进水模式对SBBR性能及氮形态转化的影响

通过对4种不同进水模式下序批式生物膜反应器(SBBR)的性能、微生物群落结构以及氮形态转化的差异分析, 比较不同进水模式对SBBR性能和氮形态转化的影响及其产生的机制. 结果表明, 分散式进水模式表现出比一次性进水更好的脱氮效率和更高的抗冲击负荷能力, 在达到相同的处理效率的前提下, 分散式进水模式M₄的COD和氨氮负荷最高可达2 540和540 mg·(L·d)^-1, 而一次性进水模式M₁仅能分别达到2 000和420 mg·(L·d)^-1；分散进水模式能降低一次性进水所带来的冲击性负荷, 将负荷均化分散到周期内的各个时段, 同时也减少了进水对微生物的稀释作用, 使得单位体积内有效微生物的数量相对充足, 从而提高反应器的负荷能力. 在分散进水模式下， 从M₄与M₂、M₃的对比来看, 分散模式的进水规律越接近运行模式的循环规律, 反应器的氮素转化效率就越高, 残留的氮素总量也就越低.

Effect on the Performance of SBBR and the Form Transformation of Nitrogen by Different Influent Pattern

The difference of sequencing batch biofilm reactor (SBBR) performance and nitrogen transformation mechanism which caused by four different influent patterns were researched. Through variance analysis of SBBR performance, microbial community structure and nitrogen transformation, the results indicated that, on the one hand the dispersed influent pattern displayed higher anti-load ability than the centralized one, under the same efficiency, COD and ammonia load of the dispersed M₄reached 2 540 mg·(L·d)^-1 and 540 mg·(L·d)^-1 respectively compared with 2 000 mg·(L·d)^-1 and 420 mg·(L·d)^-1 by the centralized M₁; on the other hand, considering the dispersed influent pattern, the closer influent mood was to the cycle mood of operation, the higher the nitrogen transformation efficiency was, which finally led residual nitrogen concentration declined.