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Transport Phenomena II Essentials
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REA’s Essentials provide quick and easy access to critical information in a variety of different fields, ranging from the most basic to the most advanced. As its name implies, these concise, comprehensive study guides summarize the essentials of the field covered. Essentials are helpful when preparing for exams, doing homework and will remain a lasting reference source for students, teachers, and professionals. Transport Phenomena II covers forced convention, temperature distribution, free convection, diffusitivity and the mechanism of mass transfer, convective mass transfer, concentration distribution in solids and in laminar flow, and the equation of change for multicomponent systems.
LanguageEnglish
PublisherResearch & Education Association
Release dateJan 1, 2013
ISBN9780738672472
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Book preview
Transport Phenomena II Essentials - The Editors of REA
CHAPTER 8
FORCED CONVECTION
8.1 DEFINITION
(1)
e9780738672472_i0002.jpg(2)
e9780738672472_i0003.jpg(3)
e9780738672472_i0004.jpg(4)
e9780738672472_i0005.jpg(5)
e9780738672472_i0006.jpg(6)
e9780738672472_i0007.jpg(7)
e9780738672472_i0008.jpg8.2 FLOW OVER A FLAT PLATE
8.2.1 LAMINAR FLOW
e9780738672472_i0009.jpgRestrictions:
(1) 0.6 ≤ Pr ≤ 50
(2) 100 < R < Re < Rex,c e9780738672472_img_8771.gif 5 × 10⁵
(3) Evaluate properties at tm
(4) Dissipation is neglected
e9780738672472_i0010.jpgRestrictions:
(1) Pr < 0.05
(2) Re < Rex,c e9780738672472_img_8771.gif 5 × 10⁵
(3) Evaluate properties at tm m
(4) Dissipation is neglected
8.2.2 TURBULENT FLOW
e9780738672472_i0011.jpgRestrictions:
(1) 0.6 ≤ Pr ≤ 60
(2) Properties at tm
(3) Dissipation is neglected
e9780738672472_i0012.jpgRestrictions:
(1) 0.6 ≤ Pr ≤ 60
(2) R = 5 × 10⁵ ex,c
(3) Evaluate properties at tm m
(4) Dissipation is neglected
(5) Obtain A from table 8.1
Table 8.1
8.3 FLOW INSIDE CYLINDRICAL PIPES AND TUBES
8.3.1 LAMINAR FLOW
e9780738672472_i0014.jpgRestrictions:
(1) Fully developed flow
(2) ReD < 2300
(3) Constant surface temperature, ts = constant
(4) Evaluate properties at tmb
(5) e9780738672472_i0015.jpg
e9780738672472_i0016.jpgRestrictions:
(1) 0.48 < Pr < 16,700
(2) Evaluate properties except µs at tmb
Evaluate µs at t s
(3) e9780738672472_i0017.jpg
8.3.2 TURBULENT FLOW
e9780738672472_i0018.jpgRestrictions:
(1) n = 0.4 for t > t
(2) n = 0.3 for ts < tb
(3) 0.7 < Pr < 160 10 ⁴
(4) |ts – tb| < 6°C for liquids |ts – tb| < 60°C for gases
(5) Evaluate properties at tb
(6) Fully developed flow
Effect of starting length is negligible
e9780738672472_i0019.jpg(7) ReD > 2300
e9780738672472_i0020.jpgRestrictions:
(1) 0.7 < Pr < 160
(2) 10⁴ < ReD < 10⁶
(3) Evaluate properties except µs at tb
Evaluate µs at ts
(4) Fully developed flow
(5) Effect of starting length is negligible e9780738672472_i0021.jpg
8.4 HEAT-TRANSFER COEFFICIENT FOR TRANSITION FLOW INSIDE A PIPE
Fig. 8.1
e9780738672472_i0022.jpgEnjoying the preview?
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