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10-59 The Reynolds number for condensate flow is defined as \(\operatorname{Re}=4 \dot{m} / p \mu_{l}\), where \(p\) is the wetted perimeter. Obtain simplified relations for the Reynolds number by expressing \(p\) and \(\dot{m}\) by their equivalence for the following geometries: \((a)\) a vertical plate of height \(L\) and width \(w,(b)\) a tilted plate of height \(L\) and width \(W\) inclined at an angle \(u\) from the vertical, \((c)\) a vertical cylinder of length \(L\) and diameter \(D,(d)\) a horizontal cylinder of length \(L\) and diameter \(D\), and (e) a sphere of diameter \(D\).

Short Answer

Expert verified
Question: Write the simplified expressions for the Reynolds number for condensate flow in the following geometries: (a) vertical plate, (b) tilted plate, (c) vertical cylinder, (d) horizontal cylinder, and (e) sphere. Answer: (a) Vertical plate: $\operatorname{Re} = \frac{2 \rho L w v}{(L+w) \mu_l}$ (b) Tilted plate: $\operatorname{Re} = \frac{2 \rho L_p W v}{(L_p+W) \mu_l}$ (c) Vertical cylinder: $\operatorname{Re} = \frac{2 \rho D v}{\mu_l}$ (d) Horizontal cylinder: $\operatorname{Re} = \frac{2 \rho D v}{\mu_l (1 + 2L/\pi D)}$ (e) Sphere: $\operatorname{Re} = \frac{8 \rho D^2 v}{3 \mu_l}$

Step by step solution

01

(a) Vertical plate

For a vertical plate of height \(L\) and width \(w\), the wetted perimeter \(p\) is given as \(p=2(L+w)\). The mass flow rate \(\dot{m}\) is given by \(\rho L w v\), where \(\rho\) is the density of the fluid, and \(v\) is the velocity. Thus, the Reynolds number is: $$\operatorname{Re} = \frac{4 \rho L w v}{2(L+w) \mu_l} = \frac{2 \rho L w v}{(L+w) \mu_l}$$
02

(b) Tilted plate

For a tilted plate of height \(L\) and width \(W\) inclined at an angle \(u\) from the vertical, we first find the projected length \(L_p = L \cos u\). The wetted perimeter \(p\) is given as \(p=2(L_p+W)\). The mass flow rate \(\dot{m}\) is given by \(\rho L_p W v\). Thus, the Reynolds number is: $$\operatorname{Re} = \frac{4 \rho L_p W v}{2(L_p+W) \mu_l} = \frac{2 \rho L_p W v}{(L_p+W) \mu_l}$$
03

(c) Vertical cylinder

For a vertical cylinder of length \(L\) and diameter \(D\), the wetted perimeter \(p\) is given as \(p=\pi D\). The mass flow rate \(\dot{m}\) is given by \(\rho \pi (D/2)^2 v\). Thus, the Reynolds number is: $$\operatorname{Re} = \frac{4 \rho \pi (D/2)^2 v}{\pi D \mu_l} = \frac{2 \rho D v}{\mu_l}$$
04

(d) Horizontal cylinder

For a horizontal cylinder of length \(L\) and diameter \(D\), the wetted perimeter \(p\) is given as \(p=\pi D + 2L\). The mass flow rate \(\dot{m}\) is given by \(\rho \pi (D/2)^2 v\). Thus, the Reynolds number is: $$\operatorname{Re} = \frac{4 \rho \pi (D/2)^2 v}{(\pi D + 2L) \mu_l} = \frac{2 \rho D v}{\mu_l (1 + 2L/\pi D)}$$
05

(e) Sphere

For a sphere of diameter \(D\), the wetted perimeter \(p\) is given as \(p=\pi D\). The mass flow rate \(\dot{m}\) is given by \(\rho (4/3)\pi (D/2)^3 v\). Thus, the Reynolds number is: $$\operatorname{Re} = \frac{4 \rho (4/3)\pi (D/2)^3 v}{\pi D \mu_l} = \frac{8 \rho D^2 v}{3 \mu_l}$$

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Condensate Flow
Condensate flow refers to the movement of a liquid, typically water, that has condensed from a vapor state. This is common in heat exchangers and cooling systems. The flow behavior is vital in designing efficient thermal systems. When studying condensate flow, understanding various factors such as geometry and fluid properties is essential.
The geometry of the surface affects how the condensate is collected and flows. For instance:
  • Vertical plates allow condensate to flow down due to gravity.
  • Tilted surfaces alter flow paths depending on inclination.
  • Cylinders and spheres involve more complex flow patterns due to curvature.
By examining the condensate flow, engineers can optimize heat transfer efficiency, reducing energy consumption and enhancing system operation.
Wetted Perimeter
The wetted perimeter is the part of a surface in contact with a fluid. In flow analysis, it helps determine the area that offers frictional resistance to flow.
For different geometries, the wetted perimeter varies:
  • For a vertical plate, it is calculated as the total perimeter in contact with the flow, often expressed as \(p = 2(L + w)\).
  • In cylinders, it can become more complex, considering circular shapes where \(p = \pi D\).
  • Spheres experience a similar circular approach, but the flow interaction changes due to 3D curvature.
Understanding the wetted perimeter is crucial for calculating Reynolds number, which helps in evaluating the flow regime, whether laminar or turbulent.
Mass Flow Rate
Mass flow rate represents the amount of mass passing through a section per unit time. It's a key factor in determining how much fluid is moving and affects pressure and velocity within a system.
In condensate flow, the mass flow rate \(\dot{m}\) varies based on the geometry of the object:
  • For a plate, it might be expressed as \(\rho L w v\), involving height \(L\), width \(w\), fluid density \(\rho\), and velocity \(v\).
  • For a cylindrical shape, the expression might become \(\rho \pi (D/2)^2 v\), where \(D\) represents the diameter.
The accurate calculation of mass flow rate ensures that thermal systems are designed with efficiency and reliability, minimizing potential losses or issues.
Fluid Dynamics
Fluid dynamics is the study of fluids in motion and is essential in understanding real-world problems involving condensate flow. Key aspects such as velocity, pressure, and flow patterns are analyzed to predict how fluids behave in different situations.
In fluid dynamics, the Reynolds number is crucial as it determines the flow regime:
  • Laminar flow indicates smooth and orderly motion, occurring at low Reynolds numbers.
  • Turbulent flow is chaotic and irregular, typically happening at high Reynolds numbers.
By measuring parameters like the wetted perimeter and mass flow rate, engineers use fluid dynamics to design systems that operate effectively under various conditions. This ensures proper management of flow, reducing energy wastage and enhancing performance.

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Most popular questions from this chapter

A cylindrical rod is used for boiling water at 1 atm. The rod has a diameter of \(1 \mathrm{~cm}\) and its surface has an emissivity of \(0.3\). Determine the film boiling convection heat transfer coefficient at the burnout point. Evaluate the properties of vapor at \(1150^{\circ} \mathrm{C}\). Discuss whether \(1150^{\circ} \mathrm{C}\) is a reasonable film temperature for the vapor properties.

The condenser of a steam power plant operates at a pressure of \(4.25 \mathrm{kPa}\). The condenser consists of 100 horizontal tubes arranged in a \(10 \times 10\) square array. The tubes are \(8 \mathrm{~m}\) long and have an outer diameter of \(3 \mathrm{~cm}\). If the tube surfaces are at \(20^{\circ} \mathrm{C}\), determine \((a)\) the rate of heat transfer from the steam to the cooling water and (b) the rate of condensation of steam in the condenser.

What is condensation? How does it occur?

An air conditioner condenser in an automobile consists of \(2 \mathrm{~m}^{2}\) of tubular heat exchange area whose surface temperature is \(30^{\circ} \mathrm{C}\). Saturated refrigerant-134a vapor at \(50^{\circ} \mathrm{C}\) \(\left(h_{f g}=152 \mathrm{~kJ} / \mathrm{kg}\right)\) condenses on these tubes. What heat transfer coefficent must exist between the tube surface and condensing vapor to produce \(1.5 \mathrm{~kg} / \mathrm{min}\) of condensate? (a) \(95 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(640 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(727 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(799 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(960 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

A 1 -mm diameter-long electrical wire submerged in water at atmospheric pressure is dissipating \(4100 \mathrm{~W} / \mathrm{m}\) of heat, and the surface temperature reaches \(128^{\circ} \mathrm{C}\). If the experimental constant that depends on the fluid is \(n=1\), determine the nucleate boiling heat transfer coefficient and the value of the experimental constant \(C_{s f}\)

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