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PROTEIN INTERACTIONS WITH AND SEPARATIONS BY SYNTHETIC ULTRAFILTRATION MEMBRANES.

机译:蛋白质与合成超滤膜的相互作用及分离。

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Diaflo ultrafiltration (UF) membranes from Amicon Corp., polyacrylonitrile (PAN) membranes, and hydrophilized PAN membranes (designated as PAN-H membranes) were evaluated as to their ability to separate serum albumin (SA) from a gamma globulin (gG) fraction at pH 7.0 and 23{dollar}spcirc{dollar}C. High flux PAN-H and YM100 membranes were observed to recover more than 90% of their initial water fluxes upon rinsing with buffer after processing of protein. The best separation of SA from gG was obtained in a thin-channel crossflow cell; no separation was achieved in a stirred cell. The maximum separation corresponded to a permeate containing 2:1 SA:gG under initial feed conditions of 1:1 weight ratio of SA to gG and 1 mg/ml total protein concentration. The best separation was with PAN-H membranes of initial water flux of 200 {dollar}mu{dollar}m/sec-atm. The extent of separation decreased as the recirculation rate in the thin-channel cell was increased, or as the pressure or the initial protein concentration in the feed was increased. As the starting ratio of SA to gG in the feed was increased, the separation of the two increased.; For mixtures of SA-lysozyme and gG-lysozyme, large separation were obtained in both stirred and thin-channel cells with Diaflo and PAN-H membranes of appropriate porosity. Therefore, an increase in the molecular size differential of the proteins facilitated their separation.; The pore size distributions of both Diaflo and PAN/PAN-H membranes were determined by UF of polydisperse dextran. Aqueous gel permeation chromatography analysis generated a sieving profile from 4,000 to 2,000,000 daltons. A log-normal probability function described only the central portions of the dextran sieving profiles.; A mathematical model, based upon purely geometric considerations was developed to relate the flux and solute rejection of a membrane to the pore size distribution and the total number of pores; it proved useful in the comparison of membranes.; The polymeric dyes blue dextran 2000 and Poly R-478 were observed not to be applicable for the measurement of the molecular weight cutoff and flux of all membranes. These dyes were useful, however, for quality control tests of membrane integrity.
机译:对来自Amicon Corp.的Diaflo超滤(UF)膜,聚丙烯腈(PAN)膜和亲水化PAN膜(称为PAN-H膜)进行了评估,以从γ球蛋白(gG)组分中分离血清白蛋白(SA)的能力在7.0和23 {dollar} spcirc {dollar} C下的温度。观察到高通量的PAN-H和YM100膜在蛋白质加工后用缓冲液冲洗后可恢复其初始水通量的90%以上。在细通道错流池中,SA与gG的分离效果最佳。在搅拌池中没有分离。最大分离度对应于在初始进料条件下,SA与gG的重量比为1:1,总蛋白质浓度为1 mg / ml的渗透液中含有2:1 SA:gG。最佳分离是使用初始水通量为200 {μm} m / sec-atm的PAN-H膜。随着细通道池中再循环率的增加,或者进料中压力或初始蛋白质浓度的增加,分离程度降低。随着进料中SA与gG的起始比例增加,两者的分离度增加。对于SA溶菌酶和gG溶菌酶的混合物,在带有适当孔隙率的Diaflo和PAN-H膜的搅拌和薄通​​道细胞中均获得了较大的分离。因此,蛋白质分子大小差异的增加促进了它们的分离。 Diaflo和PAN / PAN-H膜的孔径分布均通过多分散右旋糖酐的超滤测定。凝胶渗透色谱分析产生的筛分曲线为4,000至2,000,000道尔顿。对数正态概率函数仅描述了右旋糖酐筛分曲线的中心部分。建立了基于纯粹几何考虑的数学模型,将膜的通量和溶质截留率与孔径分布和孔总数相关联;它被证明对膜的比较有用。观察到聚合染料蓝色葡聚糖2000和Poly R-478不适合用于测量所有膜的分子量截留值和通量。但是,这些染料可用于膜完整性的质量控制测试。

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