Multi-chamber fixed-bed biomembrane reactor and method for treating perchlorate in sewage using same
A biofilm reactor and perchlorate technology, which is applied in biological treatment devices, biological water/sewage treatment, chemical instruments and methods, etc., can solve the problems of large differences in the proportion of dominant bacteria, high sulfate and hydrogen sulfide yields, etc. , to achieve low one-time investment cost, reduce follow-up maintenance costs, and reduce side effects
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Embodiment 1
[0036] ① First, mix the sulfur particles and quartz stone in a volume ratio of 1:1~3:1 to make filler, then inoculate the filler with settled thiosulfate-acclimated sludge, mix evenly, and then inoculate the sludge The filler of mud is respectively added to single-chamber, 2-chamber and 3-chamber reactors with a total volume of 3.6L, wherein the volume of each reaction chamber of the 3-chamber reactor is 1.2L, and the volume of each reaction chamber of the 2-chamber reactor is The volume is 1.8L, and the inoculum amount of sludge per liter of filler is 8g, calculated as SS.
[0037] The sludge was taken from the activated sludge of Shijiazhuang Qiaoxi Sewage Treatment Plant. The sludge was placed in a conical flask and cultivated with sodium thiosulfate. After seven days of anaerobic cultivation, the removal efficiency of perchlorate reached 100%. %.
[0038] The sulfur particles mainly provide electrons for the biofilm and are used for the attachment of the biofilm. The quar...
Embodiment 2~5
[0045] In embodiment 2, single-chamber reactor, 2-chamber reactor and 3-chamber reactor are on the basis of embodiment 1, adopt the parameter in table 1 to run respectively 5 days; Embodiment 3 is on the basis of embodiment 2 , adopting the parameters in Table 1 to run respectively for 5 days; Embodiment 4, on the basis of Example 3, adopting the parameters in Table 1 to run respectively for 5 days; Embodiment 5, on the basis of Example 4, using the parameters of Table 1 Run for 15 days respectively.
[0046] The degradation rate of perchlorate in each reactor, the utilization rate of sulfur particles, and the distribution of bacteria in the reactor were respectively analyzed through the water quality monitoring port and the sludge sampling port, and the production rate of hydrogen sulfide was detected through the gas outlet 6. For the above results, see Figure 3~7 .
[0047] from image 3 It can be seen that when ClO enters 4 - When the load is low, such as the 0.2~0.5g / ...
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