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Published bySharon Robertson Modified over 8 years ago
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Lesson 13 CONVECTION HEAT TRANSFER Given the formula for heat transfer and the operating conditions of the system, CALCULATE the rate of heat transfer by convection.
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Convection Heat transfer by the motion and mixing of the molecules of a liquid or gas Natural convection is used if this motion and mixing is caused by density variations resulting from temperature differences within the fluid. Affected by: – Fluid velocity – Fluid viscosity – Heat flux – Surface roughness – Type of flow (single-phase/two-phase)
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Convection
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The convective heat transfer coefficient (h) is dependent upon the physical properties of the fluid and the physical situation. Laminar flow – relatively low h Turbulent flow – higher h stagnant fluid film layer is thinner on the heat transfer surface. Values of h have been measured and tabulated for the commonly encountered fluids and flow situations occurring during heat transfer by convection.
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Heat Transfer Coefficient Heat transfer processes encountered in nuclear facilities involve a combination of both conduction and convection. For a heat exchanger, there are two values for h. – Convective heat transfer coefficient (h) for the fluid film inside the tubes – Convective heat transfer coefficient for the fluid film outside the tubes. Thermal conductivity (k) and thickness (Δ x ) of the tube wall must also be accounted for. U o - Overall heat transfer coefficient Total rate of heat transfer (Q) must be related to the cross- sectional area for heat transfer (Ao) and the overall heat transfer coefficient (Uo).
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Overall Heat Transfer Coefficient
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Combined Heat Transfer
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Three processes - – Heat transfer by convection between temperatures T1 and T2; – Heat transfer by conduction between temperatures T2 and T3 – Heat transfer occurs by convection between T3 and T4. Each has an associated heat transfer coefficient, cross-sectional area for heat transfer, and temperature difference.
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Overall heat transfer coefficient in cylindrical geometry Where : Δr = r o – r in k = Thermal conductivity coefficient of the tube wall h 1 = Convective heat transfer coefficient inside tube h 2 = Convective heat transfer coefficient outside the tube
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Summary
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