Islam Md Nazibul, Liu Yang, Herr Amy E
Department of Bioengineering, University of California, Berkeley, CA 94720, USA.
School of Chemical, Materials and Biomedical Engineering, University of Georgia, Athens, GA 30602, USA.
bioRxiv. 2024 Jun 2:2024.05.29.596534. doi: 10.1101/2024.05.29.596534.
Multiphasic buffer systems have been of greatest interest in electrophoresis and liquid-liquid electrotransfer; this study extends that foundation by exploring the interplay of the geometric and viscous properties of an interleaving oil layer on the electrotransfer of a charged analyte from an aqueous solution into a hydrogel. We utilized finite element analysis to examine two complementary configurations: one being electrotransfer of a charged analyte (protein) in an aqueous phase into a surrounding hydrogel layer and another being electrotransfer of the protein from that originating aqueous phase - through an interleaving oil layer of predetermined viscosity and thickness - and into a surrounding hydrogel layer. Results indicate that the presence of an oil layer leads to increased skew of the injected peak. To explain this difference in injection dispersion, we utilize Probstein's framework and compare the Péclet (Pe) number with the ratio between length scales characteristic to the axial and radial dispersion, respectively. The formulation assigns electrotransfer conditions into six different dispersion regimes. We show that the presence or absence of an interleaving oil layer moves the observed peak dispersion into distinct electrotransfer regimes; the presence of an oil layer augments the electrophoretic mobility mismatch between the different phases, resulting in a five-fold increase in Pe and a six-fold increase in the ratio between the axial to radial dispersion characteristic lengths. We further show that oil viscosity significantly influences resultant injection dispersion. A decrease in oil-layer viscosity from 0.08 Pa·s to 0.02 Pa·s results in a >100% decrease in injection dispersion. Our theoretical predictions were experimentally validated by comparing the electrotransfer regimes of three different mineral oil samples. We show that lowering the oil viscosity to 0.0039 Pa·s results in an injection regime similar to that of the absence of an oil layer. Additionally, we measure the migration distance and show that average electromigration velocity over the transit duration is inversely proportional to the viscosity of an interleaving oil layer. Understanding of the impact of electrotransfer of charged species across multiple immiscible fluid layers on peak dispersion informs the design of multiphasic electrophoresis systems.
多相缓冲系统在电泳和液-液电转移方面一直备受关注;本研究通过探索交错油层的几何和粘性特性对带电分析物从水溶液电转移到水凝胶中的相互作用,扩展了这一基础。我们利用有限元分析来研究两种互补配置:一种是将水相中的带电分析物(蛋白质)电转移到周围的水凝胶层中,另一种是蛋白质从起始水相通过具有预定粘度和厚度的交错油层电转移到周围的水凝胶层中。结果表明,油层的存在会导致注入峰的偏斜增加。为了解释注入分散的这种差异,我们利用普罗布斯坦的框架,分别将佩克莱特(Pe)数与轴向和径向分散特征长度尺度的比值进行比较。该公式将电转移条件分为六种不同的分散状态。我们表明,交错油层的存在与否会将观察到的峰分散转移到不同的电转移状态;油层的存在会增加不同相之间的电泳迁移率不匹配,导致Pe增加五倍,轴向与径向分散特征长度的比值增加六倍。我们进一步表明,油的粘度会显著影响最终的注入分散。油层粘度从0.08 Pa·s降低到0.02 Pa·s会导致注入分散降低>100%。我们通过比较三种不同矿物油样品的电转移状态,对理论预测进行了实验验证。我们表明,将油粘度降低到0.0039 Pa·s会导致注入状态类似于没有油层的情况。此外,我们测量了迁移距离,并表明在整个传输持续时间内的平均电迁移速度与交错油层的粘度成反比。了解带电物质在多个不混溶流体层之间的电转移对峰分散的影响,有助于多相电泳系统的设计。