Physically, what does the Grashof number represent? How does the Grashof number differ from the Reynolds number?

Short Answer

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Answer: The Grashof number (Gr) is a dimensionless quantity related to natural convection driven by buoyancy forces, representing the ratio of buoyancy forces to viscous forces in a fluid. On the other hand, the Reynolds number (Re) is another dimensionless quantity that deals with the flow behavior and the transition between laminar and turbulent flow in forced convection situations, measuring the ratio of inertial forces to viscous forces in a given flow. Therefore, the Grashof number is focused on buoyancy-driven flow and natural convection, while the Reynolds number pertains to inertial forces and the onset of turbulence in forced convection.

Step by step solution

01

Introduce the Grashof number

The Grashof number (Gr) is a dimensionless quantity that represents the ratio of buoyancy forces to viscous forces in a fluid. It characterizes the influence of fluid density differences on natural convection. A high Grashof number indicates a strong buoyancy-driven flow, while a low Grashof number signifies that the flow is primarily governed by viscous forces.
02

Introduce the Reynolds number

The Reynolds number (Re) is another dimensionless quantity that is used to predict the onset of turbulence in a fluid flow. It measures the ratio of inertial forces to viscous forces in a given flow and is generally used for characterizing the flow of fluids in pipes, channels, and around objects. Larger Reynolds numbers indicate a higher likelihood of turbulence, while smaller Reynolds numbers suggest a laminar (smooth and steady) flow.
03

Compare Grashof and Reynolds numbers

While both the Grashof number and Reynolds number are dimensionless quantities, they represent different aspects of fluid dynamics. The Grashof number is related to natural convection driven by buoyancy forces, while the Reynolds number is connected to the flow behavior and the transition between laminar and turbulent flow mainly in forced convection. In summary, the Grashof number is related to the buoyancy forces and natural convection, whereas the Reynolds number focuses on the inertial forces and the transition between laminar and turbulent flow in forced convection situations.

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Key Concepts

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

Buoyancy Forces in Fluid Dynamics
Buoyancy forces play a pivotal role in fluid dynamics and are central to understanding natural convection. These forces arise due to variations in fluid density, which in turn, are often caused by temperature differences within the fluid. When part of a fluid is warmer than its surroundings, it becomes less dense and rises, creating what is known as a buoyancy force. In contrast, cooler, denser fluid will sink beneath the warmer fluid, creating a circular motion called a convection current. This process is the engine behind many natural phenomena, such as the circulation of air in the earth's atmosphere and the convection currents in a boiling pot of water.

Role of the Grashof Number

To quantify the significance of buoyancy forces relative to the fluid's viscosity, we use the Grashof number (Gr). As Gr increases, buoyancy forces become more dominant, and one can expect to see more vigorous convective currents. For students to fully grasp this concept, it is critical to remember that buoyancy is all about relative density and the tendency of warmer, less dense fluid to rise, driving natural convection.
Natural Versus Forced Convection
Convection can be classified into two categories: natural and forced. Natural convection, as explained earlier, occurs due to buoyancy forces when there are temperature differences within the fluid. It doesn't require an external source to move the fluid; the movement is a result of density changes within the fluid itself. Forced convection, on the other hand, occurs when a fluid is pushed by external means such as a fan or a pump. This type of convection is commonly seen in many engineering systems, including heating, ventilation, and air conditioning (HVAC) systems, where air is circulated through rooms artificially.

Understanding the Distinction

It's crucial for students to recognize the mechanisms driving these two types of convection; natural convection is driven by internal fluid density gradients, while forced convection is driven by external forces. This understanding helps in analyzing which dimensionless number should be considered in their respective scenarios: for natural convection, the Grashof number is key, while for forced convection scenarios, the focus shifts to the Reynolds number.
Laminar and Turbulent Flow
The behavior of fluid flow can be broadly categorized into two types: laminar and turbulent. Laminar flow is characterized by smooth, parallel layers of fluid sliding past each other. This flow is steady and predictable, occurring at lower velocities or in fluids with higher viscosity. In contrast, turbulent flow is chaotic and disordered, with eddies and fluctuations. It occurs at higher velocities or in lower viscosity fluids and is much harder to predict due to its chaotic nature.

Relevance of the Reynolds Number

This is where the Reynolds number (Re) becomes particularly useful. It helps in predicting the type of flow that will occur under certain conditions by comparing inertial forces to viscous forces. A low Re indicates that viscous forces are dominating, resulting in laminar flow, whereas a high Re suggests that inertial forces are dominating, leading to turbulent flow. As students delve into fluid dynamics problems, understanding the transition from laminar to turbulent flow is essential for predicting fluid behavior, designing fluid systems, and analyzing fluid motion, all of which can be influenced by different factors such as fluid velocity, viscosity, and the characteristic length of the system.

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Most popular questions from this chapter

Consider a fluid whose volume does not change with temperature at constant pressure. What can you say about natural convection heat transfer in this medium?

An electric resistance space heater is designed such that it resembles a rectangular box \(50 \mathrm{~cm}\) high, \(80 \mathrm{~cm}\) long, and \(15 \mathrm{~cm}\) wide filled with \(45 \mathrm{~kg}\) of oil. The heater is to be placed against a wall, and thus heat transfer from its back surface is negligible. The surface temperature of the heater is not to exceed \(75^{\circ} \mathrm{C}\) in a room at \(25^{\circ} \mathrm{C}\) for safety considerations. Disregarding heat transfer from the bottom and top surfaces of the heater in anticipation that the top surface will be used as a shelf, determine the power rating of the heater in W. Take the emissivity of the outer surface of the heater to be \(0.8\) and the average temperature of the ceiling and wall surfaces to be the same as the room air temperature. Also, determine how long it will take for the heater to reach steady operation when it is first turned on (i.e., for the oil temperature to rise from \(25^{\circ} \mathrm{C}\) to \(75^{\circ} \mathrm{C}\) ). State your assumptions in the calculations.

Two concentric cylinders of diameters \(D_{i}=30 \mathrm{~cm}\) and \(D_{o}=40 \mathrm{~cm}\) and length \(L=5 \mathrm{~m}\) are separated by air at \(1 \mathrm{~atm}\) pressure. Heat is generated within the inner cylinder uniformly at a rate of \(1100 \mathrm{~W} / \mathrm{m}^{3}\), and the inner surface temperature of the outer cylinder is \(300 \mathrm{~K}\). The steady-state outer surface temperature of the inner cylinder is (a) \(402 \mathrm{~K}\) (b) \(415 \mathrm{~K}\) (c) \(429 \mathrm{~K}\) (d) \(442 \mathrm{~K}\) (e) \(456 \mathrm{~K}\) (For air, use \(k=0.03095 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7111, v=\) \(\left.2.306 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\)

Exhaust gases from a manufacturing plant are being discharged through a \(10-\mathrm{m}-\) tall exhaust stack with outer diameter of \(1 \mathrm{~m}\). The exhaust gases are discharged at a rate of \(0.125 \mathrm{~kg} / \mathrm{s}\), while temperature drop between inlet and exit of the exhaust stack is \(30^{\circ} \mathrm{C}\), and the constant pressure-specific heat of the exhaust gases is \(1600 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\). On a particular calm day, the surrounding quiescent air temperature is \(33^{\circ} \mathrm{C}\). Solar radiation is incident on the exhaust stack outer surface at a rate of \(500 \mathrm{~W} / \mathrm{m}^{2}\), and both the emissivity and solar absorptivity of the outer surface are \(0.9\). Determine the exhaust stack outer surface temperature. Assume the film temperature is \(60^{\circ} \mathrm{C}\).

The side surfaces of a 3-m-high cubic industrial (?) furnace burning natural gas are not insulated, and the temperature at the outer surface of this section is measured to be \(110^{\circ} \mathrm{C}\). The temperature of the furnace room, including its surfaces, is \(30^{\circ} \mathrm{C}\), and the emissivity of the outer surface of the furnace is 0.7. It is proposed that this section of the furnace wall be insulated with glass wool insulation \((k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) wrapped by a reflective sheet \((\varepsilon=0.2)\) in order to reduce the heat loss by 90 percent. Assuming the outer surface temperature of the metal section still remains at about \(110^{\circ} \mathrm{C}\), determine the thickness of the insulation that needs to be used. The furnace operates continuously throughout the year and has an efficiency of 78 percent. The price of the natural gas is \(\$ 1.10 /\) therm ( 1 therm \(=105,500 \mathrm{~kJ}\) of energy content). If the installation of the insulation will cost \(\$ 550\) for materials and labor, determine how long it will take for the insulation to pay for itself from the energy it saves.

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