...
首页> 外文期刊>Journal of industrial microbiology & biotechnology >Separation of xylose oligomers using centrifugal partition chromatography with a butanol-methanol-water system
【24h】

Separation of xylose oligomers using centrifugal partition chromatography with a butanol-methanol-water system

机译:使用丁醇-甲醇-水系统的离心分配色谱法分离木糖低聚物

获取原文
获取原文并翻译 | 示例
           

摘要

Xylose oligomers are the intermediate products of xylan depolymerization into xylose monomers. An understanding of xylan depolymerization kinetics is important to improve the conversion of xylan into monomeric xylose and to minimize the formation of inhibitory products, thereby reducing ethanol production costs. The study of xylan depolymerization requires copious amount of xylose oligomers, which are expensive if acquired commercially. Our approach consisted of producing in-house oligomer material. To this end, birchwood xylan was used as the starting material and hydrolyzed in hot water at 200 degrees C for 60 min with a 4% solids loading. The mixture of xylose oligomers was subsequently fractionated by a centrifugal partition chromatography (CPC) with a solvent system of butanol:methanol:water in a 5:1:4 volumetric ratio. Operating in an ascending mode, the butanol-rich upper phase (the mobile phase) eluted xylose oligomers from the water-rich stationary phase at a 4.89 mL/min flow rate for a total fractionation time of 300 min. The elution of xylose oligomers occurred between 110 and 280 min. The yields and purities of xylobiose (DP 2), xylotriose (DP 3), xylotetraose (DP 4), and xylopentaose (DP 5) were 21, 10, 14, and 15 mg/g xylan and 95, 90, 89, and 68%, respectively. The purities of xylose oligomers from this solvent system were higher than those reported previously using tetrahydrofuran:dimethyl sulfoxide:water in a 6:1:3 volumetric ratio. Moreover, the butanol-based solvent system improved overall procedures by facilitating the evaporation of the solvents from the CPC fractions, rendering the purification process more efficient.
机译:木糖低聚物是木聚糖解聚为木糖单体的中间产物。对木聚糖解聚动力学的理解对于提高木聚糖向单体木糖的转化并最小化抑制产物的形成是重要的,从而降低乙醇生产成本。对木聚糖解聚的研究需要大量的木糖低聚物,如果从商业上获得则价格昂贵。我们的方法包括生产内部低聚物材料。为此,将桦木木聚糖用作起始材料,并在固体含量为4%的情况下于200摄氏度的热水中水解60分钟。随后通过离心分配色谱法(CPC),以体积比为5:1:4的丁醇:甲醇:水的溶剂体系对木糖低聚物的混合物进行分馏。以升压模式运行时,富含丁醇的上层相(流动相)以4.89 mL / min的流速从富含水的固定相洗脱出木糖低聚物,总分馏时间为300分钟。木糖低聚物的洗脱发生在110至280分钟之间。木糖(DP 2),木三糖(DP 3),木四糖(DP 4)和木戊糖(DP 5)的产量和纯度分别为21、10、14和15 mg / g木聚糖和95、90、89和分别为68%。来自该溶剂系统的木糖低聚物的纯度高于以前使用体积比为6:1:3的四氢呋喃:二甲基亚砜:水的纯度。此外,丁醇基溶剂系统通过促进从CPC馏分中蒸发掉溶剂,改善了整个流程,从而使纯化过程更加有效。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号