Question 12.12: Analyzing a Steam-Spray Humidifier Moist air with a temperat...

Analyzing a Steam-Spray Humidifier

Moist air with a temperature of 22°C and a wet-bulb temperature of 9°C enters a steam-spray humidifier. The mass flow rate of the dry air is 90 kg/min. Saturated water vapor at 110°C is injected into the mixture at a rate of 52 kg/h. There is no heat transfer with the surroundings, and the pressure is constant throughout at 1 bar. Using the psychrometric chart, determine at the exit (a) the humidity ratio and (b) the temperature, in °C.

The Blue Check Mark means that this solution has been answered and checked by an expert. This guarantees that the final answer is accurate.
Learn more on how we answer questions.

Known Moist air enters a humidifier at a temperature of 22°C and a wet-bulb temperature of 9°C. The mass flow rate of the dry air is 90 kg/min. Saturated water vapor at 110°C is injected into the mixture at a rate of 52 kg/h.

Find Using the psychrometric chart, determine at the exit the humidity ratio and the temperature, in °C.

Schematic and Given Data:

Engineering Model

1. The control volume shown in the accompanying figure operates at steady state. Changes in kinetic and potential energy can be neglected and \dot{W}_{ cv }=0.

2. There is no heat transfer with the surroundings.

3. The pressure remains constant throughout at 1 bar. Figure A-9 remains valid at this pressure.

4. The moist air streams are regarded as ideal gas mixtures adhering to the Dalton model.

Analysis

a. The humidity ratio at the exit \omega_{2} can be found from mass rate balances on the dry air and water individually. Thus,

 

\dot{m}_{ a 1}=\dot{m}_{ a 2} (dry air)

 

\dot{m}_{ v 1}+\dot{m}_{ st }=\dot{m}_{ v 2} (water)

 

With \dot{m}_{ v 1}=\omega_{1} \dot{m}_{ a } \text {, and } \dot{m}_{ v 2}=\omega_{2} \dot{m}_{ a } \text {, where } \dot{m}_{ a } is the mass flow rate of the air, the second of these becomes

 

\omega_{2}=\omega_{1}+\frac{\dot{m}_{ st }}{\dot{m}_{ a }}

 

Using the inlet dry-bulb temperature, 22°C, and the inlet wet-bulb temperature, 9°C, the value of the humidity ratio \omega_{1} can be found by inspection of the psychrometric chart, Fig. A-9. The result is \omega_{1}=0.002 kg (vapor)/kg(dry air). This value should be verified as an exercise. Inserting values into the expression for \omega_{2}

 

\omega_{2}=0.002+\frac{(52 kg / h )|1 h / 60 min |}{90 kg / min }=0.0116 \frac{ kg (\text { vapor })}{ kg (\text { dry air })}

 

b. The temperature at the exit can be determined using an energy rate balance. With assumptions 1 and 2, the steady-state form of the energy rate balance reduces to a special case of Eq. 12.55. Namely,

 

0=\dot{Q}_{ cv }+\dot{m}_{ a }\left[\underline{\left(h_{ a 1}-h_{ a 2}\right)}+\underline{\omega_{1} h_{ g 1}+\left(\omega_{2}-\omega_{1}\right) h_{ w }-\omega_{2} h_{ g 2}}\right] (12.55)

 

0=h_{ a 1}-h_{ a 2}+\omega_{1} h_{ g 1}+\left(\omega_{2}-\omega_{1}\right) h_{ g 3}-\omega_{2} h_{ g 2} (a)

 

In writing this, the specific enthalpies of the water vapor at 1 and 2 are evaluated as the respective saturated vapor values, and h_{ g 3} denotes the enthalpy of the saturated vapor injected into the moist air.

Equation (a) can be rearranged in the following form suitable for use with the psychrometric chart.

 

1 \left(h_{ a }+\omega h_{ g }\right)_{2}=\left(h_{ a }+\omega h_{ g }\right)_{1}+\left(\omega_{2}-\omega_{1}\right) h_{ g 3} (b)

 

As shown on the sketch of the psychrometric chart, Fig. E12.12b, the first term on the right of Eq. (b) can be obtained from Fig. A-9 at the inlet state, defined by the intersection of the inlet dry-bulb temperature, 22°C, and the inlet wet-bulb temperature, 9°C; the value is 27.2 kJ/kg(dry air). The second term on the right can be evaluated using the known humidity ratios \omega_{1} \text { and } \omega_{2} \text { and } h_{ g 3} from Table A-2: 2691.5 kJ/kg(vapor). The value of the second term of Eq. (b) is 25.8 kJ/kg (dry air). The state at the exit is then fixed by \omega_{2} \text { and }\left(h_{ a }+\omega h_{ g }\right)_{2}=53 kJ/kg (dry air), calculated from the two values just determined. Finally, the temperature at the exit can be read directly from the chart. The result is T_{2} \approx 23.5^{\circ} C.

 

Alternative IT Solution

2 The following program allows T_{2} to be determined using IT, where \dot{m}_{ a } is denoted as mdota, \dot{m}_{ st } is denoted as mdotst, w1 and w2 denote \omega_{1} \text { and } \omega_{2}, respectively, and so on.

Using the Solve button, the result is T_{2}=23.4^{\circ} C, which agrees closely with the values obtained above, as expected.

1 A solution of Eq. (b) using data from Tables A-2 and A-22 requires an iterative (trial) procedure. The result is T_{2}=24^{\circ} C, as can be verified.

2 Note the use of special Moist Air functions listed in the Properties menu of IT.

Skills Developed

Ability to…

• apply psychrometric terminology and principles.

• apply mass and energy balances for a spray humidification process in a control volume at steady state.

• retrieve necessary property data using the psychrometric chart.

• apply IT for psychrometric analysis.

Quick Quiz

Using the psychrometric chart, what is the relative humidity at the exit? Ans. ≈63%.

12
12.1
12.2
The 'Blue Check Mark' means that either the MATLAB code/script/answer provided in the answer section has been tested by our team of experts; or the answer in general has be fact checked.

Learn more on how do we answer questions.

// Given data
T1 = 22 // °C
Twb1 = 9 // °C
mdota = 90 // kg/min
p = 1 // bar
Tst = 110 // °C
mdotst = (52 / 60) // converting kg/h to kg/min
// Evaluate humidity ratios
w1 = w_TTwb (T1,Twb1,p)
w2 = w1 + (mdotst / mdota)
// Denoting the enthalpy of moist air at
state 1 by
// h1, etc., the energy balance, Eq. (a),
becomes
0 = h1 − h2 + (w2 − w1)*hst
// Evaluate enthalpies
h1 = ha_Tw(T1,w1)
h2 = ha_Tw(T2,w2)
hst = hsat_Px(“Water/Steam”,psat,1)
psat = Psat_T(“Water/Steam ”,Tst)

Related Answered Questions