مشروع البحث:
Newtonian and Non-Newtonian Two-Phase Flow in Complex Pipelines

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المساهمين
الممولين
رقم التعريف
251
الباحث
Faraj Ali Ben Rajeb
المشرفين
منشورات
وحدات تنظيمية
الوصف
Creating a new model to estimate void fraction for gas-non-Newtonian flow is another objective done in the present work. The void fraction is considered one of the most important flow parameters used to describe two-phase flows in tubes. Void fraction is an important process variable for the volume and mass calculation required to transport gas-liquid mixture in pipelines, storage in tanks, metering, and custody transfer. Furthermore, it is important to determine other flow parameters such as two-phase density and viscosity or the average velocities of gas and liquid mixture. In addition, it plays a significant role in estimating and modelling two-phase pressure drop and flow pattern transitions. The created void fraction model is used to determine constants of general form posted by Butterworth[2]. Both developed void fraction models give a good estimation for the void fraction with about 5% percent errors compared with our experimental results and other available literature experimental results.
الكلمات الدالة
Keywords: Newtonian, Non-Newtonian, Two-Phase Flow, Pressure Drop, Void Fraction, Flow Regime.