1) critical water flow rate
临界雾通量
2) critical flux
临界通量
1.
Study on effect of membrane fiber length on critical flux in a novel membrane bioreactor;
新型膜-生物反应器中膜丝长度对临界通量的影响
2.
Study of critical flux in flat-sheet membrane bioreactors;
平板膜生物反应器临界通量测定方法研究
3.
Factors affecting critical flux in submerged flat membrane bioreactor;
影响一体式平板膜生物反应器临界通量的因素
3) sub-critical flux
次临界通量
1.
Critical flux region was measured by using"flux step-wise" method,and the the operating characteristics at sub-critical flux were investigated.
针对膜生物反应器运行中膜污染问题,利用"逐级通量法"测定了膜组件的临界通量,并考察了次临界通量下膜污染的运行特性。
2.
Critical flux region for two membrane modules was measured by using "flux step-wise" method,and then the operating characteristics at sub-critical flux were investigated.
利用"通量阶式递增法"测定了两种膜组件的临界通量,在此基础上考察了次临界通量下的运行特性。
4) critical flux zone
临界通量区
1.
If the imposed flux was below critical flux zone, the TMP increasing curve can be divided into two phases.
当膜通量小于临界通量区时,膜污染发展具有“2阶段”趋势,并且膜通量越小“第1阶段”和“第2阶段”的膜污染发展速率对比越显著。
5) critical airflow
临界通风量
6) critical membrane flux
临界膜通量
1.
Under crossflow velocity of 1 9m/s, critical membrane flux was enhanced from 72L/(m 2·h) to 76 L/(m 2·h) or 81 L/(m 2·h) respectively when powdered activated carbon (PAC) or both PAC and alum were added to the system.
膜侧污水流速在 0 9～ 1 9m/s范围内 ,临界膜通量随膜侧污水流速的增大而增大 。
2.
Comparative studies were also conducted with the two different MBR modules in terms of the optimal ratio of gas to permeated effluent,critical membrane flux,the quality of the permeate,membrane fouling and membrane cleaning.
选取两种不同结构类型的膜组件进行化工废水处理的中试应用研究,对比研究了MBR膜系统的最佳气水比、临界膜通量、膜系统的分离与处理效果以及膜的污染和清洗方式。
补充资料：传质通量
分子式：
CAS号：
性质：又称传质通量。单位时间、单位面积所传过去的物质质量，用符号N表示，其单位为kg/(m2·s)。
CAS号：
性质：又称传质通量。单位时间、单位面积所传过去的物质质量，用符号N表示，其单位为kg/(m2·s)。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条