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Solvent extraction of organic acids from stillage for its re-use in ethanol production process

机译:从釜馏物中溶剂萃取有机酸,再用于乙醇生产工艺

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摘要

Stillage re-use in the fermentation stage in ethanol production is a technique used for the reduction of water and fermentation nutrients consumption. However, the inhibitory effect on yeast growth of the by-products and feed components that remains in stillage increases with re-use and reduces the number of possible recycles. Several methods such as ultrafiltration, electro-dialysis and advanced oxidation processes have been used in stillage treatment prior its re-use in the fermentation stage. Nevertheless, few studies evaluating the effect of solvent extraction as a stillage treatment option have been performed. In this work, the inhibitory effect of serial stillage recycling over ethanol and biomass production was determined, using acetic acid as a monitoring compound during the fermentation and solvent extraction process. Raw palm oil methyl ester showed the highest acetic acid extraction from the aqueous phase, presenting a distribution coefficient of 3.10 for a 1:1 aqueous phase mixture:solvent ratio. Re-using stillage without treatment allowed up to three recycles with an ethanol production of 53.7 ± 2.0 g L~(-1), which was reduced 25% in the fifth recycle. Alternatively, treated stillage allowed up to five recycles with an ethanol final concentration of 54.7 1.3 g L~(-1). These results show that reduction of acetic acid concentration by an extraction process with raw palm oil methyl ester before re-using stillage improves the number of recycles without a major effect on ethanol production. The proposed process generates a palm oil methyl ester that contains organic acids, among other by-products, that could be used for product recovery and as an alternative fuel.
机译:在乙醇生产中的发酵阶段,蒸馏物的再利用是用于减少水和发酵营养物消耗的技术。但是,残留在酒糟中的副产物和饲料成分对酵母生长的抑制作用随重复使用而增加,并减少了可能的循环次数。在釜馏处理中将几种方法(例如超滤,电渗析和高级氧化工艺)用于其在发酵阶段的再利用之前。然而,很少有研究评估溶剂萃取作为釜馏处理选项的效果。在这项工作中,在发酵和溶剂萃取过程中,使用乙酸作为监测化合物,确定了连续馏分回收对乙醇和生物质生产的抑制作用。未加工的棕榈油甲酯显示出从水相中提取的乙酸最高,对于1:1的水相混合物:溶剂比率,其分配系数为3.10。未经处理再利用釜馏物最多可进行三个循环,乙醇产量为53.7±2.0 g L〜(-1),在第五次循环中减少了25%。或者,经处理的釜馏物最多可进行5次循环,乙醇终浓度为54.7 1.3 g L〜(-1)。这些结果表明,在重新使用釜馏物之前,通过使用粗棕榈油甲酯的萃取工艺降低乙酸浓度可以提高循环次数,而不会对乙醇生产产生重大影响。所提出的方法产生了一种棕榈油甲酯,其中含有有机酸以及其他副产物,这些有机酸可用于产品回收和替代燃料。

著录项

  • 来源
    《Waste management & research》 |2010年第6期|P.533-538|共6页
  • 作者单位

    Department of Chemical Engineering, Universidad Nacional de Colombia (Sede Bogota), Bogota, Colombia;

    rnDepartment of Chemical Engineering, Universidad Nacional de Colombia (Sede Bogota), Bogota, Colombia;

    rnInborn Errors of Metabolism Institute, Pontificia Universidad Javeriana, Bogota, Colombia;

    rnDepartment of Chemical Engineering, Design Group of Process and Products, Universidad de Los Andes, Kra 1 E No. 19 A-40, Bogota, Colombia;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    ethanol; stillage; solvent extraction; raw palm oil methyl ester;

    机译:乙醇酒糟溶剂萃取;原料棕榈油甲酯;
  • 入库时间 2022-08-17 13:44:48

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