膜
乙烯醇
反渗透
接触角
聚酰胺
苯酚
化学工程
渗透
化学
薄膜复合膜
高分子化学
渗透
色谱法
材料科学
聚合物
有机化学
生物化学
工程类
作者
Marwa Shalaby,Moustapha Salem Mansour,Mohamed Adel Ahmed,Heba Abdallah,Ibrahim Ismail Ibrahim,Marwa Abdel Fattah,Gaweł Sołowski
标识
DOI:10.1002/ceat.202200065
摘要
Abstract A commercial thin‐film membrane (unmodified) of polyamide improved by poly(vinyl alcohol) (PVA)‐coated membranes (modified) was investigated for separating phenol in sour water by reverse osmosis. Dependences of pressure and pore surface area on flux and phenol rejection were tested. A graphical correlation was found between the relative flux decline and phenol concentration decrease in the feed. The modified membrane provided rejection of 86 % at 2 bar with the highest permeate flux of 8.46 L m −2 h −1 . The average contact angle for the former membrane was 58.4°, while that for the modified membrane was 49.1°. The reduction in contact angle enhances the surface hydrophilicity of the membrane leading to the antifouling effect. The modified membrane provides 95.4 % flux recovery compared to the unmodified membrane that provides only 66.2 %.
科研通智能强力驱动
Strongly Powered by AbleSci AI