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Novel process for the Separation and / or recovery of Citric Acid with ion exchange resins and chromatographic

机译:用离子交换树脂和色谱分离柠檬酸的新方法

摘要

The present Invention relates to a novel process for the Separation and Recovery of Citric Acid with ion exchange resins and chromatographicWhere the raw materials from Industrial Waste or by-products of fermentation broths, fruits, or any solution that contain IT,Because it can be characterized by a continuous or batch process and consists of the following stages. Stage 1. Saturation.The ion Exchange Column containing a Weakly basic anion Resin as Anger or Rage 93 68 or similarUpward flow is fed into the Broth containing the organic acid at a flow rate between 2 and 25 VC / hr to provoke a fluidized bed, Stage II. Circumvention.The Citrate ion adsorbed to the Resin was eluted with a Mineral acid in downward Flow preferably sulfuric acid at a concentration of 0.1 to 1.5 molar and a flow rate of 2 to 14 VC / hr until a sample of the eluates displayed the first Fire Traces of sulfates. Stage III. dechlorination.The Citric Acid Solution obtained in the previous Stage, if it is colored, it downstream to a Column containing a type Resin xad-4,XAD 16 or similar to a flow rate of 2 to 12 VC / HR, resulting in a Citric Acid Solution transparent.
机译:本发明涉及一种用离子交换树脂和色谱法分离和回收柠檬酸的新方法,其中工业废物的原料或发酵液,水果的副产物或任何含有IT的溶液的特征在于其特征通过连续或分批过程进行,并包括以下阶段。阶段1.饱和。含有弱碱性阴离子树脂(如愤怒或愤怒93 68或类似物)的离子交换柱以2至25 VC / hr的流速被送入含有有机酸的肉汤中,以引发流化床,第二阶段。规避。吸附在树脂上的柠檬酸根离子用无机酸向下洗脱,最好以0.1至1.5摩尔浓度,流速为2至14 VC / hr的硫酸流动,直到洗脱液样品显示出第一个硫酸痕迹。第三阶段。在前一阶段获得的柠檬酸溶液,如果是有色的,则在下游的色谱柱中含有树脂xad-4,XAD 16或类似的流速为2至12 VC / HR柠檬酸溶液透明。

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