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采用尺寸排阻色谱模拟移动床对聚乙二醇颗粒进行分级。

Fractionation of polyethylene glycol particles by simulated moving bed with size-exclusion chromatography.

机构信息

Department of Chemical Engineering, I-Shou University, Kaohsiung City, Taiwan.

出版信息

J Chromatogr A. 2012 Mar 16;1229:107-12. doi: 10.1016/j.chroma.2011.12.094. Epub 2012 Jan 8.

Abstract

In this study, a three-section simulated moving bed (SMB) with an open-loop design is used to fractionate polyethylene glycol (PEG) with different molecular weights. The purchased PEGs are mixed and separated by the open-loop SMB. A size-exclusion column with a pore size ranging from 10 to 100 nm, TOSOH GMPW 7.5 mm × 30 cm, is used to separate the mixtures. Based on the Triangle theory, the operating parameters of the SMB are determined and used to separate the three binary mixtures. The results show that the PEG mixtures with molecular weights of 400 and 8000, and those of 1500 and 20,000, are separable, yet those of 1500 and 3500 are difficult to separate by the selected column. The relative elution for molecular weights of 400 and 8000, and 1500 and 2000, is 1.49 and 1.54, respectively, resulting in easy separation. However, the difference in the elution volume for mixtures with molecular weights of 1500 and 3500 is so small that the operation condition is confined to a tiny area on the (m(2), m(3)) plane defined by the Triangle theory. This makes robust application of the SMB impossible. Fortunately, it is still possible to obtain pure raffinate with low recovery, but a pure extract is still not possible. It is concluded that the low selectivity of the binary mixture and the fluctuation of the operation result in the difficulty in separating the 1500 and 3000 molecular weight mixtures. This paper presents the operation procedures, including the selection of the column, the discovery of selectivity, the application of the Triangle theory and the experimental results, in order to illustrate how to apply an SMB to the fractionation of PEGs.

摘要

在这项研究中,使用具有开环设计的三节模拟移动床(SMB)来对不同分子量的聚乙二醇(PEG)进行分级。所购买的 PEG 通过开环 SMB 进行混合和分离。使用 TOSOH GMPW 7.5mm×30cm 的孔径范围为 10 至 100nm 的尺寸排阻柱来分离混合物。基于三角形理论,确定 SMB 的操作参数并用于分离三种二元混合物。结果表明,分子量为 400 和 8000 的 PEG 混合物以及分子量为 1500 和 20000 的 PEG 混合物是可分离的,而所选柱难以分离分子量为 1500 和 3500 的 PEG 混合物。分子量为 400 和 8000 以及 1500 和 2000 的相对洗脱值分别为 1.49 和 1.54,因此易于分离。然而,分子量为 1500 和 3500 的混合物的洗脱体积差异非常小,以至于操作条件被限制在三角形理论定义的(m(2),m(3))平面上的一个微小区域内。这使得 SMB 的稳健应用变得不可能。幸运的是,仍然可以获得低回收率的纯馏分,但仍无法获得纯提取物。结论是二元混合物的低选择性和操作结果的波动导致难以分离分子量为 1500 和 3000 的混合物。本文介绍了操作程序,包括柱的选择、选择性的发现、三角形理论的应用和实验结果,以说明如何将 SMB 应用于 PEG 的分级。

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