Transient flows associated with the water hammer phenomenon are commonly encountered in both natural and engineering systems, such as hydraulic systems, oil transportation systems, and human arterial network. Sudden changes in pressurized pipe flow conditions caused by valve closure, pump operation, etc. are routine events. The excitations arising from these transient events can cause significant pressures leading to devastating forces [1].The flow of non-Newtonian fluids and slurries in pipes occurs in a wide range of practical applications in the processing industries and many natural systems. If the fluid has a significant yield stress, or if its effective viscosity is high, industrially relevant flow rates may occur in the laminar flow regime.The fluids under consideration in this study are shear-thinning non-Newtonian, whose rheology is described by a generalized Newtonian fluid (GNF) model, i.e. the dependency of isotropic viscosity on flow properties [2] and [3]. In the specific fluids of the present work, the viscosity can be described using either the power law or Cross models. The capability of these models has been investigated by several researchers, including such as Pinho and Whitelaw Herein, unsteady pipe flow of a non-Newtonian fluid is studied. This work may be seen as a new extension to the classic water hammer model in which transients of a Newtonian fluid contained in a straight elastic pipe supported at the valve and along the pipeline with sufficient longitudinal anchors to suppress fluid-structure interaction effects is investigated. Having done this fluid hammer simulation for the power law and Cross models, several alternate works (in terms of studying the other effects [15]) on the transients of these fluids can be offered for future research. They include viscosity
Investigation of Non-Newtonian Fluid Effects during Transient Flows in a Pipeline