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Surface modification to produce superhydrophobic hollow fiber membrane contactor to avoid membrane wetting for biogas purification under pressurized conditions

机译:生产超疏水中空纤维膜接触器的表面改性,以避免加压条件下沼气净化的膜润湿

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摘要

This article investigates CO2 removal from biogas (containing 40% CO2 and 60% CH4) using a hollow fiber membrane contactor (HFMC) with K2CO3 aqueous solutions as absorbent at elevated pressures up to 10 bar. Superhydrophobic PTFE membrane fibers (with a water contact angle of 158.4 degrees and sliding angle of 1.3 degrees) were fabricated by spraying silica nanoparticles on membrane surface and then used in membrane module for absorption experiments. The modified membrane outperformed the original membrane at elevated absorption pressures, and the highest CO2 removal efficiency and absorption flux reached 97.1% and 1.85 x 10(-3) mol m(-2) s(-1), respectively. A 2D axisymmetric non-wetted mathematic model was developed to determine the membrane wetness conditions during absorption experiments. The model validation results indicated that when using aqueous K2CO3 solutions as absorbent the modified superhydrophobic membrane used in this study was able to prevent membrane wetting even at pressurized conditions up to 10 bar. This work showed that the superhydrophobic membranes modified by spray-deposition technique have great potential for application in HFMC to avoid membrane wetting for biogas purification under pressurized conditions.
机译:本文研究使用中空纤维膜接触剂(HFMC)与K2CO3水溶液的沼气(含有40%CO 2和60%CH4)从沼气(含有40%CO 2和60%CH4)的CO 2一起去除,其吸收剂在高达10巴的升高压力下。通过在膜表面上喷涂二氧化硅纳米粒子,通过在膜表面上喷涂二氧化硅纳米颗粒,制备超疏水性PTFE膜纤维(具有158.4度的158.4度和1.3度的滑动角度)。然后用于吸收实验的膜组件。改性膜在升高的吸收压力下优于原始膜,并且最高的CO 2去除效率和吸收通量分别达到97.1%和1.85×10(-3)摩尔M(-2)S(-1)。开发了2D轴对称非湿润的数学模型以确定吸收实验期间的膜湿度条件。模型验证结果表明,当使用K2CO3水溶液作为吸收剂时,该研究中使用的改性超疏水膜即使在加压条件下也能够预防膜润湿,高达10巴。这项工作表明,通过喷雾沉积技术改性的超疏水膜具有很大的应用在HFMC中的应用,以避免在加压条件下造成沼气净化的膜润湿。

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