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Study of biomolecules partition coefficients on a novel continuous separator using polymer-salt aqueous two-phase systems

机译:聚合物-盐水溶液两相系统在新型连续分离器上生物分子分配系数的研究

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A novel experimental prototype device was evaluated for the continuous operation of an aqueous two-phase extraction protocol. As proof-of-concept, preliminary tests were performed using an organic blue and Gentian violet dyes, to demonstrate the capacity of the system for solute partitioning and continuous phase separation. Different experimental configurations were established by changing tubular separator length (3.0 and 5.0 m) and static mixer configurations (single Beads-filled tube, zig-zag, 3 Serial Beads-filled and tube Spiral/ single Beads-filled tube). The use of different static mixer configurations ensured total organic dyes transfer from bottom to top phase with shorter equilibration time (1.0-4.0 min) than batch system. The turbulent regime created at the entrance of the device by the static mixer, contributed to an efficient mass transfer that resulted in improvement of product partition coefficient (Kp) previously obtained from batch systems, when bovine serum albumin (BSA) was used as a model protein. A complex protein extract, namely whey protein extract (WPI), characterized by the presence of two main proteins (α-lactalbumin and β-lactoglobulin) with different phase affinities was successfully processed, resulting in differential protein partitioning with total recoveries up to 90% (top+bottom phase) and minimal protein precipitation at the interface. The obtained results suggested that the concentration of protein products in a defined phase could be feasible, by controlling the PEG-rich or salt-rich phase flow rates. These findings demonstrated the potential application of the proposed separator device for the continuous protein recovery using aqueous two-phase systems.
机译:新型实验原型设备进行了评估为水两相萃取协议的连续操作。作为概念验证,使用有机蓝色和Gentian紫色染料进行了初步测试,以证明系统用于溶质分配和连续相分离的能力。通过更改管状分离器的长度(3.0和5.0 m)和静态混合器配置(单珠填充管,之字形,3个连续珠填充和管螺旋/单珠填充管),建立了不同的实验配置。与分批系统相比,使用不同的静态混合器配置可确保总有机染料从下层相转移到上层相,并且平衡时间(1.0-4.0分钟)更短。当使用牛血清白蛋白(BSA)作为模型时,静态混合器在设备入口处产生的湍流状态有助于有效的传质,从而改善了以前从分批系统获得的产品分配系数(Kp)。蛋白。一种复杂的蛋白质提取物,即乳清蛋白提取物(WPI),其特征在于存在两种具有不同相亲合力的主要蛋白质(α-乳白蛋白和β-乳球蛋白),导致蛋白质差异分配,总回收率高达90% (顶部+底部相)和最小的蛋白质沉淀在界面上。获得的结果表明,通过控制富含PEG或富含盐的相的流速,在确定的相中浓缩蛋白质产物是可行的。这些发现证明了提出的分离器装置在使用含水两相系统连续回收蛋白质方面的潜在应用。

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