Unterschiede
Hier werden die Unterschiede zwischen zwei Versionen angezeigt.
| Beide Seiten der vorigen RevisionVorhergehende ÜberarbeitungNächste Überarbeitung | Vorhergehende Überarbeitung | ||
| en:grundlagenhandbuch:zylinderwaermestroeme [2026/05/28 09:52] – deppe2 | en:grundlagenhandbuch:zylinderwaermestroeme [2026/05/28 09:53] (aktuell) – [Barrel Heat Flows] deppe2 | ||
|---|---|---|---|
| Zeile 89: | Zeile 89: | ||
| In this case, the twin bore is not replaced by a rectangular prism with the same surface but by a pipe with the same surface. | In this case, the twin bore is not replaced by a rectangular prism with the same surface but by a pipe with the same surface. | ||
| - | $$\frac{O_{Acht}}{O_{Rohr}} = 1$$ | + | $$\frac{O_{Acht}}{O_{Rohr}} = 1 \tag{13}$$ |
| Hence, the diameter of the pipe $r_i$ results. | Hence, the diameter of the pipe $r_i$ results. | ||
| - | $$r_i = -\frac{L_{cyl}}{2} + \sqrt{\left(\frac{L_{cyl}}{2}\right)^2 + U}$$ | + | $$r_i = -\frac{L_{cyl}}{2} + \sqrt{\left(\frac{L_{cyl}}{2}\right)^2 + U} \tag{14}$$ |
| whereas | whereas | ||
| - | $$U = \frac{\frac{1}{2}(2\pi - \Omega) \cdot D_Z^2 + a \cdot D_Z \cdot \sin\left(\frac{\Omega}{2}\right) + (2\pi - \Omega) \cdot D_Z \cdot L_{cyl}}{2\pi}$$ | + | $$U = \frac{\frac{1}{2}(2\pi - \Omega) \cdot D_Z^2 + a \cdot D_Z \cdot \sin\left(\frac{\Omega}{2}\right) + (2\pi - \Omega) \cdot D_Z \cdot L_{cyl}}{2\pi} \tag{15}$$ |
| The surrogate arrangement is divided into an amount of elements which correspond to amount of the cooling channels. | The surrogate arrangement is divided into an amount of elements which correspond to amount of the cooling channels. | ||
| Zeile 103: | Zeile 103: | ||
| The distance $s_r^*$ is then calculated with | The distance $s_r^*$ is then calculated with | ||
| - | $$s_r = r_a - r_i$$ | + | $$s_r = r_a - r_i \tag{16}$$ |
| After introducing the dimensionless coordinate in radial direction | After introducing the dimensionless coordinate in radial direction | ||
| - | $$\zeta = \frac{r' | + | $$\zeta = \frac{r' |
| with r' as moving coordinate the heat balance in radial direction is | with r' as moving coordinate the heat balance in radial direction is | ||
| - | $$\dot{Q}_{cyl, | + | $$\dot{Q}_{cyl, |
| After inserting the following equation the result is | After inserting the following equation the result is | ||
| - | $$\frac{A_{tube}}{A_{cool, | + | $$\frac{A_{tube}}{A_{cool, |
| with the area of the section of the surrogate pipe | with the area of the section of the surrogate pipe | ||
| - | $$A_{tube} = \frac{2\pi \cdot r_i \cdot L_{cyl}}{i_{cool}}$$ | + | $$A_{tube} = \frac{2\pi \cdot r_i \cdot L_{cyl}}{i_{cool}} \tag{20}$$ |
| And the cooling channel area | And the cooling channel area | ||
| - | $$A_{cool, | + | $$A_{cool, |
| Here the length of the cooling channel in z-direction $L_{Kühl, | Here the length of the cooling channel in z-direction $L_{Kühl, | ||
| Zeile 129: | Zeile 129: | ||
| Therefore the temperature $T_r$ at the barrel surface is | Therefore the temperature $T_r$ at the barrel surface is | ||
| - | $$T_{cyl,r} = T_{cool} - \frac{\dot{q}_{cool} \cdot s_r}{\lambda_{cyl}} \cdot \frac{\ln\left(\frac{A_{cool, | + | $$T_{cyl,r} = T_{cool} - \frac{\dot{q}_{cool} \cdot s_r}{\lambda_{cyl}} \cdot \frac{\ln\left(\frac{A_{cool, |
| ===== Literatur ===== | ===== Literatur ===== | ||