为了降低陶瓷膜-生物反应器的能耗、同时提高膜的渗透通量，本文将气升式外循环引入膜-生物反应器的设计。
To raise permeate flux of ceramic membrane, reduce industrial specific power consumption, airlift circulation was led into membrane bioreactor under the suction filtration.
初步建立了颗粒体系微滤过程中的膜微观结构与性能关系模型，对陶瓷膜孔径对膜通量的影响进行模拟计算。
An ultra- filtration process was used to treat the eucalyptus CTMP effluent and the optimal pore diameter of membrane was found out.
初步建立了颗粒体系微滤过程中的膜微观结构与性能关系模型，对陶瓷膜孔径对膜通量的影响进行模拟计算。
An ultra- filtration process was used to treat the eucalyptus CTMP effluent and the optimal pore diameter of membrane was found out.
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