/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 56 The evaporator section of a refr... [FREE SOLUTION] | 91Ó°ÊÓ

91Ó°ÊÓ

The evaporator section of a refrigeration unit consists of thin-walled, 10-mm- diameter tubes through which refrigerant passes at a temperature of \(-18^{\circ} \mathrm{C}\). Air is cooled as it flows over the tubes, maintaining a surface convection coefficient of \(100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and is subsequently routed to the refrigerator compartment. (a) For the foregoing conditions and an air temperature of \(-3^{\circ} \mathrm{C}\), what is the rate at which heat is extracted from the air per unit tube length? (b) If the refrigerator's defrost unit malfunctions, frost will slowly accumulate on the outer tube surface. Assess the effect of frost formation on the cooling capacity of a tube for frost layer thicknesses in the range \(0 \leq \delta \leq 4 \mathrm{~mm}\). Frost may be assumed to have a thermal conductivity of \(0.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). (c) The refrigerator is disconnected after the defrost unit malfunctions and a 2-mm-thick layer of frost has formed. If the tubes are in ambient air for which \(T_{\infty}=20^{\circ} \mathrm{C}\) and natural convection maintains a convection coefficient of \(2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), how long will it take for the frost to melt? The frost may be assumed to have a mass density of \(700 \mathrm{~kg} / \mathrm{m}^{3}\) and a latent heat of fusion of \(334 \mathrm{~kJ} / \mathrm{kg}\).

Short Answer

Expert verified
(a) The rate at which heat is extracted from the air per unit tube length is \(47.12 \mathrm{~W} / \mathrm{m}\). (b) To assess the effect of frost formation on the cooling capacity of the tubes for different frost layer thicknesses, we need to calculate the total thermal resistance for each thickness, and then plug it into the formula for the new rate of heat extraction. (c) To find the time required for the frost to melt, we need to use the energy balance equation and the provided parameters to solve for the time, \(\Delta t\).

Step by step solution

01

Use the heat transfer formula

The formula of heat transfer through convection is given by: \[q = h A (T_s - T_{\infty})\] where \(q\) = heat extraction rate (W), \(h\) = surface convection coefficient (W/m²K), \(A\) = surface area (m²), \(T_s\) = surface temperature (°C), \(T_{\infty}\) = fluid temperature (°C). Since we are asked to calculate the rate of heat extraction per unit tube length, we can rewrite the area as: \[A = \pi D L\] where \(D\) = diameter of the tube (m), \(L\) = length of the tube (m).
02

Plug in the values and calculate the heat extraction rate per unit length

Using the given values: \(h = 100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), \(D = 0.01 \mathrm{~m}\), \(T_s = -18^{\circ}\mathrm{C}\), \(T_{\infty} = -3^{\circ}\mathrm{C}\). The heat extraction rate per unit length is: \[\frac{q}{L} = h \pi D (T_s - T_{\infty})\] Plugging in the values, we get: \[\frac{q}{L} = 100 \times \pi \times 0.01 \times (-18 - (-3))\] \[\frac{q}{L} = 47.12 \mathrm{~W} / \mathrm{m}\] (b) Assess the effect of frost formation on the cooling capacity of a tube for frost layer thicknesses in the range \(0 \leq \delta \leq 4 \mathrm{~mm}\)
03

Determine the additional thermal resistance due to frost layer

The additional thermal resistance due to the frost layer is given by: \[R_f = \frac{\delta}{k_f A_f}\] where \(R_f\) = frost thermal resistance (K/W), \(\delta\) = frost layer thickness (m), \(k_f\) = frost thermal conductivity (W/mK), \(A_f\) = outer surface area (m²). The outer surface area is: \[A_f = \pi (D+2\delta) L\] Now we can express the total thermal resistance (\(R_{total}\)) as the sum of the frost layer resistance and the convection resistance: \[R_{total} = R_f + \frac{1}{hA}\]
04

Calculate the new rate of heat extraction for different frost layer thicknesses

Using the given parameters, we get: \[\frac{q_{new}}{L} = \frac{\pi (D + 2\delta) (T_s - T_{\infty})}{R_{total}}\] For the given range of frost layer thicknesses (\(0 \leq \delta \leq 4 \mathrm{~mm}\)), we must calculate \(R_{total}\) and plug it in above formula to find the new rate of heat extraction. (c) Find the time required for the frost to melt
05

Use the energy balance equation to find the time

We know that, to melt the frost, the energy required is given by \(Q = m_L \cdot L_f\), where \(m_L\) is the mass of frost per unit length and \(L_f\) is the latent heat of fusion. We can also relate the energy input with the heat transfer from the surroundings, where \(q_{melt}\) is the rate of heat transfer from the surrounding air per unit length, then: \[q_{melt} \Delta t = m_L \cdot L_f\] We know \(q_{melt} = h_m A_{melt} (T_\infty - T_s)\), where \(\Delta t\) is the time required to melt the frost, \(h_m\) is convection coefficient value, \(A_{melt}\) is the area where the melting process takes place. The mass of frost per unit length can be written as \(m_L = \rho L\delta\), where \(\rho\) is the mass density of the frost. Plugging in the given values and the calculated values, we can find \(\Delta t\), the time required for the frost to melt.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with 91Ó°ÊÓ!

Key Concepts

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

Conduction
Conduction is a mode of heat transfer through which energy flows due to the temperature gradient within a solid object or between solid objects in direct contact. It primarily occurs without the movement of the material itself. This mechanism is driven by the interaction of particles vibrating at different energy levels.
Inside a refrigeration unit, conduction plays a significant role when considering the flow of heat within the tubes carrying the refrigerant. The tube material's conductivity influences how efficiently heat can be transferred from the tube surface to the refrigerant inside it.
The basic formula governing conduction is Fourier's Law: \[ q = -kA \frac{dT}{dx} \] where:
  • \( q \) is the heat transfer rate through conduction (Watt),
  • \( k \) is the thermal conductivity of the material (W/mK),
  • \( A \) is the cross-sectional area perpendicular to the direction of heat flow (\( m^2 \)),
  • \( \frac{dT}{dx} \) is the temperature gradient over the distance \( x \)
To assess the system's efficiency, understanding conduction is fundamental, as it influences not only the cooling capacity but also determines the necessity to control material properties like thickness and thermal conductivity.
Convection
Convection is all about the transportation of heat through fluids, which can be liquids or gases. It combines the aspects of environmental interaction and flow within a given system. In the context of heat transfer in the refrigeration unit, the air moving over the tube surface is responsible for the convection heat transfer process.
This heat transfer can be characterized by Newton's Law of Cooling: \( q = hA(T_s - T_{\infty}) \)where:
  • \( q \) is the rate of heat transfer through convection (Watt),
  • \( h \) is the surface convection heat transfer coefficient (W/m²K),
  • \( A \) is the surface area over which convection takes place (\( m^2 \)),
  • \( T_s \) is the temperature of the surface (°C),
  • \( T_{\infty} \) is the temperature of the bulk fluid (°C)
When frost forms on the tubes, it may affect the convection coefficient \( h \), as the surface texture changes. This can lead to reduced cooling efficiency. Also, different conditions, such as forced or natural convection, impact the heat transfer rate, particularly during the defrosting process.
Thermal Resistance
Thermal resistance is a concept that quantifies an object’s ability to resist the flow of heat. It is central when layers of materials with different thermal conductivities are involved, like when frost builds up on the refrigeration tubes.
This resistance can be thought of similarly to electrical resistance where high resistance implies less heat flows. The formula for thermal resistance in the context of the frost on tubes is given by: \[ R = \frac{\delta}{kA} \]where:
  • \( R \) is the thermal resistance (K/W),
  • \( \delta \) is the thickness of the frost layer (m),
  • \( k \) is the thermal conductivity of the frost (W/mK),
  • \( A \) is the area through which heat is being transferred (\( m^2 \))
As frost accumulates, the total thermal resistance of the tube and the frost layer increases, reducing the rate of heat transfer, which impacts the cooling capacity of the system. Effectively managing layers and accounting for their resistances are crucial for maintaining efficient thermal systems.
Latent Heat of Fusion
Latent heat of fusion is the amount of heat needed to convert a solid into a liquid at its melting point, without changing its temperature. This concept is key in understanding the energy requirements for melting frost in a refrigeration unit.
When frost accumulates and needs to be melted, the energy needed is calculated using the frost's mass and its latent heat of fusion. The basic relation is:\[ Q = mL_f \]where:
  • \( Q \) is the heat energy required (Joules),
  • \( m \) is the mass of the frost (kg),
  • \( L_f \) is the latent heat of fusion (J/kg)
In the exercise, given the frost's thickness and density, one can compute how much energy is needed to melt it. Understanding this helps in estimating the time it takes for natural or assisted thawing processes to complete, impacting practical operations of cooling systems after defrosting issues occur.

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A storage tank consists of a cylindrical section that has a length and inner diameter of \(L=2 \mathrm{~m}\) and \(D_{i}=1 \mathrm{~m}\), respectively, and two hemispherical end sections. The tank is constructed from 20-mm-thick glass (Pyrex) and is exposed to ambient air for which the temperature is \(300 \mathrm{~K}\) and the convection coefficient is \(10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The tank is used to store heated oil, which maintains the inner surface at a temperature of \(400 \mathrm{~K}\). Determine the electrical power that must be supplied to a heater submerged in the oil if the prescribed conditions are to be maintained. Radiation effects may be neglected, and the Pyrex may be assumed to have a thermal conductivity of \(1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\).

The cross section of a long cylindrical fuel element in a nuclear reactor is shown. Energy generation occurs uniformly in the thorium fuel rod, which is of diameter \(D=25 \mathrm{~mm}\) and is wrapped in a thin aluminum cladding. (a) It is proposed that, under steady-state conditions, the system operates with a generation rate of \(\dot{q}=\) \(7 \times 10^{8} \mathrm{~W} / \mathrm{m}^{3}\) and cooling system characteristics of \(T_{\infty}=95^{\circ} \mathrm{C}\) and \(h=7000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Is this proposal satisfactory? (b) Explore the effect of variations in \(\dot{q}\) and \(h\) by plotting temperature distributions \(T(r)\) for a range of parameter values. Suggest an envelope of acceptable operating conditions.

Approximately \(10^{6}\) discrete electrical components can be placed on a single integrated circuit (chip), with electrical heat dissipation as high as \(30,000 \mathrm{~W} / \mathrm{m}^{2}\). The chip, which is very thin, is exposed to a dielectric liquid at its outer surface, with \(h_{o}=1000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(T_{\infty, 0}=20^{\circ} \mathrm{C}\), and is joined to a circuit board at its inner surface. The thermal contact resistance between the chip and the board is \(10^{-4} \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\), and the board thickness and thermal conductivity are \(L_{b}=5 \mathrm{~mm}\) and \(k_{b}=1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), respectively. The other surface of the board is exposed to ambient air for which \(h_{i}=40\) \(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(T_{\infty, i}=20^{\circ} \mathrm{C}\). (a) Sketch the equivalent thermal circuit corresponding to steady-state conditions. In variable form, label appropriate resistances, temperatures, and heat fluxes. (b) Under steady-state conditions for which the chip heat dissipation is \(q_{c}^{\prime \prime}=30,000 \mathrm{~W} / \mathrm{m}^{2}\), what is the chip temperature? (c) The maximum allowable heat flux, \(q_{c, m}^{\prime \prime}\), is determined by the constraint that the chip temperature must not exceed \(85^{\circ} \mathrm{C}\). Determine \(q_{c, m}^{\prime \prime}\) for the foregoing conditions. If air is used in lieu of the dielectric liquid, the convection coefficient is reduced by approximately an order of magnitude. What is the value of \(q_{c, m}^{\prime \prime}\) for \(h_{o}=100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) ? With air cooling, can significant improvements be realized by using an aluminum oxide circuit board and/or by using a conductive paste at the chip/board interface for which \(R_{t, c}^{n}=10^{-5} \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) ?

The air inside a chamber at \(T_{\infty, i}=50^{\circ} \mathrm{C}\) is heated convectively with \(h_{i}=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) by a 200 -mm-thick wall having a thermal conductivity of \(4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and a uniform heat generation of \(1000 \mathrm{~W} / \mathrm{m}^{3}\). To prevent any heat generated within the wall from being lost to the outside of the chamber at \(T_{\infty, o}=25^{\circ} \mathrm{C}\) with \(h_{o}=5\) \(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\), a very thin electrical strip heater is placed on the outer wall to provide a uniform heat flux, \(q_{\sigma^{\prime}}\) (a) Sketch the temperature distribution in the wall on \(T-x\) coordinates for the condition where no heat generated within the wall is lost to the outside of the chamber. (b) What are the temperatures at the wall boundaries, \(T(0)\) and \(T(L)\), for the conditions of part (a)? (c) Determine the value of \(q_{o}^{\prime \prime}\) that must be supplied by the strip heater so that all heat generated within the wall is transferred to the inside of the chamber. (d) If the heat generation in the wall were switched off while the heat flux to the strip heater remained constant, what would be the steady-state temperature, \(T(0)\), of the outer wall surface?

An electrical current of 700 A flows through a stainless steel cable having a diameter of \(5 \mathrm{~mm}\) and an electrical resistance of \(6 \times 10^{-4} \mathrm{\Omega} / \mathrm{m}\) (i.e., per meter of cable length). The cable is in an environment having a temperature of \(30^{\circ} \mathrm{C}\), and the total coefficient associated with convection and radiation between the cable and the environment is approximately \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) If the cable is bare, what is its surface temperature? (b) If a very thin coating of electrical insulation is applied to the cable, with a contact resistance of \(0.02 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\), what are the insulation and cable surface temperatures? (c) There is some concern about the ability of the insulation to withstand elevated temperatures. What thickness of this insulation \((k=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) will yield the lowest value of the maximum insulation temperature? What is the value of the maximum temperature when this thickness is used?

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.