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Jakob (1949) suggests the following correlation be used for square tubes in a liquid cross-flow situation: Nu=0.102Re0.675Pr1/3 Water (k=0.61 W/mK,Pr=6) at 50C flows across a 1cm square tube with a Reynolds number of 10,000 and surface temperature of 75C. If the tube is 2 m long, the rate of heat transfer between the tube and water is (a) 6.0 kW (b) 8.2 kW (c) 11.3 kW (d) 15.7 kW (e) 18.1 kW

Short Answer

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Question: A 2-meter long, 1-cm side square tube is placed inside water with a Reynolds number of 10,000 and a Prandtl number of 6. The thermal conductivity of the water is given as 0.6 W/mK. Calculate the rate of heat transfer between the tube and the water using the following correlation from Jakob (1949) for square tubes in liquid cross-flow situations: Nu = 0.102 × Re^0.675 × Pr^(1/3). Answer: Follow the steps below to find the rate of heat transfer between the tube and water: 1. Calculate the Nusselt number (Nu) using the given correlation: Nu = 0.102 × (10,000)^0.675 × (6)^(1/3) Nu ≈ 394.16 2. Calculate the convective heat transfer coefficient (h) using the Nu, thermal conductivity (k), and characteristic length (L): h = (394.16 × 0.6) / 0.01 h ≈ 23649.6 W/m²K 3. Calculate the surface area (A) of the square tube: A = 4 × (0.01) × (2) A = 0.08 m² 4. Calculate the heat transfer rate (Q) using the convective heat transfer coefficient (h), surface area (A), and the temperature difference (ΔT) between the tube surface and the water (assuming a constant ΔT): Q = 23649.6 × 0.08 × ΔT Q = 1891.97 × ΔT W The heat transfer rate between the tube and water depends on the temperature difference (ΔT) between the tube surface and the water, and is given by Q = 1891.97 × ΔT W.

Step by step solution

01

Calculate the Nusselt number (Nu)

Using the given correlation and the known values for the Reynolds and Prandtl numbers, calculate the Nusselt number (Nu): Nu=0.102×Re0.675×Pr1/3 Substituting the known values: Nu=0.102×(10,000)0.675×(6)1/3
02

Calculate the convective heat transfer coefficient (h)

Using the Nusselt number (Nu), the thermal conductivity of the fluid (k), and the characteristic length (L): h=Nu×kL The characteristic length (L) is equal to the side length of the square tube, which is given as 1 cm (0.01 m). Using the calculated Nusselt number and the given thermal conductivity, calculate the convective heat transfer coefficient (h).
03

Calculate the heat transfer rate (Q)

Using the convective heat transfer coefficient (h), the surface area (A), and the temperature difference (ΔT) between the tube surface and the water, calculate the heat transfer rate (Q): Q=h×A×ΔT The surface area (A) of the square tube can be calculated as: A=P×L=4×(side length)×(tube length) Substitute the known values and solve for the heat transfer rate (Q), then compare the result with the given options to choose the correct answer.

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Key Concepts

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

Nusselt Number
The Nusselt number (Nu) is a dimensionless parameter of paramount importance in the study of convective heat transfer. It is essentially a comparative measure of convective to conductive heat transfer at a boundary in a fluid flow. The higher the Nusselt number, the more efficient the convective heat transfer relative to conduction. The Nusselt number is calculated using certain key physical properties and flow characteristics of the fluid, such as the Reynolds number and the Prandtl number.

For our example exercise, Jakob's correlation formula provides a specific way to calculate the Nusselt number for water flowing over a square tube. By inserting the given Reynolds number (Re) for the flow velocity and dimensions, and the Prandtl number (Pr) representing the physical properties of water at the specified temperature, we can determine the Nusselt number, which is crucial to finding the heat transfer coefficient.
Reynolds Number
The Reynolds number (Re) is another dimensionless number used to predict flow patterns in different fluid flow situations. It expresses the ratio of inertial forces to viscous forces and is key in determining the regime of the flow, whether it's laminar or turbulent. Laminar flow leads to a lower heat transfer rate compared to turbulent flow, which significantly enhances the mixing and therefore, the rate of convective heat transfer.

In the given problem, we have a Reynolds number of 10,000, which suggests that the flow is turbulent. Turbulent flow tends to have higher Nusselt numbers, implying enhanced convection. Knowing the right Reynolds number for the fluid crossing over the tube is crucial for applying the correlation formula accurately to calculate the Nusselt number.
Prandtl Number
The Prandtl number (Pr) is a dimensionless number named after the German physicist Ludwig Prandtl. This figure represents the ratio of momentum diffusivity (kinematic viscosity) to thermal diffusivity. It essentially compares how quickly momentum and thermal energy are transmitted through the fluid.

In our exercise, the Prandtl number is given as 6 for water at a temperature of 50 degrees Celsius. This number plays a significant role in determining the convective heat transfer for the given situation, as seen in Jakob's correlation. The Prandtl number makes it clear how the fluid properties at a specific temperature affect heat transfer, and it must be combined with the Reynolds number to compute the Nusselt number effectively.
Heat Transfer Coefficient
The heat transfer coefficient (h) is a measurable property that quantifies the convective heat transfer between a solid boundary and the adjacent fluid. It reflects the ease with which heat is transferred from the solid surface to the fluid medium or vice versa. In essence, a higher heat transfer coefficient indicates that the fluid is more effective at absorbing heat from the surface or giving it off.

Once the Nusselt number has been calculated, the heat transfer coefficient can be found using the relationship between these two, the thermal conductivity (k), and the characteristic length of the surface (L). In the square tube example involving water, the coefficient is derived to find out how effectively the tube can transfer heat to the moving water at the set conditions.
Heat Transfer Rate
The heat transfer rate (Q) describes the amount of thermal energy transferred per unit time, typically measured in watts (W) or kilowatts (kW). It is affected by various factors, including the heat transfer coefficient, the surface temperature of the heat exchanging body, and the temperature of the moving fluid. Mathematically, it is expressed as the product of the heat transfer coefficient, the surface area for heat exchange, and the temperature difference between the two exchanging mediums.

The final step of our problem requires calculating this rate using the heat transfer coefficient derived from the Nusselt number, the surface area of the tube, and the temperature difference between the tube surface and the water. By doing so, we can determine the actual heat being transferred in kilowatts, which is a practical and measurable output that engineers and scientists use to analyze and design thermal systems.

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Most popular questions from this chapter

A 0.2 m×0.2 m street sign surface has an absorptivity of 0.6 and an emissivity of 0.7, while the street sign is subjected to a cross flow wind at 20C with a velocity of 1 m/s. Solar radiation is incident on the street sign at a rate of 1100 W/m2, and the surrounding temperature is 20C. Determine the surface temperature of the street sign. Evaluate the air properties at 30C. Treat the sign surface as a vertical plate in cross flow.

Warm air is blown over the inner surface of an automobile windshield to defrost ice accumulated on the outer surface of the windshield. Consider an automobile windshield (kw= 0.8Btu/hftR) with an overall height of 20 in and thickness of 0.2 in. The outside air ( 1 atm) ambient temperature is 8F and the average airflow velocity over the outer windshield surface is 50mph, while the ambient temperature inside the automobile is 77F. Determine the value of the convection heat transfer coefficient for the warm air blowing over the inner surface of the windshield, necessary to cause the accumulated ice to begin melting. Assume the windshield surface can be treated as a flat plate surface.

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For laminar flow of a fluid along a flat plate, one would expect the largest local convection heat transfer coefficient for the same Reynolds and Prandl numbers when (a) The same temperature is maintained on the surface (b) The same heat flux is maintained on the surface (c) The plate has an unheated section (d) The plate surface is polished (e) None of the above

Solar radiation is incident on the glass cover of a solar collector at a rate of 700 W/m2. The glass transmits 88 percent of the incident radiation and has an emissivity of 0.90. The entire hot water needs of a family in summer can be met by two collectors 1.2 m high and 1 m wide. The two collectors are attached to each other on one side so that they appear like a single collector 1.2 m×2 m in size. The temperature of the glass cover is measured to be 35C on a day when the surrounding air temperature is 25C and the wind is blowing at 30 km/h. The effective sky temperature for radiation exchange between the glass cover and the open sky is 40C. Water enters the tubes attached to the absorber plate at a rate of 1 kg/min. Assuming the back surface of the absorber plate to be heavily insulated and the only heat loss to occur through the glass cover, determine (a) the total rate of heat loss from the collector, (b) the collector efficiency, which is the ratio of the amount of heat transferred to the water to the solar energy incident on the collector, and (c) the temperature rise of water as it flows through the collector.

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