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Operational parameters optimization of cross-flow ceramic membrane ultrafiltration for water depyrogenation.

机译:用于水热解的错流陶瓷膜超滤操作参数优化。

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Water ultrafiltration has been suggested as an alternative for the removal of lypopolysaccharides in the production of Water for Injection and, Pyrogen Reduced Water. Ultrafiltration of water using an annular ceramic membrane with nominal molecular weight cut off 50,000, has been confirmed as a viable choice for the production of such water types, producing filtrates of pyrogenic concentration below 0.03 EU/mL at permeate rates of up to 775 L/m2-hr. Operational parameters like endotoxin feed concentration, feed rate and transmembrane pressure were assessed utilizing a factorial experimental design. The flux profiles obtained showed a linear relationship with transmembrane pressure up to the maximum concentrations studied of 667 EU/mL. Statistical evidence revealed that the permeate flux response is proportionally determined by the feed rate and transmembrane pressure main factors and the interaction of them. The endotoxin concentration was statistically identified as a non-significant factor affecting permeates flux.
机译:在注射用水和减少热原的水的生产中,已经建议使用水超滤作为去除脂多糖的替代方法。使用环形陶瓷膜对水进行超滤,标称分子量<50,000,已被证实是生产此类水的可行选择,在高达775 L的渗透速率下,产生热解浓度低于0.03 EU / mL的滤液/ m2-hr。使用因子试验设计评估了诸如内毒素进料浓度,进料速率和跨膜压等操作参数。所获得的通量曲线显示跨膜压力与所研究的最大浓度667 EU / mL呈线性关系。统计证据表明,渗透通量响应由进料速率和跨膜压力主要因素以及它们之间的相互作用成比例地确定。内毒素浓度经统计学鉴定为影响渗透通量的非重要因素。

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