ملخص البحث :
A hydrothermal performance of helical annular turbulent flow in a shell and tube heat
exchanger has been investigated numerically. The numerical investigation involves a three
dimension numerical solution of four models by a commercial package ANSYS FLUENT
16.0. The boundary conditions of all models that solved by the numerical solution was taken
as a constant temperature and constant heat flux for inner tube wall, while the outer wall of
shell side was insolation. The first model has a straight annular with air flow in annular
regime, while the second model has a straight annular with water flow in annular regime. The
third model has a twist annular with air flow in annular regime, while the fourth model has a
twist annular with water flow in annular regime. Different Reynolds number for the air and
water flow inside the annular regime of heat exchanger namely (500, 1000, 1500, 2000, 2500,
3000, 3500, 4000, 4500, 5000, 5500, and 6000) were used for each model. The results
indicated that the annular shape has significant effects on the hydrothermal performance; it
found enchainment in all results of twist annular compared with the results of the straight
annular, which included increasing in temperature difference of 9.1% and 24.2%, outlet
temperature of 3.2% and 5.8%, while the increasing in heat flux, Nuselts number, and heat
transfer coefficient of 11.2% and 31.3%, finally the increasing in pressure drop of 29% and
29.2% for air and water flow respectively. The results obtained from numerical solution
presented the static temperature contours and showed that the temperature distribution of twist
annular is better than straight annular. The present numerical results have been compared with
the available previous studied and give a good agreement
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سنة النشر : 2017
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تصنيف البحث : رسالة ماجستير
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