Tab. 7 Berechnungsergebnisse zum Verdampferrohr (Beispiel 3)
\( \dot{x} \) | 0 | 0,1 | 0,2 | 0,3 | 0,4 | 0,5 | 1 |
---|---|---|---|---|---|---|---|
z/m | 0 | 2,12 | 4,23 | 6,35 | 8,47 | 10,59 | 21,17 |
αLO/W/m2 K | 12.176 | 12.176 | 12.176 | 12.176 | 12.176 | 12.176 | 12.176 |
αGO/W/m2 K | 12.270 | 12.270 | 12.270 | 12.270 | 12.270 | 12.270 | 12.270 |
\( \frac{\alpha {(z)}_{\mathrm{k}}}{\alpha_{\mathrm{LO}}} \) | 1 | 1,896 | 2,110 | 2,235 | 2,313 | 2,363 | 1,008 |
α(z)k/W/m2 K | 12 176 | 23.079 | 25.694 | 27.209 | 28.168 | 28.768 | 12.270 |
ψ | 1 | 0,825 | 0,825 | 0,825 | 0,825 | 0,825 | – |
α(z)B/W/m2 K | 75.163 | 58.335 | 55.456 | 52.577 | 49.698 | 49.385 | – |
α(z)/W/m2 K | 75.270 | 59.515 | 57.237 | 54.902 | 52.548 | 52.446 | 12.270 |
ΔT/K | 2,66 | 3,36 | 3,49 | 3,64 | 3,81 | 3,81 | 16,3 |