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A polyamide resin based method for adsorption of anthocyanins from blackberries

机译:一种基于聚酰胺树脂的从黑莓中吸附花色苷的方法

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摘要

The present study deals with the downstream processing of anthocyanins from blackberries in order to obtain anthocyanins in a purified form. Adsorption was carried out employing four different mesh sizes of polyamide resin and among these, the 60-100 mesh polyamide resin showed the highest adsorption capacity (4.41 mg mL(-1) of the adsorbent) and desorption capacity (3.29 mg mL(-1) of the adsorbent). Adsorption results were found to correlate best using the Freundlich equation at all the temperatures studied. The second order kinetics model was found to be more appropriate to describe the adsorption of anthocyanins. Under all conditions, the polyamide resin showed optimal adsorption and desorption capacity towards anthocyanins at an initial concentration of 0.75 mg mL(-1), an adsorption liquid pH of 1, an eluent pH of 3 and an ethanol concentration of 80%. The dynamic adsorption process parameters for the purification of anthocyanins using the 60-100 mesh polyamide resin were as follows: processing volume, 5 BV; the flow rate of adsorption, 5 BV per h; the temperature of adsorption, 15 degrees C; eluent volume, 3.5 BV and the flow rate of desorption, 5 BV per h. Polyamide resin adsorption resulted in a gram of concentrated blackberry extract that contained 432 mg of anthocyanins, which was superior to cation exchange resin adsorption (160 mg g(-1)) and macroporous adsorbent resin adsorption (176 mg g(-1)). This method provides an efficient and low-cost approach for anthocyanin purification for industrial applications.
机译:本研究涉及黑莓中花色苷的下游加工,以获得纯化形式的花色苷。使用四种不同筛孔尺寸的聚酰胺树脂进行吸附,其中60-100目聚酰胺树脂显示出最高的吸附容量(4.41 mg mL(-1)的吸附剂)和解吸容量(3.29 mg mL(-1) )的吸附剂)。在所有研究温度下,使用Freundlich方程发现吸附结果之间的相关性最佳。发现二阶动力学模型更适合描述花色苷的吸附。在所有条件下,聚酰胺树脂在初始浓度为0.75 mg mL(-1),吸附液pH为1,洗脱液pH为3和乙醇浓度为80%时,都显示出对花色苷的最佳吸附和解吸能力。使用60-100目聚酰胺树脂提纯花色苷的动态吸附工艺参数如下:处理量,5 BV;吸附流速,每小时5 BV;吸附温度为15摄氏度;洗脱液体积为3.5 BV,脱附流速为每小时5 BV。聚酰胺树脂吸附后产生的克浓缩黑莓提取物每克含432 mg花青素,优于阳离子交换树脂吸附(160 mg g(-1))和大孔吸附树脂吸附(176 mg g(-1))。该方法为工业应用中的花色苷纯化提供了一种高效且低成本的方法。

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