht M C M, Heijnen J J. 2000. Aerobic granulation [J]. Water Sci Technol, 41:41-48.
  • 6Beun J J, Loosdrecht M C M, Heijnen J J. 2002. Aerobic granulation in a Sequencing batch airlift reactor[J]. Wat Res, 36:702-712.
  • 7Boon N, De Gelder L D, Lievens H, et al. 2002. Bioaugmenting Bioreactors for the Continuous Removal of 3-Chloroaniline by a Slow Release [ J].Environ Sci Technol,36:4698-4704.
  • 8Boon N, Top E M, Verstraete W, et al.2003. Bioaugmenting as a tool to protect the structure and function of an activated-sludge microbial community against a 3-chloroaniline shock load [ J ]. Appl Environ Microbiol, 69:1511-1520.
  • 9Hu L L, Wang J, Wen X H, et al. 2005 .The formation and characteristics of aerobic granules in sequencing batch reactor (SBR) by seeding anaerobic granules[J]. Process Biochemistry, 40:5-11.
  • 10Hulshoff Pol L W, Lettinga G. 1983. Granulation in UASB reactor[J]. Wat Sci Technol, 15(2): 293-304.

二级参考文献51

  • 1任华峰,李淑芹,刘双江,刘志培.一株对氯苯胺降解菌的分离鉴定及其降解特性[J].环境科学,2005,26(1):154-158. 被引量:24
  • 2朱亮,徐向阳,郑昱.序批式气提生物反应器(SABR)处理氯苯胺类有机废水好氧污泥颗粒化研究[J].环境科学学报,2005,25(11):1448-1456. 被引量:18
  • 3Boon N, Top E M, Goris J, et al. Genetic Diversity among 3-chloroaniline and aniline-degrading strains of the Comamonadaceae [J]. Applied and Environmental Microbiology, 2001, 5 :1107--1115.
  • 4Chang C-W, Bumpus J A. Oligomers of 4-chloroaniline are intermediates formed during its biodegradation by Phanerochaete chrysosporium [J]. FEMS Microbiology Letters, 1993, 107:337-- 342.
  • 5Mars A E, Janssen D B, Kasberg T, et al. Microbial degradation of chloroaromatics: use of the meta-cleavage pathway for mineralization of chlorobenzene [ J ]. Journal of Bacteriology,1997, 179(14): 4530--4537.
  • 6Zeyer J, Kearney P C. Microbial degradation of para-chloroaniline as sole carbon and nitrogen source [ J ]. Pesticide Biochemistry and Physiology, 1982, 17: 215--213.
  • 7Michael L, Christel H, et al. Degradation of aniline and monochlorinated anilines by soil-born Pseudomonas acidovorans strains[J]. Archives of Microbiology, 1990, 155 : 56-- 61.
  • 8Surovtseva E G, Ivoilov V S, Karasevlch Yu N, et al. Chlorinated anilines, a source of carbon, nitrogen and energy for Pseudomonas [ J ]. Mikrobiologiya, 1985, 6 (54) : 948-- 952.
  • 9Boon N, Top E M, Goris J, et al. Bioaugmentation of activated sludge by an indigenous 3-chloroaniline-degrading Comamonastes tosteroni strain, 12gfp [J]. Applied and Environmental Microbiology, 2000, 7: 2906--2913.
  • 10Karninski U, Janke D, Prauser H, et al. Degradation of aniline and monochloroanilines by Rhodococcus sp. An117 and a pseudomonad: a comparative study [ J ]. Zeitschrift fur Allgemeine Mikrobiologie, 1983, 23 : 235 -- 246.

共引文献38

同被引文献288

引证文献18

二级引证文献91

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