1) resistance of filtering materials
滤料阻力
2) filtration resistance
过滤阻力
1.
Study on the filtration resistance of inorganic microfiltration membrane;
无机微滤膜过滤阻力的研究
2.
Performance of hybrid membrane bioreactor(HMBR) with suspended carriers during long-term operation was studied under the lab conditions in such aspects as COD removal efficiency,transmembrane pressure(TMP),sludge particle size distribution and filtration resistances of sludge suspension.
在实验室条件下,从有机物去除效果、透膜压差、污泥颗粒粒径和污泥混合液过滤阻力等方面对颗粒填料复合式膜生物反应器(HMBR)的长期运行特性进行了研究。
3.
Average filtration resistance increase rate(K) over the operation time was introduced to evaluate membrane fouling.
在实验过程中用平均膜过滤阻力的上升速率(K)来表征膜污染速率。
3) filter cake resistance
滤饼阻力
4) resistance of filter cloth
滤布阻力
5) filtering resistance
过滤阻力
1.
Describes the straight cylinder type strainer and considers it as better than Y type strainer in maximizing the filtration area, ensuring the water flow direction, minimizing the filtering resistance and considerations for the cost and maintenance.
介绍了直筒式水过滤器,指出其在增大水过滤器过流面积、过滤水流不拐向、降低过滤阻力以及造价、清洗等方面均优于Y形水过滤器。
6) membrane filtration resistance
膜过滤阻力
1.
The modified MBR and non-modified MBR were applied to treat the wastewater,and the effluent quality,membrane flux and membrane filtration resistance were compared.
采用喷涂纳米TiO2的方法对聚偏氟乙烯(PVDF)微滤膜进行改性,用改性膜生物反应器(MBR)和非改性MBR处理污水,对比了两者的出水水质、膜通量和膜过滤阻力。
2.
The effect of powdered activated carbon(PAC) on the mixed liquor characteristics and membrane filtration resistance was studied by using two membrane bioreactors(Reactor 1 no PAC and Reactor 2 added PAC 500 mg/L)under the same influent and operating conditions.
采用两组膜生物反应器(反应器1未投加粉末活性炭,反应器2投加粉末活性炭量为500 mg/L)研究了在相同的进水和运行条件下其混合液特性和膜过滤阻力的变化。
补充资料：多层滤料滤池
分子式：
CAS号：
性质：一种下流式重力深床滤池。一般采用3种滤料，上层为无烟煤(粒径1～2mm)，中层为砂(粒径0.4～0.8mm)，底层为石榴石(粒径<0.5mm)。过滤速度为10m/h，反冲强度为48～72m/h。在对生物处理后的出水进行过滤时，需采取某种形式的辅助冲洗措施。
CAS号：
性质：一种下流式重力深床滤池。一般采用3种滤料，上层为无烟煤(粒径1～2mm)，中层为砂(粒径0.4～0.8mm)，底层为石榴石(粒径<0.5mm)。过滤速度为10m/h，反冲强度为48～72m/h。在对生物处理后的出水进行过滤时，需采取某种形式的辅助冲洗措施。
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