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Temperature profiles for turbulent flow of air in a pipe I. The fully developed heat transfer region

✍ Scribed by W. Squire


Publisher
Elsevier Science
Year
1964
Tongue
English
Weight
156 KB
Volume
19
Category
Article
ISSN
0009-2509

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✦ Synopsis


Letters to the Editor According to our procedure, the functional relation, mixing condition and objective function are rewritten as x1.1 = fib,o; Wl) x1.0 = Q1Cl.f + Bx1.1; ct+p=1 x2.1 = x2.0 + -; (x1,1 -x1.0) -C(WI) xa,o = 0 For this case, equations (1) through (4) reduce to n z1.0 = Zl.1 afi(xl.0; Wl) + 2% mQ,o; wd _ 1 (6) ax1,o a axl,O I z&o = za.1 (7) z1.1 = 8Zl.O (8) zz.1 = 1 (9) The maximum condition, represented by equation (S), becomes ~~,~fi(~~.~; wl) + $~xI.o; WI) -x1.01 -&I) = max. CL (10)

If the maximum lies at the stationary place, equation ( 10) is equivalent to


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