/*! 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 42 The melting of water initially a... [FREE SOLUTION] | 91Ó°ÊÓ

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The melting of water initially at the fusion temperature, \(T_{f}=0^{\circ} \mathrm{C}\), was considered in Example 1.6. Freezing of water often occurs at \(0^{\circ} \mathrm{C}\). However, pure liquids that undergo a cooling process can remain in a supercooled liquid state well below their equilibrium freezing temperature, \(T_{f}\), particularly when the liquid is not in contact with any solid material. Droplets of liquid water in the atmosphere have a supercooled freezing temperature, \(T_{f s s}\), that can be well correlated to the droplet diameter by the expression \(T_{f, s c}=-28+0.87 \ln \left(D_{p}\right)\) in the diameter range \(10^{-7}

Short Answer

Expert verified
In summary, for a droplet of diameter 50 µm and initial temperature 10°C subject to ambient conditions of -40°C and h = 900 W/m² ⋅ K, the time needed to completely solidify the droplet is approximately 0.01694 s for Case A (when the droplet solidifies at Tf = 0°C), and 0.0242 s for Case B (when the droplet solidifies at a supercooled freezing temperature Tf,sc ≈ -16.19°C). The temperature history plot is a step function, with Case A transitioning from 10°C to 0°C, and Case B transitioning from 10°C to -16.19°C.

Step by step solution

01

Identify and Compute Essential Parameters

Given data from the exercise: - Initial temperature Ti = 10°C - Ambient temperature T∞ = -40°C - Droplet diameter D = 50 µm - Heat transfer coefficient h = 900 W/m² ⋅ K - Fusion temperature Tf=sc = -28 + 0.87 ln(Dp) - Diameter range = \(10^{-7}<D_{p}<10^{-2}\), with Dp in meters First, convert the droplet diameter into meters, as the expression for Tf,sc utilizes the diameter in meters and the given diameter is in micrometers. D = 50 x \(10^{-6}\) m
02

Calculate Tf,sc for Droplet

Now, substitute D in the expression for Tf,sc to compute the supercooled freezing temperature. Tf,sc = -28 + 0.87 ln(D) Tf,sc ≈ -16.19°C
03

Find Time to Solidify the Droplet under Case A and Case B

Apply Newton's Law of Cooling to find the time for both cases. For Case A (Droplet solidifies at Tf=0°C): t_A = (Ti-Tf)/(h * (Ti-T∞)) t_A ≈ 0.01694 s For Case B (Droplet solidifies at Tf,sc ≈ -16.19°C): t_B = (Ti-Tf,sc)/(h * (Ti-T∞)) t_B ≈ 0.0242 s Since solidification occurs rapidly when the droplet reaches Tf,sc, the time taken in case B is already the time for the droplet to completely solidify.
04

Sketch the Temperature Histories for Case A and Case B

To sketch the temperature histories, we can create two plots as follows: - Case A: - Starts at Ti = 10°C - Takes time t_A ≈ 0.01694 s to reach Tf = 0°C - Maintains temperature at Tf = 0°C until completely solid - Case B: - Starts at Ti = 10°C - Takes time t_B ≈ 0.0242 s to reach Tf,sc ≈ -16.19°C - Rapid solidification occurs under ambient conditions - Becomes completely solid at Tf,sc. The temperature history plot will look like a step function in both cases. In Case A, the step will be from 10°C to 0°C, whereas in Case B, it will be from 10°C to -16.19°C.

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Key Concepts

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

Newton's Law of Cooling
Newton's Law of Cooling offers an understanding of how heat moves from one body to another and is fundamental in this exercise. This law states that the rate of heat loss of a body is directly proportional to the difference in temperature between the body and its surrounding environment.

This process is described mathematically as:\[\frac{dT}{dt} = -h(A)(T-T_\infty)\]where:
  • \(dT/dt\) is the rate of change of temperature with time.
  • \(h\) represents the heat transfer coefficient.
  • \(A\) is the surface area of the body.
  • \(T\) is the temperature of the body at time \(t\).
  • \(T_\infty\) is the ambient temperature.
In our case, this law helps in determining the time required for a droplet to cool to its solidification temperature. We calculated the time using simplified forms of this equation for both normal and supercooled solidification scenarios.

This approach considers the temperature difference and the given heat transfer coefficient to estimate how long the cooling process will take, based on the initial and target temperatures.
Heat Transfer Coefficient
Understanding the heat transfer coefficient, denoted by \( h \), is crucial to our calculations. This concept describes how effectively heat is transferred between a surface and a fluid in contact with it, such as air or water. A higher coefficient indicates that heat is transferred more rapidly.

In this exercise, the heat transfer coefficient is given as \( 900 \, \text{W/m}^2 \cdot \text{K} \). This high value signifies efficient heat transfer, meaning the droplet's temperature will change relatively quickly when exposed to the colder ambient temperature.
The heat transfer coefficient is influenced by factors such as:
  • The properties of the fluid, like viscosity and thermal conductivity.
  • The flow characteristics of the fluid, such as velocity.
  • The characteristics of the surface, including its roughness.
By accounting for this coefficient in our calculations, we better understand how the droplet's internal energy changes as it interacts with its environment.
Solidification Process
The solidification process is a phase transition process where a liquid turns into a solid when its temperature drops below its freezing point. In our exercise, we see two variations of this process through normal freezing and supercooled freezing.

For normal solidification (Case A), the droplet begins to transform into a solid at the fusion temperature \(T_f = 0^\circ \text{C}\). Once this temperature is reached, energy loss continues until the entire droplet is solidified.
In contrast, in the supercooled solidification (Case B), the droplet cools past the typical freezing point without turning solid immediately. It remains liquid until it reaches the supercooled freezing temperature \(T_{f,sc} \). Once this temperature is reached, the solidification happens quickly, driven by the latent heat released during ice formation.
The rapid transition occurs because any small presence of ice provides a surface for further ice crystals to form, speeding up the solidification process. Once this happens, the remaining liquid quickly solidifies.
Latent Heat Release
Latent heat release plays a significant role in the transformation of a liquid to a solid state during freezing. This concept refers to the energy exchange that occurs without any temperature change.

When a liquid droplet begins to freeze, latent heat is released as the molecular structure of the liquid becomes more ordered in the solid phase. This release happens without causing the temperature to drop further, until the phase change is complete.
Contrary to the sensible heat, which relies on temperature differences, latent heat remains hidden until the phase change occurs. In supercooling scenarios, once freezing starts, the released latent heat can heat the adjacent liquid marginally. However, since the droplet becomes solid rapidly, this heat does not lead to a measurable temperature rise.

Understanding latent heat, therefore, provides insight into the energy dynamics at play during rapid solidification, highlighting why phase transitions can undergo acceleration once begun."

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Most popular questions from this chapter

In a material processing experiment conducted aboard the space shuttle, a coated niobium sphere of \(10-\mathrm{mm}\) diameter is removed from a furnace at \(900^{\circ} \mathrm{C}\) and cooled to a temperature of \(300^{\circ} \mathrm{C}\). Although properties of the niobium vary over this temperature range, constant values may be assumed to a reasonable approximation, with \(\rho=8600 \mathrm{~kg} / \mathrm{m}^{3}, c=290 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\), and \(k=\) \(63 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). (a) If cooling is implemented in a large evacuated chamber whose walls are at \(25^{\circ} \mathrm{C}\), determine the time required to reach the final temperature if the coating is polished and has an emissivity of \(\varepsilon=0.1\). How long would it take if the coating is oxidized and \(\varepsilon=0.6\) ? (b) To reduce the time required for cooling, consideration is given to immersion of the sphere in an inert gas stream for which \(T_{\infty}=25^{\circ} \mathrm{C}\) and \(h=\) \(200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Neglecting radiation, what is the time required for cooling? (c) Considering the effect of both radiation and convection, what is the time required for cooling if \(h=200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and \(\varepsilon=0.6\) ? Explore the effect on the cooling time of independently varying \(h\) and \(\varepsilon\).

The stability criterion for the explicit method requires that the coefficient of the \(T_{m}^{p}\) term of the one-dimensional, finite-difference equation be zero or positive. Consider the situation for which the temperatures at the two neighboring nodes \(\left(T_{\mathrm{m}-1}^{p}, T_{\mathrm{m}+1}^{p}\right)\) are \(100^{\circ} \mathrm{C}\) while the center node \(\left(T_{m}^{p}\right)\) is at \(50^{\circ} \mathrm{C}\). Show that for values of \(F o>\frac{1}{2}\) the finite-difference equation will predict a value of \(T_{m}^{p+1}\) that violates the second law of thermodynamics.

A long plastic rod of \(30-\mathrm{mm}\) diameter \((k=0.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\rho c_{p}=1040 \mathrm{~kJ} / \mathrm{m}^{3} \cdot \mathrm{K}\) ) is uniformly heated in an oven as preparation for a pressing operation. For best results, the temperature in the rod should not be less than \(200^{\circ} \mathrm{C}\). To what uniform temperature should the rod be heated in the oven if, for the worst case, the rod sits on a conveyor for \(3 \mathrm{~min}\) while exposed to convection cooling with ambient air at \(25^{\circ} \mathrm{C}\) and with a convection coefficient of \(8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) ? A further condition for good results is a maximum-minimum temperature difference of less than \(10^{\circ} \mathrm{C}\). Is this condition satisfied? If not, what could you do to satisfy it?

A cold air chamber is proposed for quenching steel ball bearings of diameter \(D=0.2 \mathrm{~m}\) and initial temperature \(T_{i}=400^{\circ} \mathrm{C} .\) Air in the chamber is maintained at \(-15^{\circ} \mathrm{C}\) by a refrigeration system, and the steel balls pass through the chamber on a conveyor belt. Optimum bearing production requires that \(70 \%\) of the initial thermal energy content of the ball above \(-15^{\circ} \mathrm{C}\) be removed. Radiation effects may be neglected, and the convection heat transfer coefficient within the chamber is \(1000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Estimate the residence time of the balls within the chamber, and recommend a drive velocity of the conveyor. The following properties may be used for the steel: \(k=50 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=2 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\), and \(c=450 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\).

A tile-iron consists of a massive plate maintained at \(150^{\circ} \mathrm{C}\) by an embedded electrical heater. The iron is placed in contact with a tile to soften the adhesive, allowing the tile to be easily lifted from the subflooring. The adhesive will soften sufficiently if heated above \(50^{\circ} \mathrm{C}\) for at least \(2 \mathrm{~min}\), but its temperature should not exceed \(120^{\circ} \mathrm{C}\) to avoid deterioration of the adhesive. Assume the tile and subfloor to have an initial temperature of \(25^{\circ} \mathrm{C}\) and to have equivalent thermophysical properties of \(k=0.15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and \(\rho c_{p}=1.5 \times 10^{6}\) \(\mathrm{J} / \mathrm{m}^{3} \cdot \mathrm{K}\) Tile, 4-mm thickness Subflooring (a) How long will it take a worker using the tile-iron to lift a tile? Will the adhesive temperature exceed \(120^{\circ} \mathrm{C} ?\) (b) If the tile-iron has a square surface area \(254 \mathrm{~mm}\) to the side, how much energy has been removed from it during the time it has taken to lift the tile?

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