جستجوی مقالات مرتبط با کلیدواژه « yasuda model » در نشریات گروه « مکانیک »

In this paper, the non-Newtonian immiscible two-phase polymer flow in a petroleum reservoir has been investigated numerically. The fluid flow in a porous medium is simulated as a compressible flow. The Carreau-Yasuda constitutive equation is employed as the model of non-Newtonian fluid. The IMPES method is used for numerical simulation, in which the pressure equation is discretized and solved by an implicit approach and the saturation equation is solved by an explicit method. Results reveal that zero-shear rate viscosity has a high impact on the sweep efficiency of the reservoir and also controls the channeling and viscous fingering effects. In addition increasing the viscosity of non-Newtonian fluid improves cumulative oil production and diminishes the viscous fingering phenomenon caused by injected fluid. The relaxation time of Carreau-Yasuda fluid, which is the elastic characteristic of the non-Newtonian fluid, for low permeability values cannot influence flow characteristics inside the reservoir, however for higher permeability values its effect becomes more sensible. Increasing the injection rates leads to the increase of fluid production, while the injection rate has an optimum range to reach the optimum oil production. In addition, the effect of variation of the injected fluid properties on the polymer breakthrough time has been investigated and results presented.

In this paper، numerical solution of non-Newtonian fluid flow through a channel with a cavity is studied. Carreau-Yasuda non-Newtonian model which represent dependence of stress on shear rate well is used and the effect of n index of model on attribute of flow is considered. Governing equations are discretized using finite difference method on staggered mesh and the form of allocating flow parameters on staggered mesh is based on marker and cell method. For dependence between continuity and momentum equations، artificial compressibility method is used. Numerical results express that with decrease of n index، the developing length is increased and the velocity in center of channel and pressure drop of flow are decreased.

In this paper، the steady flow of non newtonian fluid in axisymmetric sudden expansion with ratio 1:3 solved numerically. Finite difference method is used to discrete the governing equation on the staggered mesh. The non-newtonian model that used is the Carreau Yasuda five constants viscometric model. Using this model، non newtonian properties of the fluid can be simulated well. The range of the power law index is considered between 0. 6 and 1. 0. The results of this paper include the streamline diagrams، the axial velocity، viscosity and stress profiles for different values of the non newtonian property. These results show that length of vortex and fully developing region decreases، the pressure loss and the maximum axial velocity increases when the power law index (n) is decreases. It is shown that the magnitude of the velocity and viscosity in the center of the vortex are minimum and maximum respectively.