高校化学工程学报
高校化學工程學報
고교화학공정학보
JOURNAL OF CHEMICAL ENGINEERING OF CHINESE UNIVERSITIES
2012年
6期
1037-1042
,共6页
金丽梅%于水利%时文歆%衣雪松%孙楠%王硕%马聪
金麗梅%于水利%時文歆%衣雪鬆%孫楠%王碩%馬聰
금려매%우수리%시문흠%의설송%손남%왕석%마총
聚酰胺-胺%PAMAM%界面聚合%纳滤膜
聚酰胺-胺%PAMAM%界麵聚閤%納濾膜
취선알-알%PAMAM%계면취합%납려막
poly(amidoamine)%PAMAM%interfacial polymerization%nanofiltration membrane
以聚砜超滤膜为支撑膜,通过聚酰胺-胺(PAMAM,G0)与均苯三甲酰氯(TMC)的界面聚合反应制备复合纳滤膜.首先优化了界面聚合过程,并通过场发射扫描电子显微镜(FESEM)进行了膜的表面形貌分析,最后考察了纳滤膜对Na2SO4、不同分子量聚乙二醇及小分子有机物的分离性能.结果表明:较优的纳滤膜制备条件为:PAMAM浓度0.25%(wt),TMC浓度0.3%(wt),界面聚合时间90 s,热处理温度60℃.FESEM分析表明经界面聚合反应后,超滤膜表面形成了一层致密的活性层.随着操作压力的增加及Na2 SO4浓度的降低,膜对盐的截留率均不断增大.复合纳滤膜可有效截留盐,且其截留分子量(MWCO)处于600~1000 g?mol?1.
以聚砜超濾膜為支撐膜,通過聚酰胺-胺(PAMAM,G0)與均苯三甲酰氯(TMC)的界麵聚閤反應製備複閤納濾膜.首先優化瞭界麵聚閤過程,併通過場髮射掃描電子顯微鏡(FESEM)進行瞭膜的錶麵形貌分析,最後攷察瞭納濾膜對Na2SO4、不同分子量聚乙二醇及小分子有機物的分離性能.結果錶明:較優的納濾膜製備條件為:PAMAM濃度0.25%(wt),TMC濃度0.3%(wt),界麵聚閤時間90 s,熱處理溫度60℃.FESEM分析錶明經界麵聚閤反應後,超濾膜錶麵形成瞭一層緻密的活性層.隨著操作壓力的增加及Na2 SO4濃度的降低,膜對鹽的截留率均不斷增大.複閤納濾膜可有效截留鹽,且其截留分子量(MWCO)處于600~1000 g?mol?1.
이취풍초려막위지탱막,통과취선알-알(PAMAM,G0)여균분삼갑선록(TMC)적계면취합반응제비복합납려막.수선우화료계면취합과정,병통과장발사소묘전자현미경(FESEM)진행료막적표면형모분석,최후고찰료납려막대Na2SO4、불동분자량취을이순급소분자유궤물적분리성능.결과표명:교우적납려막제비조건위:PAMAM농도0.25%(wt),TMC농도0.3%(wt),계면취합시간90 s,열처리온도60℃.FESEM분석표명경계면취합반응후,초려막표면형성료일층치밀적활성층.수착조작압력적증가급Na2 SO4농도적강저,막대염적절류솔균불단증대.복합납려막가유효절류염,차기절류분자량(MWCO)처우600~1000 g?mol?1.
Composite NF membranes were prepared by interfacial polymerization of poly(amidoamine)(PAMAM,G0) and trimesoyl chloride (TMC) on the substrate of PSF UF membrane. The interfacial polymerization process was optimized and the performance of the membrane was characterized with FESEM, then the prepared NF membranes were used to separate Na2SO4, PEG with different molecular weight and small organic molecules. The experimental results indicate that the optimal preparation conditions are PAMAM concentration 0.25% (wt), TMC concentration 0.3% (wt), interfacial polymerization time 90 s, heat treatment temperature 60℃. As indicated by FESEM, selective layer of PA nanofiltration is formed on the substrate layer which is thin and dense after interfacial polymerization. The rejection increases with the increase of operating pressure and decreases with the increase of Na2SO4 concentration. The NF membrane can effectively reject salt ions and the cut-off molecular weight (MWCO) of the resulting membrane is 600~1000 g?mol?1.