绿豆蛋白污染超滤装置的清洗

Wei-Jen Chen, W. Ko
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引用次数: 1

摘要

采用ES-30超滤膜(分子量截止30000)对绿豆淀粉加工废水中的蛋白质进行了回收。在超滤过程中,由于结垢和浓差极化,装置的渗透通量从108.5 l/m2/h下降到4.0 l/m2/h。用自来水、0.5% NaOH、0.2N HCl和0.75% terg - a酶分别洗涤,通量分别恢复到10.8、40.7、50.0和82.4 l/m2/h。清洗剂及其浓度对清洗效果有显著影响。通过与表面活性剂Triton X-100(0.1%)混合,提高了NaOH的清洗效果。超滤后,用自来水连续循环10min,然后用0.3% NaOH与0.1% Triton X-100混合10min,再用0.2 N HCl混合10min,再用0.75% terg - a酶在50℃下循环30min,使装置的通量基本恢复到原来的水平。每次用清洗剂,特别是酸或碱性溶液洗涤后,都需要立即用水循环。一个半小时就足够完成清洗过程了。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Cleaning of Ultrafiltration Unit Fouled by Mungbean Protein
An ultrafiltration unit, the ES-30 membrane (molecular weight cut-off 30,000) was used to recover the proteins from the wastewater produced during mungbean starch processing. During ultrafiltration, the permeate flux of the unit decreased from 108.5 to 4.0 l/m2/h due to fouling and concentration polarization. The flux could be restored to 10.8, 40.7, 50.0, and 82.4 l/m2/h by washing individually with tap water, 0.5% NaOH, 0.2N HCl, and 0.75% Terg-A-enzyme, respectively. The cleaning effect was significantly affected by the cleaning agents and their concentrations. The cleaning effect of NaOH was enhanced by mixing with 0.1% Triton X-100 (a surfactant). After ultrafiltration, continuous circulation with tap water for 10 min, followed by 0.3% NaOH mixed with 0.1% Triton X-100 for 10 min, 0.2 N HCl for 10 min, and by 0.75% Terg-A-enzyme at 50°C for 30 min nearly restored the original flux of the unit. Circulation with water was immediately required after each washing with cleaning agents, especially with acid or basic solution. One and a half hours was sufficient to complete the washing process.
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