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首页> 外文期刊>Journal of food engineering >Phase equilibrium diagrams for the system water, inert and solutes from mate (Ilex paraguariensis) leaves at constant temperature and cyclic pressurization
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Phase equilibrium diagrams for the system water, inert and solutes from mate (Ilex paraguariensis) leaves at constant temperature and cyclic pressurization

机译:在恒温和循环加压下,来自伴侣(副瓜叶)叶子的系统水,惰性和溶质的系统相平衡图

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Experimental equilibrium curves for a three-component mixture of water, insoluble and soluble matter from dry leaves of mate at 17 degrees C, 32 degrees C and 47 degrees C were obtained. They were built from equilibrium data of solute mass fractions (on an inert-free basis) at solid to solvent mass ratios of 1.5:30, 3:30, 4.5:30 and 6:30. The equilibrium concentrations in the leached solution were tuned on a large set of kinetic data (>= 55) of solute in the liquid phase by involving a first-order solid liquid extraction model. The kinetic experiments of solute removal were carried out in an isothermal batch extractor under a frequency of pressurization of 1:600 cycles per second (300 s at 91.4 kPa + 300 s at 182.8 or 365.6 kPa per cycle) for 25,200 s. The equilibrium mass fractions of solute in the slurry were calculated by a mass balance for the mate solubles based on the known composition of the starting solid in terms of total solute and inert. A constant mass ratio of retained solvent to inert close to 4.2 was experimentally obtained by draining under gravity the bed of solids taken to leaching. The results are presented in McCabe-Thiele and Ponchon-Savarit diagrams, and revealed the significant influences of solid to solvent ratio and leaching temperature on solute equilibrium concentrations at a high probability level (p <= 0.05). The non-vertical tie lines in the rectangular diagram of Ponchon-Savarit evidenced that solute is adsorbed by the insoluble solid, which means that solute distributes unevenly between the liquid and solid phases at equilibrium (i.e.; y(Ae)not equal x(Ae)). (C) 2015 Published by Elsevier Ltd.
机译:获得了水的三组分混合物的实验平衡曲线,该水是来自交配的干叶的水,不溶物和可溶物在17摄氏度,32摄氏度和47摄氏度的条件下。它们是根据固溶质量比(在无惰性条件下)在固体与溶剂质量比为1.5:30、3:30、4.5:30和6:30的平衡数据建立的。通过涉及一阶固液萃取模型,可根据液相中的大量溶质动力学数据(> = 55)调整浸出溶液中的平衡浓度。溶质去除的动力学实验是在等温间歇式萃取器中进行的,其加压频率为每秒1:600个循环(91.4 kPa下为300 s + 182.8或365.6 kPa下为300 s /循环),持续25,200 s。淤浆中溶质的平衡质量分数是基于初始固溶体的已知组成(总溶质和惰性),通过配合物可溶物的质量平衡来计算的。通过在重力作用下沥干用于沥滤的固体床,通过实验获得了保留的溶剂与惰性物质的质量比接近4.2的恒定值。结果显示在McCabe-Thiele和Ponchon-Savarit图中,并且揭示了固溶比和浸出温度对溶质平衡浓度的显着影响(p <= 0.05)。 Ponchon-Savarit矩形图中的非垂直连接线表明溶质被不溶性固体吸附,这意味着溶质在液相和固相之间处于平衡状态(即y(Ae)不等于x(Ae ))。 (C)2015年由Elsevier Ltd.出版

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