tabelka 2

tabelka 2



0.004

0.003

0.002

350

T = at/r2


(a) Centerline temperaturę (from M. P. Heisler)


0 =


T-Tx

Ta-Ta

Bi hr

(b) Temperaturę distribution (from M. P. Heisler)


10"5 10-4 10-3 10-2

10-1 1 Bi2x = h2at/k2

10

102

103


104


(c) Heat transfer (from H. Grdber et al.)

Transient temperaturę and heat transfer charts for a long cylinder of radius r0 initially at a uniform temperaturę T( subjected to convection from all sides to an environment at temperaturę with a convection coefficient of h.


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