Hello, I am a mechanical engineering student and want to upload this question as I have an exam in early June about thermodynamics. I have been given a question that will help me answer my exams in June. Please could you answer showing step by step guidance on how to answer this question with the formula clearly shown. Thank you very much 2. Figure 2 shows the heat transfer rate per unit width (normal to the page) from alongitudinal section, x₂ - x₁, can be expressed as q12 = h₁2(x2 − x₁)(Ts - Too),where h₁2 is the average coefficient for the section of length (x₂-x₁). Considerlaminar flow over a flat plate with a uniform temperature T. The spatial variation ofthe local convection coefficient is of the form hx = Cx², where C is a constToo, Uco111TSKLX912X1Ix2IX1dqdxIX2Fig.2. A heat transfer of a longitudinal plate(a) Beginning with the convection rate equation in the form dq' =h_dx(T, -T),derive an expression for h₁2 in terms of C, x₁, andx₂.(b) Derive an expression for h₁2 in terms of x₁, x2, and the average coefficients h₁ andh₂, corresponding to lengths x₁, andx₂., respectively.

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Answered: Figure.2 shows the heat transfer rate…

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

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Hello, I am a mechanical engineering student and want to upload this question as I have an exam in early June about thermodynamics. I have been given a question that will help me answer my exams in June. Please could you answer showing step by step guidance on how to answer this question with the formula clearly shown.

Thank you very much

2. Figure 2 shows the heat transfer rate per unit width (normal to the page) from a
longitudinal section, x₂ - x₁, can be expressed as q12 = h₁2(x2 − x₁)(Ts - Too),
where h₁2 is the average coefficient for the section of length (x₂-x₁). Consider
laminar flow over a flat plate with a uniform temperature T. The spatial variation of
the local convection coefficient is of the form hx = Cx², where C is a const
Too, Uco
111
TSK
L
X
912
X1
I
x2
I
X1
dq
dx
I
X2
Fig.2. A heat transfer of a longitudinal plate
(a) Beginning with the convection rate equation in the form dq' =h_dx(T, -T),
derive an expression for h₁2 in terms of C, x₁, andx₂.
(b) Derive an expression for h₁2 in terms of x₁, x2, and the average coefficients h₁ and
h₂, corresponding to lengths x₁, andx₂., respectively.

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