| 2D-6 : |
Humidity and Partial Pressure in a Humid Ideal Gas |
6 pts |
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| An unknown amount of water and 5 kg of a non-condensable gas (Molecular Weight = 40) are produced in an industrial plant at a temperature of 70oC. These products are sent to a rigid storage tank. The pressure and relative humidity in the tank are 2 atm and 65% respectively. Determine the mass of water present in the tank. Assume that the gas behaves as an ideal gas. |
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| Given: |
mNCG = |
5 |
kg NCG |
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MWNCG = |
40 |
g NCG / mole NCG |
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T = |
70 |
oC |
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Ptot = |
2 |
atm = |
202.7 |
kPa |
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hr = |
65% |
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| Find: |
mH2O = |
??? |
kg |
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| Assumption: |
The gas in the tank behaves as an ideal gas. |
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| Solution : |
Let's begin with the definition of relative humidity: |
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Eqn 1 |
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The vapor pressure is equal to the saturation pressure at the system temperature. |
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We can find this in the saturation temperature section of the steam tables: |
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P*H2O (70oC) = |
31.19 |
kPa |
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Plug P*H2O and hr into Eqn 1 to get the partial pressure of water from the definition of relative humidity. |
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PH2O = |
20.274 |
kPa |
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For an ideal gas: |
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PH2O = yH2O Ptot |
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Eqn 2 |
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or: |
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Eqn 3 |
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yH2O = |
0.100 |
mol H2O / mol gas |
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For all gases, mole fraction is defined as: |
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Eqn 4 |
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Where : |
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ni = mi / MWi |
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Eqn 5 |
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Now, we solve Eqn 4 for nH2O : |
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Eqn 6 |
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Eqn 7 |
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Now, we can plug the numbers into equations… |
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Eqn 5 yields : |
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nNCG = |
125 |
moles NCG |
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Eqn 7 yields : |
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nH2O = |
13.90 |
moles H2O |
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Finally, Eqn 5 can be rewritten as : |
mi = ni MWi |
Eqn 8 |
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We can answer the question posed by plugging numbers into Eqn 8 : |
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Data: |
MWH20 = |
18.016 |
g H2O / mol H2O |
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mH2O = |
250 |
g H2O |
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