Thermodynamics: An Engineering Approach
Thermodynamics: An Engineering Approach
8th Edition
ISBN: 9780077624811
Author: CENGEL
Publisher: MCG
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Chapter 7.13, Problem 208RP

a)

To determine

The amount of ice added.

a)

Expert Solution
Check Mark

Answer to Problem 208RP

The amount of ice added is 34g.

Explanation of Solution

Write the expression for the energy balance equation for closed system.

EinEout=ΔEsystem (I)

Here, energy transfer into the control volume is Ein, energy transfer exit from the control volume is Eout and change in internal energy of system is ΔEsystem.

Write the expression to calculate the initial entropy of the refrigerant.

s1=sf+x1sfg (II)

Here, initial entropy is s1, saturated liquid entropy is sf, initial vapor quality is x1 and evaporated entropy is sfg.

Write the expression to calculate the initial enthalpy of the refrigerant.

h1=hf+x1hfg (III)

Here, initial enthalpy is h1, saturated liquid enthalpy is hf, initial vapor quality is x1 and evaporated enthalpy is hfg.

Write the expression to calculate the initial specific volume of the mixture.

v1=vf+x1(vgvf) (IV)

Here, initial specific volume of the mixture is v1 , specific volume of the liquid phase is vf, specific volume of the vapor phase is vg and initial vapor quality is x1.

Write the expression to calculate the mass of the stream msteam.

msteam=ν1v1 (V)

Here, the initial volume of a container is ν1.

Conclusion:

Substitute Wb,in for Ein, 0 for Eout and ΔU for ΔEsystem in Equation (I).

Wb,in=ΔUΔH=0ΔHice+ΔHwater=0

[mcp,ice(0°C(T1)solid)solid+mhif+mcp,liquid((T2)liquid0°C)liquid]ice+[m(h2h1)]water=0mice[cp,ice(0°C(T1)solid)solid+hif+cp,liquid((T2)liquid0°C)liquid]ice+[m(h2h1)]water=0 (VI)

Here, change in enthalpy in ice is ΔHice, change in enthalpy in water is ΔHwater, heat of fusion of ice is hif, mass of the ice is mice, mass of the water is mwater, initial temperature is T1, final temperature is T2 , specific heat at constant pressure for liquid is cp,liquid, initial enthalpy is h1 and final enthalpy is h2.

From the Table A-4, “Saturated water-Temperature table” the obtain the following properties at temperature of is 100°C.

vf=0.001043m3/kgvg=1.6720m3/kgsf=1.3072kJ/kgKsfg=6.0470kJ/kgKhf=419.17kJ/kghfg=2256.4kJ/kg

From the Table A-4, “Saturated water-Temperature table” the obtain the following properties at temperature of is 100°C.

h2=419.17kJ/kgs2=1.3072kJ/kgK

Here, the final entropy is s2.

Substitute 419.17kJ/kg for hf, 2256.4kJ/kg for hfg and 0.1 for x1 in Equation (III).

h1=419.17kJ/kg+(0.1)2256.4kJ/kg=644.81kJ/kg

Substitute 0.001043m3/kg for vf, 1.6720m3/kg for vg and 0.1 for x1 in Equation (IV).

v1=0.001043m3/kg+(0.1)(1.6720m3/kg0.001043m3/kg)=0.16814m3/kg

Substitute 1.3072kJ/kgK for sf, 6.0470kJ/kgK for sfg and 0.1 for x1 in Equation (II).

s1=1.3072kJ/kgK+(0.1)6.0470kJ/kgK=1.9119kJ/kgK

Substitute 0.16814m3/kg for v1 and 0.02m3 for ν1 in Equation (I).

msteam=0.02m30.16814m3/kg=0.119kg

From the Table A-3, “Properties of common liquids, solids, and foods”, select the specific heat at constant pressure at room temperature for liquid and ice as 4.18kJ/kgK and 2.11kJ/kgK respectively.

The melting temperature and the heat of fusion of ice at 1atm as 0 C and 333.7kJ/kg respectively.

Substitute 0.119kg for msteam, 100°C for T2, 2.11kJ/kgK for cp,ice, 18° C for T1, 333.7kJ/kg for hif, 4.18kJ/kg°C for cp,liquid, 644.81kJ/kg for h1 and 419.17kJ/kg for h2 in Equation (VI).

{mice[(2.11kJ/kgK)(0°C(18° C))solid+(333.7kJ/kg)+(4.18kJ/kg°C)(100°C0°C)]ice+[0.119kg(419.17kJ/kg644.81kJ/kg)]steam}=0mice=0.034kg(1000g1kg)mice=34g

Thus, the amount of ice added is 34g.

b)

To determine

The entropy generation during the process.

b)

Expert Solution
Check Mark

Answer to Problem 208RP

The generation during the process is 0.0188kJ/K.

Explanation of Solution

Write the expression for the entropy balance equation of the system.

SinSout+Sgen=ΔSsystem (VII)

Here, rate of net entropy in is Sin, rate of net entropy out is Sout, rate of entropy generation is Sgen and change of entropy of the system is ΔSsystem

Conclusion:

Substitute 0 for Sin, 0 for Sout and ΔSice+ΔSwater for ΔSsystem in Equation (VII).

00+Sgen=ΔSice+ΔSsteamSgen=(micecp,iceln(TmeltingT1)solid+micehifTmelting+micecp,liquidln(T2T1)liquid)ice+msteam(s2s1)steamSgen=mice(cp,iceln(TmeltingT1)solid+hifTmelting+cp,liquidln(T2T1)liquid)ice+msteam(s2s1)steam (VIII)

Substitute 0.119kg for msteam,0.034kg for mice, 2.11kJ/kgK for cp,ice, 0 °C for Tmelting, 18° C for T1,solid, 333.7kJ/kg for hif, 4.18kJ/kgK for cp,liquid, 0 °C for T1,liquid, 100 °C for T2,liquid,1.3072kJ/kgK for s2 and 1.9119kJ/kgK for s1 in Equation (VIII).

Sgen={0.034kg((2.11kJ/kgK)ln(0°C18°C)solid+333.7kJ/kg0°C+[(4.18kJ/kgK)ln(100°C0°C)liquid])ice+[(0.119kg)(1.3072kJ/kgK1.9119kJ/kgK)]steam}

Sgen={0.034kg((2.11kJ/kgK)ln((0+273.15)K(18+273.15)K)solid+333.7kJ/kg0+273.15K+[(4.18kJ/kgK)ln((100+273.15)K(0+273.15)K)liquid])ice+[(0.119kg)(1.3072kJ/kgK1.9119kJ/kgK)]steam}=0.0907kJ/K0.0719kJ/K=0.0188kJ/K

Thus, the generation during the process is 0.0188kJ/K.

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Chapter 7 Solutions

Thermodynamics: An Engineering Approach

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