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內循環三相流化床的生物膜的培養

Cultivation of biofilms in an inner loop three-phase fluidized bed

  • 摘要: 研究了內循環三相流化床在兩種不同進水方式情況下生物膜培養情況.研究表明:間歇進水時生成的生物膜能達到200~250μm左右,連續進水時生物膜厚度能達到100μm;前者較為圓滑緊密,而后者的活性較高;較低的啟動容積負荷有利于啟動掛膜;掛膜完成后進水的容積負荷不能過低,否則容易因污泥負荷低而引起絲狀菌膨脹.通過間歇式進水培養的活性污泥達到了生物量9.65g·L-1(其中附著生物膜占92.7%),而連續式進水負荷COD可以達到11.45kg·m-3·d-1,此時COD去除率達到80%.

     

    Abstract: This paper studied the situation of cultivating the biofilms with two different flow modes in an inner loop three-phase fluidized bed. The results showed that the diameter of the biofilm formed in a se quencing batch reactor (SBR) could increase to about 200~250μm, and that formed in a continuance reactor could arrive at 100μm. The former biofilm is smooth and compact, but the later has a higher activity. A lower initial loading rate makes for suspension membrane, and in the successive process, the loading rate can not be excessively low. Otherwise filamentous colonies expand because of the low loading rate. The biomass density of active sludge with SBR mode could increase to 9.65 g·L-1, 92.7 % of which is attachment biofilm, and the loading rate of COD with continuance mode could arrive at 11.45 kg·m-3·d-1.

     

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