Influencing factors of polarization coefficient of hollow fiber membrane
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摘要:
以氧氮分离为研究对象,通过建立中空纤维膜气体分离数学模型,分析丝内外压差、进气初始氧体积分数、进气流量、丝外侧背压等参数对极化系数的影响,以探究操作参数对浓差极化影响程度,并提出降低浓差极化技术方案。研究表明:在考虑丝内压降、浓差极化现象的情况下,所建立的中空纤维膜气体分离数学模型具有一定的可信度;丝内外压差、进气初始氧体积分数、进气流量、丝外侧背压等因素对极化系数有一定影响,其中极化系数与丝内外压差、进气初始氧体积分数、丝外侧背压呈正相关,与进气流量呈负相关;可采用渗透侧负压抽吸方式提高膜透过流量、降低浓差极化。
Abstract:The study of concentration polarization, and the analysis of its influencing factors and mechanism are theoretical basis for improving the performance of hollow fiber membrane and the separation efficiency. By establishing a mathematical model of hollow fiber membrane separation of oxygen and nitrogen, the influences of parameters, such as pressure difference between the inside and outside of the filament, initial oxygen concentration of intake air, intake air flow rate and back pressure outside the filament on the polarization coefficient, were analyzed to explore the influence degree of operating parameters on the concentration polarization, and a technical scheme was put forward to reduce the concentration polarization. Factors such as pressure difference between the inside and outside of the filament, initial oxygen concentration of intake air, intake air flow rate, and back pressure outside the filament had a certain effect on the polarization coefficient, among them, the polarization coefficient was positively correlated with pressure difference inside and outside of the filament, initial oxygen concentration of intake air, and back pressure outside the filament, and was negatively correlated with intake air flow. Negative pressure suction on the permeation side can be used to increase the membrane permeation flow rate and reduce the concentration polarization. The influence of concentration polarization on membrane performance was reduced by controlling various factors.
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表 1 实验数据与微分数学模型计算结果对比
Table 1. Comparison of experimental data with calculated results of differential mathematical model
序号 操作条件 xl/% pi/105 Pa T/K ul/(kg/h) x0/% 实验值 计算值1 计算值2 1 4 303.15 20 21 7.63 7.52 8.04 2 4 323.15 20 21 6.78 6.75 7.21 3 4 343.15 20 21 6.26 6.20 6.63 4 4 363.15 20 21 6.05 6.01 6.42 5 4 383.15 20 21 5.83 5.84 6.24 6 6 303.15 20 21 5.34 5.31 5.74 7 6 323.15 20 21 4.35 4.30 4.64 8 6 343.15 20 21 4.00 3.95 4.25 9 6 363.15 20 21 3.95 3.87 4.17 10 6 383.15 20 21 4.16 4.12 4.45 注:计算值1为考虑浓差极化的情况,计算值2为不考虑浓差极化的情况。 -
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