The Study of Hydrodynamics of Slug Flow in 10 Degrees Inclined Pipe Using Electrical Capacitance Tomography Data
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Slug flow along slightly inclined horizontal pipes is a major problem in gas-liquid transportation, it is very pronounced in chemical, oil and gas processing industries.
In reality, there is no absolute horizontal pipe due to the undulating nature/ Topography of the laid pipe terrains.
Very little research has been done in this area because of lack of experimental data. This work is proposed to use raw experimental data from 10 degrees inclined horizontal pipe to analyze the flow properties and pattern.
The experimental data obtained will be analyzed in order to improve the fundamental understanding of the flow regime promoted through them.
The following parameters concerned with slug flow in a slightly inclined horizontal pipe: void fraction in the liquid slug, void fraction in the Taylor bubble, translational velocity, slug frequency, length of liquid slug and Taylor bubble will be determined using processed data obtained from Electrical Capacitance Tomography (ECT).
Multiphase flows are of great interest to a large variety of industries. The power generation, nuclear reactor technology, food production, chemical process, petroleum, aerospace and automotive industries are all driving forces in this complex field.
This work is concerned only with gas-liquid flows in inclined pipes with particular interest towards oil and gas industry applications.
The mixtures of two fluids in pipes are frequently encountered. Flow instabilities may cause the mixture to arrange itself into different geometric configurations. These geometric configurations are usually referred to as flow patterns or regimes.
A little reflection will show that the orientation of the pipe makes a difference in the flow regime because of the role played by gravity and the density difference between the two fluids.
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