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含硫化物废水在升流式填料塔中的处理及数学模拟 被引量:4

Treatment and Mathematical Simulation of Wastewater Containing Sulfide in Aerobic Up-Flow Packed Tower
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摘要 在升流式填料塔中,通过接种排硫硫杆菌形成稳定生物膜.在pH值和温度分别控制在 7. 0±0. 1和 30±2℃条件下,进水质量浓度分别为 85. 76, 177. 83, 269. 55和 394. 26mg/L时,改变硫化物容积负荷 (VLR)和溶解氧水平进行正交试验.研究和分析硫化物容积负荷与溶解氧共同作用下硫化物的去除规律、硫酸盐的生成规律以及单质硫的生成率,并对建立的模拟方程进行了验证.结果表明,在升流式生物填料塔内废水中的硫化物去除率能达到9500以上;应用模拟方程,对于不同的进水浓度,都能找到一个最佳的运行工况.在硫化物去除率和单质硫的生成率达到最佳时,保持反应器的最大容积负荷和最小的溶解氧. The stable bio-membrane came into being after inoculating a strain of Thiobacillus thioparus sp in aerobic up-flow packed tower. When the sulfide influent concentrations were 85.76, 177.83, 269.55 and (394.26 mg/L) respectively when pH was 7.0±0.1 and tempreture was 30±2 ℃, the tests for each given concentration were finished while changing the volumetric loading rate (VLR) of sulfide and dissolved oxygen. Through the analysis of the sulfide removal rate, sulfate production rate and sulfur forming efficiency, the simulation equations were established and validated by practical tests. The results show that the sulfide removal rate reaches over 95~0_0 in the aerobic up-flow packed tower.For different influent concentrations,an optimal operation condition can be found while the established regression equations are applied. The possible maximal VLR and possible lowest dissolved oxygen can be maintained when the sulfide removal rate and sulfate production rate get the best results. These will provide the theory basis for optimizing wastewater treatment process and lowering its energy consumption.
出处 《天津大学学报(自然科学与工程技术版)》 EI CAS CSCD 北大核心 2005年第2期174-180,共7页 Journal of Tianjin University:Science and Technology
基金 天津市自然科学基金重点资助项目(023804211)
关键词 排硫硫杆菌 升流式填料塔 硫化物 废水 单质硫 回归方程 Thiobacillus thioparus sp aerobic up-flow packed tower sulfide wastewater sulfur regression equation
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参考文献13

  • 1俞汉青,顾国维.生物膜反应器挂膜方法的试验研究[J].中国给水排水,1992,8(3):13-17. 被引量:101
  • 2布坎南RE 吉本斯NE 中国科学院微生物研究所《伯杰细菌鉴定手册》.伯杰细菌鉴定手册[M]:第8版[M].北京:科学出版社,1984.631-638.
  • 3Janssen J S,Albert J H, Hulshoff Pol Look W,et al. Development of a novel process for the biological conversion of H2S and methanethiol to elemental sulfur [ J ]. Biotechnol Bioeng ,2003,82 ( 1 ) : 1-11.
  • 4Silva A J, Varesche M B, Foresti E, et al. Sulphate removal from industrial wastewater using a packed-bed anaerobic reactor [ J ]. Process Biochemistry, 2002,37 (9) :927-935.
  • 5Rinzema A, Lettiga G. Anaerobic treatment of sulphate conmining waste water [ A ]. In : Biotreatment Systems [ C ]. Boca Raton, FL : CRC Press, 1998.65-69.
  • 6Wiemann M, Schenk H, Hegemann W. Anaerobic treatment of tannery wastewater with simultaneous sulphide elimination[J]. War Res,1997 ,32 ( 3 ) :774-780.
  • 7Buisman C J N,Geraats B G, Ijspeert P, et al. Optimization of sulphur production in a biotechnological sulphide-removing reactor[ J]. Biotechnol Bioeng, 1990,35 (1) :50-56.
  • 8Yan Liu, Herbert H, Fang P. Precipitates in anaerobic granules treating sulphate-bearing wastewater [ J ]. Wat Res,1998,32(9) :2 627-2 632.
  • 9Koenig A, Liu L H. Kinetic model of autotrophic denitritlcation in sulphur packed-bed ractors [ J ]. Wat Res, 2001,35(8) : 1 969-1 978.
  • 10Buisman C J N, Wit B, Lettinga G. Biotechnological sulphide removal in three polyurethane carrier reactors: Stirred reactor, biorotor reactor and upflow reactor [ J ]. Wat Res,1990,24(2) :245-251.

二级参考文献1

  • 1余淦申.生物接触氧化法处理废水[M]浙江科学技术出版社,1983.

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