sm6_9

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PROBLEM 6.9 KNOWN: Variation of local convection coefficient with distance x from a heated plate with a uniform temperature T s . FIND: (a) An expression for the average coefficient 12 h for the section of length (x 2 - x 1 ) in terms of C, x 1 and x 2 , and (b) An expression for 12 h in terms of x 1 and x 2 , and the average coefficients 1 h and 2 h , corresponding to lengths x 1 and x 2 , respectively. SCHEMATIC: h x = Cx -1/2 dqASSUMPTIONS: (1) Laminar flow over a plate with uniform surface temperature, T s , and (2) Spatial variation of local coefficient is of the form 1/2 x h Cx = , where C is a constant. ANALYSIS: (a) The heat transfer rate per unit width from a longitudinal section, x 2 - x 1 , can be expressed as ( )( 12 12 2 1 s q h x x T T ) = (1) where 12 h is the average coefficient for the section of length (x 2 - x 1 ). The heat rate can also be written in terms of the local coefficient, Eq. (6.11), as (2) ( ) ( ) 2 1 1 x x 12 x s s x x q h dx T T T T h = = 2 x dx Combining Eq. (1) and (2), ( ) 2 1 x 12 x x 2 1 1 h x x = h dx (3) and substituting for the form of the local coefficient, 1/2 x h Cx = , find that ( ) 2 2 1 1 x 1/2 1/2 1/2 x 1/2 2 1 12 x 2 1 2 1 2 1 x x x 1 C x h Cx dx 2C x x x x 1/2 x x = = = (4)< (b) The heat rate, given as Eq. (1), can also be expressed as ( ) ( ) 12 2 2 s 11 s q hx T T hx T T = (5) which is the difference between the heat rate for the plate over the section (0 - x 2 ) and over the section (0 - x 1 ). Combining Eqs. (1) and (5), find, 2 2 11 12 2 1 hx hx h x x = (6)< COMMENTS: (1) Note that, from Eq. 6.6, x x 1/2 1/2 x x 0 0 1 1 h h dx Cx dx 2Cx x x = = = (7) or x h = 2h x . Substituting Eq. (7) into Eq. (6), see that the result is the same as Eq. (4).

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  • PROBLEM 6.9 KNOWN: Variation of local convection coefficient with distance x from a heated plate with a uniform temperature Ts. FIND: (a) An expression for the average coefficient 12h for the section of length (x2 - x1) in terms of C, x1 and x2, and (b) An expression for 12h in terms of x1 and x2, and the average coefficients 1h and

    2h , corresponding to lengths x1 and x2, respectively. SCHEMATIC:

    hx = Cx-1/2dq

    ASSUMPTIONS: (1) Laminar flow over a plate with uniform surface temperature, Ts, and (2) Spatial

    variation of local coefficient is of the form 1/ 2xh Cx= , where C is a constant.

    ANALYSIS: (a) The heat transfer rate per unit width from a longitudinal section, x2 - x1, can be expressed as ( )(12 12 2 1 sq h x x T T ) = (1) where 12h is the average coefficient for the section of length (x2 - x1). The heat rate can also be written in terms of the local coefficient, Eq. (6.11), as

    (2) ( ) ( )21 1

    x x12 x s s xx

    q h dx T T T T h = = 2x dxCombining Eq. (1) and (2),

    ( ) 21x

    12 xx2 1

    1hx x

    = h dx (3) and substituting for the form of the local coefficient, 1/ 2xh Cx

    = , find that

    ( )2

    21

    1

    x 1/ 2 1/ 21/ 2x 1/ 2 2 112 x2 1 2 1 2 1x

    x x1 C xh Cx dx 2Cx x x x 1/ 2 x x

    = = = (4)< (b) The heat rate, given as Eq. (1), can also be expressed as ( ) ( )12 2 2 s 1 1 sq h x T T h x T T = (5) which is the difference between the heat rate for the plate over the section (0 - x2) and over the section (0 - x1). Combining Eqs. (1) and (5), find,

    2 2 1 1122 1

    h x h xhx x

    = (6)< COMMENTS: (1) Note that, from Eq. 6.6,

    x x 1/ 2 1/ 2

    x x0 01 1h h dx Cx dx 2Cxx x

    = = = (7) or xh = 2hx. Substituting Eq. (7) into Eq. (6), see that the result is the same as Eq. (4).

    Nancy ProyectText BoxExcerpts from this work may be reproduced by instructors for distribution on a not-for-profit basis for testing or instructional purposes only to students enrolled in courses for which the textbook has been adopted. Any other reproduction or translation of this work beyond that permitted by Sections 107 or 108 of the 1976 United States Copyright Act without the permission of the copyright owner is unlawful.