Thermodynamics: An Engineering Approach
Thermodynamics: An Engineering Approach
9th Edition
ISBN: 9781259822674
Author: Yunus A. Cengel Dr., Michael A. Boles
Publisher: McGraw-Hill Education
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Chapter 14.7, Problem 29P

The air in a room has a dry-bulb temperature of 26°C and a wet-bulb temperature of 21°C. Assuming a pressure of 100 kPa, determine (a) the specific humidity, (b) the relative humidity, and (c) the dew-point temperature.

(a)

Expert Solution
Check Mark
To determine

The specific humidity.

Answer to Problem 29P

The specific humidity is 0.0138kgH2O/kgdryair.

Explanation of Solution

Express the specific humidity.

ω1=cp(T2T1)+ω2hfg2hg1hf2=cp(T2T1)+ω2hfg@21°Chg@26°Chf@21°C (I)

Here, specific heat at constant pressure of air is cp, initial and final temperature is T1andT2 respectively, specific humidity at exit is ω2, initial specific enthalpy at saturated vapor is hg1, final specific enthalpy at saturated liquid is hf2 and final specific enthalpy at evaporation is hfg2.

Express specific humidity at exit.

ω2=0.622Pg2P2Pg2=0.622Psat@21°CP2Psat@21°C (II)

Here, final pressure is P2, final vapor pressure is Pg2 and saturation pressure at temperature of 21°C is Psat@21°C.

Conclusion:

Refer Table A-4, “saturated water-temperature table”, and write the saturation pressure at temperature of 21°C using an interpolation method.

Write the formula of interpolation method of two variables.

y2=(x2x1)(y3y1)(x3x1)+y1 (III)

Here, the variables denote by x and y is temperature and saturation pressure respectively.

Show thesaturation pressure corresponding to temperature as in Table (1).

Temperature

T(°C)

Saturation pressure

Psat(kPa)

20 (x1)2.3392 (y1)
21 (x2)(y2=?)
25 (x3)3.1698 (y3)

Substitute 20°C,21°C,and25°C for x1,x2andx3 respectively, and 2.3392kPa for y1 and 3.1698kPa for y3 in Equation (III).

y2=(21°C20°C)(3.1698kPa2.3392kPa)(25°C20°C)+2.3392kPa=2.488kPa=Psat@21°C

Thus, the saturation pressure at temperature of 21°C is,

Psat@21°C=2.488kPa

Substitute 2.488kPa for Psat@21°C and 100kPa for P2 in Equation (II).

ω2=0.622(2.488kPa)100kPa2.488kPa=0.01587kgH2O/kgdryair

Refer Table A-4, “saturated water-temperature table”, and write final specific enthalpy evaporation at temperature of 21°C using an interpolation method.

Show thefinal specific enthalpy evaporationcorresponding to temperature as in Table(2).

Temperature

T(°C)

Final specific enthalpy evaporation

hfg2(kJ/kg)

20 (x1)2453.5 (y1)
21 (x2)(y2=?)
25 (x3)2441.7 (y3)

Use excels and tabulates the values from Table (2) in Equation (III) to get,

hfg2=2451.2kJ/kg

Refer Table A-4, “saturated water-temperature table”, and write initial specific enthalpy saturated vapor at temperature of 26°C using an interpolation method.

Show theinitial specific enthalpy saturated vapor corresponding to temperature as in Table (3).

Temperature

T(°C)

Initial specific enthalpy saturated vapor

hg1(kJ/kg)

25(x1)2546.5(y1)
26(x2)(y2=?)
30(x3)2555.6(y3)

Use excels and tabulates the values from Table (3) in Equation (III) to get,

hg1=2548.3kJ/kg

Refer Table A-4, “saturated water-temperature table”, and write final specific enthalpy saturated liquid at temperature of 21°C using an interpolation method.

Show thefinal specific enthalpy evaporationcorresponding to temperature as in Table(4).

Temperature

T(°C)

Final specific enthalpy saturated liquid

hf2(kJ/kg)

20 (x1)83.915 (y1)
21 (x2)(y2=?)
25 (x3)104.83 (y3)

Use excels and tabulates the values from Table (4) in Equation (III) to get,

hf2=88.10kJ/kg

Refer Table A-2 (a), “ideal gas specific heats of various common gases”, and write specific heat at constant pressure of dry air.

cp=1.005kJ/kg°C

Substitute 1.005kJ/kg°C for cp, 21°C for T2 and 26°C for T1, 0.01587 for ω2, 2451.2kJ/kg for hfg2, 2548.3kJ/kg for hg1 and 88.10kJ/kg for hf2 in Equation (I).

ω1=(1.005kJ/kg°C)(2126)°C+(0.01587)(2451.2kJ/kg)(2548.388.10)kJ/kg=0.0138kgH2O/kgdryair

Hence, the specific humidity is 0.0138kgH2O/kgdryair.

(b)

Expert Solution
Check Mark
To determine

The relative humidity.

Answer to Problem 29P

The relative humidity is 64.4%.

Explanation of Solution

Express saturation pressure of water at temperature of 30°C.

ϕ1=ω1P1(0.622+ω1)Pg1=ω1P1(0.622+ω1)Psat@26°C (IV)

Here, initial pressure is P1 and saturation pressure at temperature of 26°C is Psat@26°C.

Conclusion:

Refer Table A-4, “saturated water-temperature table”, and write the saturation pressure at temperature of 26°C using an interpolation method.

Show thesaturation pressure corresponding to temperature as in Table (5).

Temperature

T(°C)

Saturation pressure

Psat(kPa)

25 (x1)3.1698 (y1)
26 (x2)(y2=?)
30 (x3)4.2469 (y3)

Use excels and tabulates the values from Table (5) in Equation (III) to get,

Psat@26°C=3.3638kPa

Substitute 0.01377 for ω1, 100kPa for P1 and 3.3638kPa for Psat@26°C in Equation (IV).

ϕ1=(0.01377)(100kPa)(0.622+0.01377)(3.3638kPa)=0.644=64.4%

Hence, the relative humidity is 64.4%.

(c)

Expert Solution
Check Mark
To determine

The dew point temperature.

Answer to Problem 29P

The dew point temperature is 18.8°C.

Explanation of Solution

Express initial partial pressure of water vapor.

Pν1=ϕ1Pg1=ϕ1Psat@26°C (V)

Express the dew point temperature

Tdp=Tsat@Pν (VI)

Conclusion:

Substitute 0.644 for ϕ1 and 3.3638kPa for Psat@26°C in Equation (V).

Pν1=(0.644)(3.3638kPa)=2.166kPa

Substitute 2.166kPa for Pν1 in Equation (VI).

Tdp=Tsat@2.166kPa (VII)

Here, saturation pressure at pressure of 2.166kPa is Tsat@2.166kPa.

Refer Table A-4, “saturated water-temperature table”, and write temperature at saturation pressure of 2.166kPa using an interpolation method.

Show thetemperature corresponding to saturation pressure as in Table (6).

Saturation pressure

Psat(kPa)

Temperature

T(°C)

1.7057 (x1)15 (y1)
2.166 (x2)(y2=?)
2.3392 (x3)20 (y3)

Use excels and tabulates the values from Table (6) in Equation (III) to get,

Tsat@2.166kPa=18.8°C

Substitute 18.8°C for Tsat@2.166kPa in Equation (VII).

Tdp=18.8°C

Hence, the dew point temperature is 18.8°C.

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Chapter 14 Solutions

Thermodynamics: An Engineering Approach

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