杨宏, 陈伟, 谭科艳, 田玉斌, 鄢琳. 利用小空间厌氧移动床还原硫酸盐的试验研究[J]. 北京工业大学学报, 2016, 42(7): 1102-1107. DOI: 10.11936/bjutxb2015090072
    引用本文: 杨宏, 陈伟, 谭科艳, 田玉斌, 鄢琳. 利用小空间厌氧移动床还原硫酸盐的试验研究[J]. 北京工业大学学报, 2016, 42(7): 1102-1107. DOI: 10.11936/bjutxb2015090072
    YANG Hong, CHEN Wei, TAN Keyan, TIAN Yubin, YAN Lin. Reduction of Sulfate by Using Small Space Anaerobic Moving Bed Reactor[J]. Journal of Beijing University of Technology, 2016, 42(7): 1102-1107. DOI: 10.11936/bjutxb2015090072
    Citation: YANG Hong, CHEN Wei, TAN Keyan, TIAN Yubin, YAN Lin. Reduction of Sulfate by Using Small Space Anaerobic Moving Bed Reactor[J]. Journal of Beijing University of Technology, 2016, 42(7): 1102-1107. DOI: 10.11936/bjutxb2015090072

    利用小空间厌氧移动床还原硫酸盐的试验研究

    Reduction of Sulfate by Using Small Space Anaerobic Moving Bed Reactor

    • 摘要: 为了强化硫酸盐还原反应器的还原效能,利用小空间厌氧移动床生物膜反应器,研究了反应温度、进水pH、水力停留时间(hydraulic retention time,HRT)、 ρ(COD)/ ρ(S O 4 2 - )和回流比对S O 4 2 - 还原效果的影响,从而考察反应器还原S O 4 2 - 的效能及在高负荷条件下稳定运行状况. 研究结果表明:温度35℃、进水pH=7.0、 ρ(COD)/ ρ(S O 4 2 - )=2.5、HRT=8h和回流比=4∶1为反应器运行的最佳工况条件;进水S O 4 2 - 质量浓度在1500~2500mg/L时,S O 4 2 - 的还原率保持在78.77%~88.89%,S O 4 2 - 的还原速率最高达5.90kg/(m 3·d),表明反应器具有较强的S O 4 2 - 还原能力;在进水S O 4 2 - 质量浓度为2250mg/L左右时,连续运行20d,S O 4 2 - 还原率达87.13%并能稳定运行.

       

      Abstract: To enhance the sulfate reduction efficiency, the effects of temperature, influent pH, HRT, ρ(COD)/ ρ(S O 4 2 - ) and reflux ratio on the sulfate reduction were discussed by using small space anaerobic moving bed biofilm reactor. Then the reducing S O 4 2 - efficiency and stable operation were also studied under high load conditions. Results indicate that the optimal conditions for reactor operation is at temperature 35℃, influent pH=7.0, ρ(COD)/ ρ(S O 4 2 - )= 2.5, HRT=8h and reflux ratio=4∶1. When the sulfate reduction rate remains in the range of 78.77%-88.89% and sulfate concentrations ranges from 1500 to 2500mg/L; sulfate removal rate is up to 5.90kg/m 3·d and there is a high S O 4 2 - reduction capacity in reactor. When the condition of the influentsulfate concentrations is 2250mg/L and continuous reactor operation for 20d, the sulfate removal efficiency reaches more than 87.13% and the reactor keeps stable operation.

       

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