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Modeling mass transfer in volatile organic compounds separation by pervaporation (PV) and application of PV in blueberry aroma recovery.

机译:模拟通过全蒸发(PV)分离挥发性有机化合物中的传质以及将PV用于蓝莓香气回收中。

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摘要

Concentration polarization is a detrimental phenomenon in pervaporation (PV) operation that decreases mass transfer in upside stream near the membrane surface thus significantly reducing achievable separation efficiency. A numerical model was developed to describe pervaporative mass transfer in a slit membrane module used for removal of volatile organic compound. Computational Fluid Dynamics (CFD) program was employed to solve hydrodynamics and mass transfer equations. In order to validate the results from CFD analysis, grid independence of final predicted value was established in both local and universal scale. The modeling approach was further validated by re-examining a classical diffusion problem for which there was a known solution. Numerical modeling predicted mass transfer coefficient of 0.76–1.85 × 10−5 m/s for laminar flow with Re between about 450–1800. This prediction was higher than that predicted by semi-empirical correlation, which could be explained by the module geometry used in modeling and follow-up experiments. After modeling normal PV module, efforts were taken in modeling the effect of baffle in enhancing mass transfer. Different types of baffle structure, including single baffle of three different heights and two baffles with changing distance between each other, were chosen for modeling.; Experiments were conducted using polydimethylsiloxane (PDMS) membrane installed on a bench-scale PV unit. Experimental result using 1,1,1-trichloroethane as solute showed very good agreement with modeling result in the low end of laminar flow while an increasing discrepancy was observed at the high end of laminar flow. As an example of applying PV in extracting aroma compounds during aroma stripping or from processing side streams, model solution containing aroma compound such as ethyl acetate, trans-2-hexenal, 1-hexanol, 1-heptanol, limonene, linalool, representing typical aroma compounds in blueberry was used for feed solution. The results confirmed technical capability of PV in aroma separation.; The established model provides better understanding of the concentration polarization existing in PV operation. The modeling result related to the effect of baffle(s) can be used for optimization of module design to enhance separation of target organic compound. This approach in analyzing concentration polarization in flat module can be extended to tubular and spiral wound module.
机译:浓差极化是全蒸发(PV)操作中的有害现象,该现象会减少膜表面附近的上行流中的传质,从而显着降低可实现的分离效率。建立了一个数值模型来描述用于去除挥发性有机化合物的狭缝膜组件中的全蒸发传质。计算流体动力学(CFD)程序用于求解流体力学和传质方程。为了验证CFD分析的结果,在局部和通用尺度上都建立了最终预测值的网格独立性。通过重新检查存在已知解决方案的经典扩散问题,进一步验证了建模方法的有效性。数值模型预测层流的传质系数为0.76-1.85×10 -5 m / s,Re在450-1800之间。该预测高于半经验相关的预测,这可以通过建模和后续实验中使用的模块几何来解释。在对正常的光伏组件进行建模之后,便开始对挡板在增强传质方面的效果进行建模。选择不同类型的挡板结构,包括三个不同高度的单个挡板和两个彼此变化距离的挡板,以进行建模。使用安装在台式PV装置上的聚二甲基硅氧烷(PDMS)膜进行了实验。以1,1,1-三氯乙烷为溶质的实验结果与层流低端模拟结果非常吻合,而层流高端则差异增大。作为在香气剥离过程中或从加工副物流中提取香气化合物中应用PV的示例,包含香气化合物(例如乙酸乙酯,反式-2-己醛,1-己醇,1-庚醇,li烯,芳樟醇)的模型溶液代表了典型的香气。蓝莓中的化合物被用作饲料溶液。结果证实了PV在香气分离中的技术能力。建立的模型可以更好地了解光伏运行中存在的浓度极化。与挡板效应有关的建模结果可用于优化模块设计,以增强目标有机化合物的分离。这种分析扁平组件中浓度极化的方法可以扩展到管状和螺旋缠绕组件。

著录项

  • 作者

    Peng, Ming.;

  • 作者单位

    Rutgers The State University of New Jersey - New Brunswick.;

  • 授予单位 Rutgers The State University of New Jersey - New Brunswick.;
  • 学科 Agriculture Food Science and Technology.
  • 学位 Ph.D.
  • 年度 2004
  • 页码 161 p.
  • 总页数 161
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 农产品收获、加工及贮藏;
  • 关键词

  • 入库时间 2022-08-17 11:44:01

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