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SYNTHESIS OF 'CLICKABLE' MACRO-POROUS MATERIALS FOR ULTRAFAST PURIFICATION OF MONOCLONAL ANTIBODIES

机译:可以快速纯化单克隆抗体的“可固定”宏观多孔材料的合成

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Porous polymers are topical materials and have gained a lot of interest in both academic and industrial research because they combine particular features of porous materials with those of synthetic polymers. Nowadays, porous polymers are used for a variety of different application fields such as catalysis, gas storage, or as separation materials. Various manufacturing methods can be applied to produce macroscopic porous polymeric particles, but most of them require the utilisation of a suspension polymerisation process in the presence of a porogen. This method often negatively affects the control of the final morphologies and requires a tedious work up as the porogen has to be fully extracted. In previous works, we have already presented "reactive gelation" as an alternative, porogen-free method to produce macro-porous materials by controlled aggregation of colloidal polymer nanoparticles under high shear12. Nevertheless, the production of macroporous polymers, which allow an easy post-functionalization had yet to be proven to address relevant applications like the chromatography of therapeutic proteins for instance. Herein, we present the emulsion polymerisation of highly crosslinked styrene-co-vinyl benzyl azide core-shell nanoparticles (-40 nm), their aggregation at high shear rates (1061/s), and the hardening of the obtained fractal structures by post-polymerisation. This process results in chemically and physically stable macroporous microclusters with average size around 80 microns and pore sizes up to 10 urn. Thanks to the azide groups in the shell, the macroporous polymer scaffold can easily be post-functionalized by exploiting the concept of copper catalysed alkyne-azide cycloaddition (CuAAC). Among a vast number of functionalities that have been clicked onto the porous base material, we have also immobilised staphylococcus aureus protein A, well known as an affinity ligand for the capturing of monoclonal antibodies. By immobilising protein A on a macroporous scaffold, we are addressing the most significant bottleneck of large-scale production of therapeutic proteins, namely the purification of such. Indeed, the separation of the target protein from its cell impurities (host cell proteins, DNA, enzymes, etc.) often consists up to 80 % of the overall production costs because conventional chromatographic materials are not mechanically stable and only possess small pores (up to 150 nm). These smaller pores result in a diffusion-limited flow behaviour, making the downstream process costly and time-consuming. Our base material combines mechanical stability and perfusive flow behaviour, thereby providing protein separation at very high flow rates up to 1800 cm/hr. This excels conventional industrial materials by far, which can usually be used between 300-600 cm/hr. Noteworthy, the dynamic binding capacity is independent of the process rate, giving 10 g/l at 1800 cm/hr. The developed protein A prototype has also been proved stable under alkaline conditions, showing recovery above 80 % after 80 cycles with 0.1 M NaOH solution. However, since the industrial downstream process has a few other chromatographic steps following the capturing (such as ion-exchange chromatography and hydrophobic interaction chromatography), also polyelectrolytes and aliphatic molecules have successfully been attached to the macroporous base material. Addressing all types of chromatography needed during the purification of therapeutic proteins with just one base material highlights the true potential of this material, and might pave the way for perfusive protein chromatography. In summary, we have demonstrated emulsion polymerisation towards clickable core-shell nanoparticles, their aggregation under shear yielding macroporous particles, and their application as chromatography resins for the ultra-fast downstream of therapeutic proteins. Since the click chemistry protocol allows easy functionalization, the proposed process is expected to be suitable for other application fields as well.
机译:多孔聚合物是局部材料,并且由于其将多孔材料的特殊特征与合成聚合物的特征结合在一起,因而在学术和工业研究中都引起了很多兴趣。如今,多孔聚合物用于各种不同的应用领域,例如催化,气体存储或用作分离材料。可以采用各种制造方法来生产宏观的多孔聚合物颗粒,但是大多数方法需要在成孔剂存在下利用悬浮聚合工艺。这种方法通常会对最终形态的控制产生负面影响,并且由于必须完全提取致孔剂,因此需要繁琐的工作。在以前的工作中,我们已经提出了“反应凝胶化”作为一种替代方法,它是通过在高剪切力下通过控制胶体聚合物纳米粒子的可控聚集来生产大孔材料的无孔剂。然而,允许容易的后功能化的大孔聚合物的生产尚未被证明可解决相关的应用,例如治疗性蛋白质的色谱法。本文中,我们介绍了高度交联的苯乙烯-共乙烯基苄基叠氮化物核壳纳米粒子(-40 nm)的乳液聚合,它们在高剪切速率(1061 / s)下的聚集以及通过后固化对所得分形结构的硬化聚合。该过程导致化学和物理上稳定的大孔微团簇,其平均尺寸约为80微米,孔径最大为10微米。由于壳中有叠氮基,大孔聚合物支架可以通过利用铜催化的炔-叠氮化物环加成(CuAAC)的概念轻松地进行后功能化。在点击到多孔基础材料上的众多功能中,我们还固定了金黄色葡萄球菌蛋白A,这是众所周知的捕获单克隆抗体的亲和配体。通过将蛋白A固定在大孔支架上,我们正在解决大规模生产治疗性蛋白(即纯化此类蛋白)的最大瓶颈。的确,目标蛋白与其细胞杂质(宿主细胞蛋白,DNA,酶等)的分离通常占总生产成本的80%,因为常规色谱材料在机械上不稳定并且仅具有小孔(向上至150 nm)。这些较小的孔导致了扩散受限的流动行为,使得下游过程昂贵且费时。我们的基础材料兼具机械稳定性和良好的流动性能,从而以高达1800 cm / hr的高流速提供蛋白质分离。到目前为止,它优于传统的工业材料,通常可以在300-600 cm / hr之间使用。值得注意的是,动态结合能力与处理速率无关,在1800 cm / hr时可提供10 g / l。还证明了开发的Protein A原型在碱性条件下稳定,在使用0.1 M NaOH溶液循环80次后,回收率显示在80%以上。但是,由于工业下游工艺在捕获之后还有其他几个色谱步骤(例如离子交换色谱和疏水相互作用色谱),因此聚电解质和脂族分子也已成功地附着在大孔基材上。仅使用一种基础材料即可解决治疗性蛋白质纯化过程中所需的所有类型的色谱法,这凸显了该材料的真正潜力,并可能为进行渗透性蛋白质色谱法铺平道路。总而言之,我们已经证明了可点击的核-壳纳米粒子的乳液聚合,它们在剪切作用下的聚集产生了大孔粒子,以及它们作为用于治疗性蛋白质超快速下游的色谱树脂的应用。由于点击化学方案可以轻松实现功能化,因此所提出的方法也有望适用于其他应用领域。

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