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Effect of Non-Solvent Additives on the Structure and Performance of PVDF Hollow Fiber Membrane Contactor for CO2 Stripping

机译:非溶剂添加剂对PVDF中空纤维膜接触器结构和性能的影响

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摘要

Microporous polyvinylidene fluoride (PVDF) hollow fiber membranes with various non-solvent additives, i.e. lithium chloride, glycerol, polyethylene glycol (PEG-400), methanol and phosphoric acid, were fabricated for CO2 stripping via membrane contactors. The membranes were characterized in terms of liquid entry pressure, contact angle, gas permeation and morphology analysis. CO2 stripping performance was investigated by using an in-house made stainless steel module with CO2-preloaded aqueous diethanolamine as the liquid absorbent. Hydrophobicity and gas permeability of the membranes reduced with the addition of a non-solvent additive in the polymer dope but increase in liquid entry pressure was observed as more sponge-like structures developed in the inner layer of the fibers. It was found that PVDF/PEG-400 membrane produced the highest stripping flux of 4.03×10−2 mol m−2 s−1 which can be correlated to its high gas permeation and high effective surface porosity. The result of long-term stripping operation indicated an approximatly 80% stripping flux reduction which can be related to the interaction of polymer membrane and amine solution at high temperature.
机译:制造具有各种非溶剂添加剂的微孔聚偏二氟乙烯(PVDF)中空纤维膜,即氯化锂,甘油,聚乙二醇(PEG-400),甲醇和磷酸,用于通过膜接触器进行CO2汽提。通过液体进入压力,接触角,气体渗透和形态分析来表征膜。通过使用内部制造的不锈钢模块(其中装有预装了CO2的二乙醇胺水溶液作为液体吸收剂)研究了CO2的汽提性能。在聚合物涂料中添加非溶剂添加剂后,膜的疏水性和气体渗透性降低,但随着在纤维内层中形成更多的海绵状结构,观察到液体进入压力的增加。发现PVDF / PEG-400膜产生的最高剥离通量为4.03×10-2 mol m-2 s-1,这与其高透气性和高有效表面孔隙率有关。长期汽提操作的结果表明汽提通量减少了约80%,这可能与高温下聚合物膜和胺溶液的相互作用有关。

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