化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2012年
5期
1088-1095
,共8页
孙志猛%任晓晶%赵可卉%张忠国%赵义平%陈莉%程言君
孫誌猛%任曉晶%趙可卉%張忠國%趙義平%陳莉%程言君
손지맹%임효정%조가훼%장충국%조의평%진리%정언군
哌嗪%均苯三甲酰氯%聚乙烯醇%界面聚合%复合纳滤膜%脱墨废水
哌嗪%均苯三甲酰氯%聚乙烯醇%界麵聚閤%複閤納濾膜%脫墨廢水
고진%균분삼갑선록%취을희순%계면취합%복합납려막%탈묵폐수
piperazine%trimesoyl chloride%polyvinyl alcohol%interracial polymerization%compositenanofiltration membrane%deinking wastewater
以哌嗪(PIP)和均苯三甲酰氯(TMC)为反应单体,以聚乙烯醇(PVA)为添加剂,通过界面聚合法在聚砜超滤基膜上制备了复合纳滤膜,主要研究了PVA、PIP、TMC单体浓度、热处理条件对复合膜性能的影响,并通过扫描电子显微镜(SEM)、原子力显微镜(AFM)对复合纳滤膜结构和形貌进行表征。研究表明,PVA能够提高膜通量,增强膜亲水性,提高膜表面光滑度。最佳制膜条件是:PIP浓度为3.0 g/L,TMC浓度为1.0 g/L,PVA浓度为0.54 g/L,界面聚合时间为1 min,热处理温度为50℃,热处理时间10 min。制备的纳滤膜在处理Na2SO4、MgSO4、NaCl和MgCl2等4种盐溶液时,其截留性能与陶氏NF-270和星达NFX膜相近,而在深度处理造纸脱墨废水时,也表现出良好的分离性能和耐污染性能。
以哌嗪(PIP)和均苯三甲酰氯(TMC)為反應單體,以聚乙烯醇(PVA)為添加劑,通過界麵聚閤法在聚砜超濾基膜上製備瞭複閤納濾膜,主要研究瞭PVA、PIP、TMC單體濃度、熱處理條件對複閤膜性能的影響,併通過掃描電子顯微鏡(SEM)、原子力顯微鏡(AFM)對複閤納濾膜結構和形貌進行錶徵。研究錶明,PVA能夠提高膜通量,增彊膜親水性,提高膜錶麵光滑度。最佳製膜條件是:PIP濃度為3.0 g/L,TMC濃度為1.0 g/L,PVA濃度為0.54 g/L,界麵聚閤時間為1 min,熱處理溫度為50℃,熱處理時間10 min。製備的納濾膜在處理Na2SO4、MgSO4、NaCl和MgCl2等4種鹽溶液時,其截留性能與陶氏NF-270和星達NFX膜相近,而在深度處理造紙脫墨廢水時,也錶現齣良好的分離性能和耐汙染性能。
이고진(PIP)화균분삼갑선록(TMC)위반응단체,이취을희순(PVA)위첨가제,통과계면취합법재취풍초려기막상제비료복합납려막,주요연구료PVA、PIP、TMC단체농도、열처리조건대복합막성능적영향,병통과소묘전자현미경(SEM)、원자력현미경(AFM)대복합납려막결구화형모진행표정。연구표명,PVA능구제고막통량,증강막친수성,제고막표면광활도。최가제막조건시:PIP농도위3.0 g/L,TMC농도위1.0 g/L,PVA농도위0.54 g/L,계면취합시간위1 min,열처리온도위50℃,열처리시간10 min。제비적납려막재처리Na2SO4、MgSO4、NaCl화MgCl2등4충염용액시,기절류성능여도씨NF-270화성체NFX막상근,이재심도처리조지탈묵폐수시,야표현출량호적분리성능화내오염성능。
A composite polypiperazine-amide nanofiltration membrane, supported by polysulfone ( PSF ) ultrafiltration membrane, was prepared via interracial polymerization ofpiperazine ( PIP ) and trimesoyl chloride ( TMC ) in the present ofpolyvinyl alcohol ( PVA ) . The effects of PVA, PIP and TMC concentration, temperature and time of heat treatment on the composite membrane were studied, and the surface structure and morphology were analyzed by scanning electron microscope ( SEM ) and atomic force microscopy ( AFM ) . The experiment results showed that increasing PVA content would lead to the increase in the flux of the nanofiltration membrane, make the nanofiltration membrane more hydrophilic, and cause the surface of the nanofiltration membrane smoother. The optimal preparing condition of the composite membrane was 3.0 g/LTMC, 1.0 g/L PIP, 0.54 g/L PVA, 1 min reaction time, and 10 min heat treatment at 50 ℃.The separation performance of self-made nanofiltration membrane, treating the solutions of Na2SO4, MgSO4, NaC1 or MgC12, was similar to that of the commercial nanofiltration membranes, such as Dow NF-270 and Synder. Furthermore, the nanofiltration membrane also showed very good separation and anti-fouling performance in the advanced treatment of deinking wastewater.