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The droplet number moments approach to spray modelling: The development of heat and mass transfer sub-models

机译:液滴数矩的喷雾建模方法:传热传质子模型的发展

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In the past most poly-disperse spray models have been based on either discretising the liquid flow field into groups of equally sized droplets, as in the discrete droplet model (DDM) in which parcels of drops are tracked in space in a Lagrangian framework, or by solving separate Eulerian conservation equations for a number of size ranges. Both of these approaches can result in very long computing times, although the DDM is generally regarded as being superior in this respect under most conditions of interest. Recently an alternative approach to the modelling of sprays has been developed by Beck [Ph.D. Thesis, UMIST, 2000] and Beck and Watkins [Proc. R. Soc. Lond. A, 2003]. In this approach the size information concerning the spray is obtained by solving conservation and transport equations for two moments of the drop number distribution, and their respective mean velocities, and obtaining two other moments from an assumed size distribution function. The sub-models required in this approach, for hydro-dynamic phenomena in sprays, such as drop drag, break-up and collisions, have been presented elsewhere [Beck, Ph.D. Thesis, UMIST, 2000; Beck and Watkins, J. Comp. Phys., 2002]. The purpose of this paper is to present those sub-models relating to the mass and heat transfer processes in sprays. As part of this, an equation for the energy of the liquid phase is required. Standard gas phase equations, including a k-e turbulence model, are also solved. All the equations are solved in a Eulerian framework using the finite-volume approach. The inter-phase heat and mass transfers are captured through the use of source terms, and all the source terms for these aspects of the spray model are derived in this paper in terms of the four moments of the droplet number distribution in order to find the net effect on the whole spray flow field. The model has been applied to a wide variety of different sprays, including high-pressure diesel sprays, wide-angle solid cone water sprays, hollow cone sprays and evaporating sprays [Beck, Ph.D. Thesis, UMIST, 2000]. The comparisons of the results with experimental data show that the model generally performs well. In this paper the evaporation effects are examined and compared with experimental data wherever possible. Again this aspect of the spray model is shown to be generally successful.
机译:过去,大多数多分散喷雾模型都是基于将液体流场离散成大小相等的液滴组,例如在离散液滴模型(DDM)中,在拉格朗日框架中跟踪液滴的空间,或者通过求解多个尺寸范围的独立欧拉守恒方程。这两种方法都可能导致很长的计算时间,尽管在大多数情况下,DDM在这方面通常被认为是优越的。最近,Beck [Ph.D.Am.Chem.Soc。,Vol.26,pp.2,2,3,3,5,6,5,6,7,8,8,8,8,8,8,8,8,8,9,8,9,8,9都中都提出了一种替代的喷雾建模方法。 Thesis,UMIST,2000]和Beck and Watkins [Proc。 R. Soc。 nd A,2003]。在这种方法中,通过求解液滴数分布的两个矩及其各自的平均速度的守恒和输运方程式,并从假定的尺寸分布函数中获得另外两个矩,从而获得与喷雾有关的尺寸信息。这种方法所需的子模型,用于喷雾中的水动力现象,例如液滴阻力,破裂和碰撞,已在其他地方提出[Beck,Ph.D.论文,UMIST,2000;贝克和沃特金斯,J。Comp。物理,2002]。本文的目的是介绍与喷雾中的传质和传热过程有关的那些子模型。作为其一部分,需要用于液相能量的方程式。还解决了包括k-e湍流模型在内的标准气相方程。所有方程均使用有限体积方法在欧拉框架中求解。通过使用源项捕获相间的传热和传质,本文根据液滴数分布的四个矩导出了喷雾模型这些方面的所有源项,以便找到对整个喷雾流场的净影响。该模型已应用于多种不同的喷雾器,包括高压柴油喷雾器,广角实心锥形水喷雾器,空心锥形喷雾器和蒸发喷雾器[Beck,Ph.D.。论文,UMIST,2000年]。结果与实验数据的比较表明,该模型总体上表现良好。在本文中,将对蒸发效果进行检查,并尽可能与实验数据进行比较。再次表明,喷雾模型的这一方面通常是成功的。

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