By using a specially designed probe mechanism which entered the system through the pipe outlet and which could be located quite accurately at any radial or longitudinal position in the pipe an extensive set of measurements was made of the temperature profiles in the heat-transfer entry section of an
Temperature profiles for turbulent flow of air in a pipe I. The fully developed heat transfer region
β Scribed by W. Squire
- Publisher
- Elsevier Science
- Year
- 1964
- Tongue
- English
- Weight
- 156 KB
- Volume
- 19
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
β¦ 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
π SIMILAR VOLUMES
FIG. 1. Temperature deficiency relationship too far in predicting a temperature defect which increases acknowledge financial support from National Science Founless rapidly than a parabola. The experimental data shows dation Grant G 24354. that even if the temperature defect is flatter than the veloc