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Concentration of glycerol from dilute glycerol wastewater using sweeping gas membrane distillation

机译:吹扫气膜蒸馏法从稀甘油废水中浓缩甘油

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摘要

In this work, experimental results for the concentration of dilute glycerol wastewater using membrane distillation (MD) with a microporous hydrophobic flat-sheet PTFE membrane are reported. Experiments were performed using the sweeping gas mode of the MD (SGMD) process. The effects of various operating variables, such as feed temperature, glycerol concentration in aqueous phase, feed flow rate and sweeping gas flow rate were studied. A Taguchi analysis has been performed on the experimental results which determined the effects and contribution of each of the factors on the distillate flux and the interactions between the operating variables. Results showed that the most influential factor was feed temperature. The second significant contribution was observed for the sweeping gas flow rate. Feed concentration had a negative effect on the distillate flux. At optimum conditions (i.e. 65 C, 400mL/min, 1 mass%, and 0.453 Nm~3/h), the Taguchi model predicted the value of the response (the distillate flux) as 20.93 L/m2 h, which had good agreement with the experimental results.
机译:在这项工作中,报道了使用带有微孔疏水性平板PTFE膜的膜蒸馏(MD)浓缩甘油废水的实验结果。使用MD(SGMD)工艺的吹扫气模式进行了实验。研究了各种操作变量的影响,例如进料温度,水相中的甘油浓度,进料流速和吹扫气流速。 Taguchi分析已对实验结果进行了分析,确定了每个因素对馏分通量的影响和贡献以及操作变量之间的相互作用。结果表明,影响最大的因素是进料温度。观察到的第二大贡献是吹扫气体流速。进料浓度对馏分通量有负面影响。 Taguchi模型在最佳条件下(即65°C,400mL / min,1质量%和0.453 Nm〜3 / h)预测的响应值(馏分通量)为20.93 L / m2 h,具有很好的一致性。与实验结果。

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