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en:grundlagenhandbuch:zylinderwaermestroeme [2026/05/28 09:52] deppe2en: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
  
-$$\zeta = \frac{r'}{s_r}$$+$$\zeta = \frac{r'}{s_r} \tag{17}$$
  
 with r' as moving coordinate the heat balance in radial direction is with r' as moving coordinate the heat balance in radial direction is
  
-$$\dot{Q}_{cyl,r} - \dot{Q}_{\zeta} = \dot{Q}_{cool,r}$$+$$\dot{Q}_{cyl,r} - \dot{Q}_{\zeta} = \dot{Q}_{cool,r} \tag{18}$$
  
 After inserting the following equation the result is After inserting the following equation the result is
  
-$$\frac{A_{tube}}{A_{cool,r}} \cdot \frac{dT}{d\zeta} = \left(\frac{A_{tube}}{A_{cool,r}} - 1\right) \cdot \zeta \cdot \frac{dT}{d\zeta} = \frac{\dot{q}_{cool} \cdot s_r}{\lambda_{Zyl}}$$+$$\frac{A_{tube}}{A_{cool,r}} \cdot \frac{dT}{d\zeta} = \left(\frac{A_{tube}}{A_{cool,r}} - 1\right) \cdot \zeta \cdot \frac{dT}{d\zeta} = \frac{\dot{q}_{cool} \cdot s_r}{\lambda_{Zyl}} \tag{19}$$
  
 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
  
-$$A_{cool,r} = \frac{\pi \cdot D_{cool} \cdot L_{cyl}}{2}$$+$$A_{cool,r} = \frac{\pi \cdot D_{cool} \cdot L_{cyl}}{2} \tag{21}$$
  
 Here the length of the cooling channel in z-direction $L_{Kühl,z}$ is assumed to correspond to the length of the barrel element $L_{Zyl}$. Here the length of the cooling channel in z-direction $L_{Kühl,z}$ is assumed to correspond to the length of the barrel element $L_{Zyl}$.
Zeile 129: Zeile 129:
 Therefore the temperature $T_r$ at the barrel surface is Therefore the temperature $T_r$ at the barrel surface is
  
-$$T_{cyl,r} = T_{cool} - \frac{\dot{q}_{cool} \cdot s_r}{\lambda_{cyl}} \cdot \frac{\ln\left(\frac{A_{cool,r}}{A_{tube}}\right)}{1 - \frac{A_{tube}}{A_{cool,r}}}$$+$$T_{cyl,r} = T_{cool} - \frac{\dot{q}_{cool} \cdot s_r}{\lambda_{cyl}} \cdot \frac{\ln\left(\frac{A_{cool,r}}{A_{tube}}\right)}{1 - \frac{A_{tube}}{A_{cool,r}}} \tag{22}$$
  
 ===== Literatur ===== ===== Literatur =====