首页> 外文期刊>Innovative Food Science & Emerging Technologies >Coupling of pressure-driven membrane technologies for concentrating, purifying and fractionizing betacyanins in cactus pear (Opuntia dillenii Haw.) juice
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Coupling of pressure-driven membrane technologies for concentrating, purifying and fractionizing betacyanins in cactus pear (Opuntia dillenii Haw.) juice

机译:压力驱动膜技术在仙人掌梨(Opuntia dillenii Haw.)果汁中浓缩,纯化和分馏β染色的耦合

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An integrated process coupling crossflow micro and ultra or nanofiltration was applied to separate the betacyanins in cactus pear juice (30 degrees C). Four microfiltration ceramic membranes (0.1-0.2 mu m, 1.8-3.3 bar) and 4 ultra/nanofiltration organic membranes (0.2-4.0 kDa, 5-30 bar) were tested. Microfiltration was a first step to remove insoluble solids with low retention of soluble solids. By coupling with enzymatic liquefaction, permeate flux Jp was increased by 2 and the retention of betacyanins was limited. Ultra/nanofiltration was then used for solute separation. Retentions of solutes could be modulated by varying membrane/pressure combinations that favor rather the concentration of all the solutes or rather the purification of the betacyanins with respect to the total dry matter. Retention of individual betacyanins could be a little different which also made possible fractionation. Simulations using simple models allowed to evaluate the interest of the process for concentrating, purifying and fractionating betacyanins with a possible diafiltration step.
机译:施用综合处理偶联的偶联微杂交和超滤,以将甲基吡喃汁(30℃)分离。测试四种微滤陶瓷膜(0.1-0.2μm,1.8-3.3巴)和4个超/纳米过滤有机膜(0.2-4.0kDa,5-30巴)。微滤是除去不溶性固体的不溶性固体的第一步。通过与酶液化偶联,渗透通量JP升高2,β-萘锡的保留是有限的。然后使用超/纳滤液来溶质分离。可以通过改变膜/压力组合来调节溶质的保留,所述膜/压力组合有利于所有溶质的浓度或相对于β-苯胺的纯化相对于总干物质的纯化。保留单个甜菜碱可能有点不同,也可以进行分级。使用简单模型进行模拟,以评估浓缩,纯化和分馏β含有渗碳步骤的过程的兴趣。

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