class='kwd-title'>Abbreviations: CNBr, cyanogen '/> Alternative preparation of inclusion bodies excludes interfering non-protein contaminants and improves the yield of recombinant proinsulin
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Alternative preparation of inclusion bodies excludes interfering non-protein contaminants and improves the yield of recombinant proinsulin

机译:包涵体的替代制备可排除干扰的非蛋白质污染物并提高重组胰岛素的产量

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摘要

class="kwd-title">Abbreviations: CNBr, cyanogen bromide; DTT, dithiothreitol; GSH/GSSG, reduced glutathione/oxidized glutathione; PS/DVB, polystyrene/divinylbenzene; RPC, reversed-phase chromatography; RP-HPLC, reversed-phase high-performance liquid chromatography; SDS-PAGE, sodium dodecyl sulfate-polyacrylamide gel electrophoresis; TCEP, tris(2-carboxyethyl)phosphine; TFA, trifluoroacetic acid class="kwd-title">Method name: Improved purification of recombinant proinsulin class="kwd-title">Keywords: Proinsulin, Prohormone, Protein expression, Inclusion bodies, Protein purification, HPLC protein analysis class="head no_bottom_margin" id="idm139752070027728title">AbstractThe goal of simple, high-yield expression and purification of recombinant human proinsulin has proven to be a considerable challenge. First, proinsulin forms inclusion bodies during bacterial expression. While this phenomenon can be exploited as a capture step, conventionally prepared inclusion bodies contain significant amounts of non-protein contaminants that interfere with subsequent chromatographic purification. Second, the proinsulin molecules within the inclusion bodies are incorrectly folded, and likely cross-linked to one another, making it difficult to quantify the amount of expressed proinsulin. Third, proinsulin is an intermediate between the initial product of ribosomal translation (preproinsulin) and the final product secreted by pancreatic beta cells (insulin). Therefore, to be efficiently produced in bacteria, it must be produced as an N-terminally extended fusion protein, which has to be converted to authentic proinsulin during the purification scheme. To address all three of these problems, while simultaneously streamlining the procedure and increasing the yield of recombinant proinsulin, we have made three substantive modifications to our previous method for producing proinsulin:. class="first-line-outdent">
  • • Conditions for the preparation of inclusion bodies have been altered so contaminants that interfere with semi-preparative reversed-phase chromatography are excluded while the proinsulin fusion protein is retained at high yield.
  • • Aliquots are taken following important steps in the procedure and the quantity of proinsulin-related polypeptide in the sample is compared to the amount present prior to that step.
  • • Final purification is performed using a silica-based reversed-phase matrix in place of a polystyrene-divinylbenzene-based matrix.
  • 机译:<!-fig ft0-> <!-fig @ position =“ anchor” mode =文章f4-> <!-fig mode =“ anchred” f5-> <!-fig / graphic | fig / alternatives / graphic mode =“ anchored” m1-> class =“ kwd-title”>缩写: CNBr,溴化氰; DTT,二硫苏糖醇; GSH / GSSG,还原型谷胱甘肽/氧化型谷胱甘肽; PS / DVB,聚苯乙烯/二乙烯基苯; RPC,反相色谱法; RP-HPLC,反相高效液相色谱; SDS-PAGE,十二烷基硫酸钠-聚丙烯酰胺凝胶电泳; TCEP,三(2-羧乙基)膦; TFA,三氟乙酸 class =“ kwd-title”>方法名称:改进的重组胰岛素原的纯化 class =“ kwd-title”>关键字:胰岛素原,激素,蛋白质表达,包涵体身体,蛋白质纯化,HPLC蛋白质分析 class =“ head no_bottom_margin” id =“ idm139752070027728title”>摘要简单,高产量表达和纯化重组人胰岛素原的目标已被证明是一个巨大的挑战。首先,胰岛素原在细菌表达过程中形成包涵体。虽然可以将这种现象用作捕获步骤,但常规制备的包涵体包含大量非蛋白质污染物,这些杂质会干扰后续的色谱纯化。其次,包涵体内的胰岛素原分子被错误地折叠,并且可能彼此交联,使得难以定量表达的胰岛素原的量。第三,胰岛素原是核糖体翻译的起始产物(胰岛素原)与胰腺β细胞分泌的最终产物(胰岛素)之间的中间产物。因此,要在细菌中有效生产,必须将其生产为N端延伸的融合蛋白,在纯化方案中必须将其转化为真正的胰岛素原。为了解决所有这三个问题,同时简化了流程并提高了重组胰岛素的产量,我们对以前的生产胰岛素的方法进行了三个实质性修改: class =“ first-line-outdent”> <! -list-behavior =简单的前缀-word = mark-type = none max-label-size = 9->
  • •制备包涵体的条件已更改,因此污染物会干扰排除半制备型反相色谱,同时保留胰岛素原融合蛋白的高产率。
  • •在该过程中的重要步骤和胰岛素原相关多肽的数量上均分取等分试样将样品中的样品与该步骤之前的含量进行比较。
  • •使用硅胶基反相基质代替聚苯乙烯-二乙烯基苯基基质进行最终纯化
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