北京化工大学学报(自然科学版)
北京化工大學學報(自然科學版)
북경화공대학학보(자연과학판)
JOURNAL OF BEIJING UNIVERSITY OF CHEMICAL TECHNOLOGY
2010年
1期
19-22
,共4页
刘玉君%丁忠伟%刘丽英%牛秦肃%马润宇
劉玉君%丁忠偉%劉麗英%牛秦肅%馬潤宇
류옥군%정충위%류려영%우진숙%마윤우
微滤%浸没式中空纤维膜%鼓泡%反冲洗%阻力分析
微濾%浸沒式中空纖維膜%鼓泡%反遲洗%阻力分析
미려%침몰식중공섬유막%고포%반충세%조력분석
microfiltration%submerged hollow fiber membrane%gas bubbling%backwash%resistance analysis
针对浸没式中空纤维膜微滤过程中颗粒物污染膜的情况,提出采用鼓泡、反冲洗以及鼓泡和反向脉冲清洗联合使用的方法和措施来减缓或消除膜污染.实验结果表明,鼓泡的作用在于减少膜表面颗粒物的堆积,在鼓泡气量为300mL/min的条件下,鼓泡可以使滤饼阻力减少到原来的40%.而周期性的反冲洗,如每过滤10min反冲洗4min条件下,使得膜内部污染阻力下降到不带反冲洗条件下的1/3.反向脉冲清洗(每过滤10 min反向脉冲清洗30 B)和鼓泡(气量为160mL/min)的联合使用是本系统的最优膜污染控制方法,可以使滤饼阻力和膜内部污染阻力分别降低到没有任何膜污染控制措施下的10%和20%.
針對浸沒式中空纖維膜微濾過程中顆粒物汙染膜的情況,提齣採用鼓泡、反遲洗以及鼓泡和反嚮脈遲清洗聯閤使用的方法和措施來減緩或消除膜汙染.實驗結果錶明,鼓泡的作用在于減少膜錶麵顆粒物的堆積,在鼓泡氣量為300mL/min的條件下,鼓泡可以使濾餅阻力減少到原來的40%.而週期性的反遲洗,如每過濾10min反遲洗4min條件下,使得膜內部汙染阻力下降到不帶反遲洗條件下的1/3.反嚮脈遲清洗(每過濾10 min反嚮脈遲清洗30 B)和鼓泡(氣量為160mL/min)的聯閤使用是本繫統的最優膜汙染控製方法,可以使濾餅阻力和膜內部汙染阻力分彆降低到沒有任何膜汙染控製措施下的10%和20%.
침대침몰식중공섬유막미려과정중과립물오염막적정황,제출채용고포、반충세이급고포화반향맥충청세연합사용적방법화조시래감완혹소제막오염.실험결과표명,고포적작용재우감소막표면과립물적퇴적,재고포기량위300mL/min적조건하,고포가이사려병조력감소도원래적40%.이주기성적반충세,여매과려10min반충세4min조건하,사득막내부오염조력하강도불대반충세조건하적1/3.반향맥충청세(매과려10 min반향맥충청세30 B)화고포(기량위160mL/min)적연합사용시본계통적최우막오염공제방법,가이사려병조력화막내부오염조력분별강저도몰유임하막오염공제조시하적10%화20%.
This study is aimed at improving the particle fouled submerged hollow fiber membrane microfiltration process by employing several methods to alleviate or eliminate membrane fouling. The total resistance in microfiltra-tion can he classified into clean membrane resistance R_m, cake resistance Ro and membrane internal fouling resist-ance R_i. It was found that gas bubbling is helpful in reducing particle deposition on the membrane surface, e.g. R_c was only 40% of that without bubbling when the gas flow rate was 300 mL/min. Periodic backwashing could mainly mitigate internal fouling of the membrane, e.g. under conditions of 4 min backwashing for every 10 min filtration, R_i was 33% of that without backwashing. The combination of backpulsing (30 s backpulsing for every 10 min filtra-tion) and gas bubbling (with a gas flow rate of 160 mL/min) was found to he the optimal strategy for this sub-merged microfihration system; under these conditions the values of R_c and R_i were just 10% and 20% of the corre-sponding values without employing any membrane fouling controlling method.