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FILTRATION AND DRYING STUDY OF ALCOHOL EXTRACT OF DE-OILED SOY-LECITHIN

机译:脱油大豆卵磷脂醇提取物的过滤及干燥研究

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De-oiled soy lecithin is divided in to two major parts i.e.alcohol soluble phosphatidylcholine (PC) fraction and alcohol insoluble phosphatidylinositol (PI) fraction.Both the fractions are highly desired for their variety of applications in fields such as medicine, cosmetics and food applications.Separation and purification of PC and PI fractions to their utmost purity is still a challenge to industries for the reason of its source and molecular and structural complexity. The present study deals with the filtration of the PI rich fraction followed by drying of the cake for its further purification and value addition. The filtration of PI rich fraction was carried out under constant pressure conditions followed by the cake drying in a vacuum tray dryer. The average specific cake resistance (αav) as a function of operating pressure was studied and it showed little variation with respect to the applied pressure differential. The initial solvent content in the cake after filtration was approx.1kg solvent kg dry solid-1 which was subsequently reduced to 0.04 kg solvent/kg dry solid. The drying kinetics of the cake in vacuum tray dryer was studied at different drying temperatures with constant as well as variable vacuum. The drying rate curve showed prominently the falling rate period with the effective solvent diffusivity in the range of 5.4×10-10 m2s-1 to 1.18×10-9 m2s-1 within the temperature range of 40oC to 60oC. The temperature dependence of the effective solvent diffusivity was described by an Arrhenius type relationship and the activation energy was found to be 39.28 kJmol-1.
机译:将脱油大豆卵磷脂分为两种主要部分Ieal醇可溶性磷脂酰胆碱(PC)级分和醇不溶性磷脂酰肌醇(PI)馏分。在药物,化妆品和食品应用等各种应用中,馏分非常需要馏分。对PC和PI分数的分析和纯化至最大的纯度对工业仍然是其来源和分子和结构性复杂性的挑战。本研究涉及过滤PI富含部分,然后干燥滤饼,以进一步纯化和增值。在恒定的压力条件下进行Pi富分裂的过滤,然后在真空托盘干燥器中干燥。研究了作为操作压力函数的平均特异性滤饼电阻(αAv),并且它对施加的压差略微变化。过滤后滤饼中的初始溶剂含量约为1Kg溶剂kg干燥固体-1,随后将其还原为0.04kg溶剂/ kg干燥固体。在不同的干燥温度下,在不同的干燥温度下,在不同的干燥温度和可变真空中研究了真空托盘干燥器中的干燥动力学。干燥速率曲线占据突出的下降速率,其有效溶剂扩散率在5.4×10-10m2s-1至1.18×10-9m2s-1的范围内,温度范围为40℃至60℃。有效溶剂扩散率的温度依赖性由Arrhenius型关系描述,并且发现活化能量为39.28kJmol-1。

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