首页> 外文会议>ASME Fluids Engineering Division summer meeting;FEDSM'97 >TWO FLUID MODEL FOR TWO-PHASE TURBULENT JETS
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TWO FLUID MODEL FOR TWO-PHASE TURBULENT JETS

机译:两相湍流的两种流体模型

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An Eulerian multidimensional model for a cylindricaltwo-phase dispersed particle jet is proposed and compared withexperimental data. The averaged equations of mass andmomentum are solved for each phase and the turbulent kineticenergy equation is solved for the continuous phase.The phase distribution is controlled by the interfacialforces and the Reynolds stress gradient. The two fluid modelaveraging procedure developed by Reeks (1992) results in aturbulent diffusion force. This force is constituted for the caseof homogeneous turbulent flow. Furthermore, it is proposedthat the eddies interact primarily with those particles that aresmaller than them, i.e., only bigger eddies can trap particles anddeflect their path. The constitutive relations for the turbulentkinetic energy of the continuous phase consists of a k-ε modelwhich has been modified for two-phase flows.Once the constitutive relations have been defined, thetwo-fluid model is implemented in a computational fluiddynamics code. The results are compared against experimentaldata for an air jet with 39 μm glass particles. Because thefluid flow around these particles is well understood, theyrepresent a good starting point for the development of a twophaseturbulence model. The particles are assumed to follow adrag law consistent with Oseen’s equation. Furthermore, theseparticles have very small turbulent wakes so they producenegligible additional turbulence. Their effect on turbulencemodulation is primarily dissipative due to viscous shear in theflow field around them.In the vicinity of the jet source the time constant of theglass particles is significantly larger than the time constant ofthe turbulent eddies. Therefore, the trajectories of the particlesare quite different from those eddies and the turbulent diffusionforce may be validated at conditions where the classicalgradient-diffusion approximation is not very good. It has beenshown that the present model is equivalent to Taylor’s gradientdiffusionequation when the particle-gas flow approachesturbulent equilibrium.Good agreement between the model and the data isobtained. The sensitivity of the results to the turbulence timeconstant definition is discussed. Furthermore, the effect ofturbulence anisotropy is also considered.
机译:提出了圆柱状两相分散粒子射流的欧拉多维模型,并与实验数据进行了比较。求解每个相的平均质量和动量方程,求解连续相的湍动能方程。相分布受界面力和雷诺应力梯度控制。 Reeks(1992)开发的两种流体模型平均程序导致了饱和扩散力。对于均匀的湍流,该力是构成的。此外,提出涡流主要与小于它们的那些粒子相互作用,即,只有较大的涡流才能捕获粒子并偏转它们的路径。连续相湍动能的本构关系由一个k-ε模型组成,该模型已针对两相流进行了修改。一旦定义了本构关系,就可以在计算流体力学代码中实现双流体模型。将结果与带有39μm玻璃颗粒的空气喷嘴的实验数据进行比较。由于围绕这些粒子的流体流动已被很好地理解,因此它们代表了开发两相湍流模型的良好起点。假定这些粒子遵循与Oseen方程一致的adrag定律。此外,这些颗粒的湍流很小,因此它们产生的附加湍流可以忽略不计。它们对湍流调制的影响主要是由于它们周围的流场中的粘性剪切而消散的。在射流源附近,玻璃颗粒的时间常数明显大于湍流涡流的时间常数。因此,粒子的轨迹与那些涡旋完全不同,并且可以在经典梯度扩散近似不是很好的条件下验证湍流扩散力。结果表明,当颗粒气流达到湍流平衡时,该模型等效于泰勒梯度扩散方程。该模型与数据具有良好的一致性。讨论了结果对湍流时间常数定义的敏感性。此外,还考虑了湍流各向异性的影响。

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