共查询到18条相似文献,搜索用时 171 毫秒
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多孔介质喷雾干燥过程的热质传递 总被引:1,自引:0,他引:1
多孔介质是大量干燥过程的主体,由于实际多孔介质干燥过程的复杂性,建立通用的干燥过程传热传质模型十分困难。本文通过分析喷雾干燥过程中高初始含湿多孔介质与干燥介质之间的传热传质机理以及各因素对传热传质的影响,根据马歇尔方程探讨了干燥介质与料雾之间的水蒸汽分压差在干燥过程中的变化情况,反映了多孔湿介质在喷雾干燥操作中的传热传质过程的几种特性,为确定实际生产中喷雾干燥器的操作奈件指明了新的出路。 相似文献
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物料干燥过程—传质传热最优化方法的研究 总被引:1,自引:0,他引:1
论述了多孔介质干燥过程中传质传热的数学模型及干燥过程最优化准则的建立;并且动用控制理论产物料干燥过程传热的动态优化方法--准则约束法,且得到了最优解。 相似文献
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喷雾干燥热风分布器的设计原则 总被引:1,自引:0,他引:1
喷雾干燥装置中的热风分布器与干燥的传热传质密切相关。指出,干燥的传热传质系数与Re数有关并呈0.8次方关系。文中列出了工业中常见的三种不正确的分布形式,并提出三条设计热风分布器的原则。 相似文献
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含湿多孔介质的干燥特性 总被引:2,自引:0,他引:2
基于含湿多孔介质的水分蒸发过程及其内部毛细管水分的蒸发特性,分析了含湿多孔介质在干燥过程中发生体积收缩的原因.讨论了多孔介质的物性和外部干燥条件对其体积收缩特性的影响。 相似文献
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Drying Research and Development in China 总被引:1,自引:0,他引:1
The developments in fundamental research on drying, drying technology, dryer manufacture from 1995 to 2001 in China were reviewed. The progress and current situation in drying fundamental research in China, such as heat and mass transfer in wet porous media, non-Fick and non-Fourier effects on rapid transient heat and mass transfer during drying, numerical simulations of a drying process and so on, were reviewed. The states of manufacturing of various dryers in China were investigated. Some studies on novel drying processes, such as pulse combustion drying, biomaterial drying, electro-dewatering technique etc., were also presented. 相似文献
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Through-air drying is commonly used in the drying of high-quality tissue and towel products. A representative elementary volume method was used to model the fluid flow and heat and mass transfer during through drying in heterogeneous porous biobased materials such as tissue and towel products. Results of flow both upstream and downstream of a modeled porous sheet allowed visualization of the effects of mixing at the top and bottom of the porous medium. The effect of initial nonuniformity on fluid flow and convective heat and mass transfer in heterogeneous porous media was studied. The effect of material nonhomogeneity and associated transport properties on moisture content of the porous material as a function of drying time was studied. Modeling results indicate that for the first time it is possible to simulate the effect of nonuniformity on fluid flow and convective heat and mass transfer in porous media during through-air drying of paper. Moisture and structural nonuniformity contributing to nonuniformity in air flow might contribute significantly to drying nonuniformity. Depending on the moisture regimes and degree of saturation of the convective medium, heat and mass transfer coefficients may have varying effects on the overall drying. 相似文献
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This paper mainly focuses on cross-effect of heat and mass transfer of capillary porous media which A.B.Luikov set up on irreversible thermodynamics principle. On the basis of perfecting the equations of heat and mass transfer, the heat and mass transfer parameters are determined during drying processes, and thermal gradient coefficient δ and moisture gradient coefficient ξ are obtained which show the cross-effect of heat and mass transfer. Thus the fundamentals are provided for quantitative analysis of cross-effect of heat and mass transfer. The convective drying mathematical model under the first unsteady boundary condition is therefore proposed. By the application of Henry transform, the theoretical solution of unsteady drying process is given and its validity is verified 相似文献
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Abstract This paper mainly focuses on cross-effect of heat and mass transfer of capillary porous media which A.B.Luikov set up on irreversible thermodynamics principle. On the basis of perfecting the equations of heat and mass transfer, the heat and mass transfer parameters are determined during drying processes, and thermal gradient coefficient δ and moisture gradient coefficient ξ are obtained which show the cross-effect of heat and mass transfer. Thus the fundamentals are provided for quantitative analysis of cross-effect of heat and mass transfer. The convective drying mathematical model under the first unsteady boundary condition is therefore proposed. By the application of Henry transform, the theoretical solution of unsteady drying process is given and its validity is verified 相似文献
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《Drying Technology》2012,30(15):1742-1749
The drying of plant materials with cellular tissue is often viewed as drying of porous media that is assumed to consist of cell cytoskeleton and intercellular space. Various approaches have been reported in the literature to describe heat and mass transfer during drying of such porous materials. However, the fact remains that the water in a cellular tissue is mostly intracellular and it should be driven out of the cells across cell membranes before transporting in cell gaps, as in a general porous media. In the present study, the transport process of moisture in a cellular tissue was analyzed. A mathematical model for moisture transport across the cell membrane was established, which was correlated to a self-developed, dual-scale pore network model (cell and pore network) for drying of plant materials. The relationship between mass volumetric flux and average intracellular moisture content was developed based on the microscopic images and the drying experiments. 相似文献
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多孔介质内部热质传递的等效耦合扩散模型的推导及其应用 总被引:1,自引:2,他引:1
基于Whitaker的体积平均方程,在不附加任何新的假设的基础上,对多孔介质内部热质传递的等效耦合扩散模型进行推导,得出了多孔介质内部热质传递的等效耦合扩散模型。并应用该模型对瓷质砖体干燥过程进行了数值模拟,模拟结果与实验结果十分吻合。 相似文献
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Multiscale and multilayer structural modeling and simulation on drying of grain packing porous media
Yuejin Yuan Libin Tan Zhe Zhao Yingying Xu Yu Zhao Yueding Yuan 《Drying Technology》2016,34(14):1664-1676
ABSTRACTAiming at the problem of multilayer physical structure for the skeleton of porous media, a multiscale and multilayer structural model of heat and mass transfer processes for drying of grain packing porous media was established by applying the pore network method and multiscale theory. An experimental study on rice drying was conducted in order to validate this model. The simulation and experimental results indicated that the established model could explain the mechanical properties of rice drying well. The rate of heat transfer was faster than the rate of mass transfer and there was a higher moisture gradient inside the rice grain. The diffusion coefficient of rice embryo played an important role in the drying process, and whose effect on drying was larger than the diffusion coefficient of rice hull and chaff. The moisture was imprisoned effectively inside the rice when the diffusion coefficient of rice embryo was very small. 相似文献
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基于局部质量非平衡假设,建立了多相多孔介质热、质耦合传递数学模型,理论验证具有预制孔隙的初始非饱和多孔物料对冷冻干燥过程的强化作用。模型考虑了多孔介质的吸湿效应,构建了3种吸附-解吸平衡关系。模型使用基于有限元法的COMSOL Multiphysics软件平台数值求解,并与实验数据进行了比较。结果表明,初始非饱和冷冻物料能够有效地强化冷冻干燥过程。采用不同函数形式的吸附-解吸平衡关系模拟的干燥曲线均与实验数据非常吻合。通过分析物料内部的饱和度、温度和质量源分布,探讨了初始非饱和物料冷冻干燥过程的传热传质机理。初始非饱和物料的干燥速率控制因素主要是传热。模拟考察环境辐射温度对冷冻干燥过程影响的结果表明,所建模型具有良好的预测能力。 相似文献