Question 11.181E: A commercial laundry runs a dryer that has an exit flow of 1...

A commercial laundry runs a dryer that has an exit flow of 1 lbm/s moist air at 120 F, 70% relative humidity. To save on the heating cost a counterflow stack heat exchanger is used to heat a cold water line at 50 F for the washers with the exit flow, as shown in Fig. P11.105. Assume the outgoing flow can be cooled to 70 F. Is there a missing flow in the figure? Find the rate of energy recovered by this heat exchanger and the amount of cold water that can be heated to 85 F.

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Dryer oulet,   1: 120  F,  \Phi = 70%

\begin{gathered}\Rightarrow h _{ g 1}=1113.54   Btu / lbm \\P _{ g 1}=1.695   psia \\P _{ v1 }=0.7 \times 1.695   psia =1.1865   psia \\\omega_{1}=\frac{0.622 \times 1.1865}{14.7-1.1865}=0.0546\end{gathered}

State 2:      T _{2}< T _{ dew 1} \approx 107   F \text { so } \Phi_{2}=100 \% . P _{ g 2}=0.363   psia , h _{ g 2}=1092.04  Btu/lbm

h _{ f 2}=38.09   Btu / lbm , \quad \omega_{2}=0.622 \times 0.363 /(14.7-0.363)=0.01575

Continuity Eq. water 1-2 line:    \dot{ m }_{ a } \omega_{1}=\dot{ m }_{ a } \omega_{2}+\dot{ m }_{ liq } ; \quad \dot{ m }_{ liq }=\dot{ m }_{ a }\left(\omega_{1}-\omega_{2}\right)

The mass flow rate of dry air is

\dot{ m }_{ a }=\dot{ m }_{\text {moist air }} /\left(1+\omega_{1}\right)=1   lbm / s /(1+0.0546)=0.948   lbm / s

The heat out of the exhaust air which also equals the energy recovered becomes

\begin{aligned}\dot{ Q }_{ CV }=& \dot{ m }_{ a }\left[ C _{ p a }\left( T _{1}- T _{2}\right)+\omega_{1} h _{ g 1}-\left(\omega_{1}-\omega_{2}\right) h _{ f 2}-\omega_{2} h _{ g 2}\right] \\=& 0.948[0.24(120-70)+0.0546 \times 1113.54-0.03885 \times 38.09\\&\quad-\quad 0.01575 \times 1092.04] \\=& 0.948   lbm / s \times 54.12   Btu / lbm = 5 1 . 3   Btu / s\end{aligned}

 

\dot{ m }_{ liq }=\dot{ Q }_{ CV } /\left( C _{ P  liq}  \Delta T _{ liq }\right)=51.3 /[1.0(85-50)]= 1 . 4 6 6   lbm / s

 

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