Consider moist air with absolute humidity of 0.02 (kg moisture)/(kg dry air) at 1 bar pressure. The vapour pressure of water is given by the equation
$\ln P^{sat} = 12 - \frac{4000}{T-40}$
where $P^{sat}$ is in bar and $T$ is in K. The molecular weight of water and dry air are 18 kg/kmol and 29 kg/kmol, respectively. The dew temperature of the moist air is ____________ °C (rounded off to the nearest integer).
The dew point temperature is the temperature at which the air becomes saturated with water vapor, meaning the partial pressure of the water vapor ($P_v$) equals the saturation vapor pressure ($P^{sat}$) at that temperature.
Use the formula for absolute humidity ($\omega$):
$ \omega = \frac{M_w}{M_a} \times \frac{P_v}{P_{total} - P_v} $
Where:
Rearranging the formula to solve for $P_v$:
$ P_v = \frac{\omega \times P_{total}}{\omega + \frac{M_w}{M_a}} $
Substitute the values:
$ P_v = \frac{0.02 \times 1}{0.02 + \frac{18}{29}} $
Calculate the ratio $\frac{M_w}{M_a}$:
$ \frac{18}{29} \approx 0.6207 $
Now calculate $P_v$:
$ P_v = \frac{0.02}{0.02 + 0.6207} = \frac{0.02}{0.6407} \approx 0.03121 \text{ bar} $
At the dew point, the partial pressure $P_v$ is equal to the saturation pressure $P^{sat}$.
Use the given saturation vapor pressure equation:
$ \ln P^{sat} = 12 - \frac{4000}{T - 40} $
Set $P^{sat} = P_v = 0.03121$ bar and solve for $T$ (which will be $T_{dp}$ in Kelvin):
$ \ln(0.03121) = 12 - \frac{4000}{T_{dp} - 40} $
Calculate $\ln(0.03121)$:
$ \ln(0.03121) \approx -3.467 $
Substitute this back into the equation:
$ -3.467 = 12 - \frac{4000}{T_{dp} - 40} $
Rearrange to solve for $T_{dp} - 40$:
$ \frac{4000}{T_{dp} - 40} = 12 - (-3.467) = 15.467 $
$ T_{dp} - 40 = \frac{4000}{15.467} \approx 258.6 \text{ K} $
Solve for $T_{dp}$ in Kelvin:
$ T_{dp} = 258.6 + 40 = 298.6 \text{ K} $
Convert the dew point temperature from Kelvin to Celsius:
$ T_{dp}(°C) = T_{dp}(K) - 273.15 $
$ T_{dp}(°C) = 298.6 - 273.15 = 25.45 \text{ °C} $
Rounding the result to the nearest integer gives:
$ T_{dp} \approx 25 \text{ °C} $
This value lies between 23 and 27 °C.
| Temperature (in K) | 284 | 289 | 294 | 299 | 310 |
| Vapor pressure of water (in kPa) | 1.28 | 1.80 | 2.50 | 3.40 | 6.40 |
Partially saturated air at 1 bar and $50 ^{\circ}C$ is contacted with water in an adiabatic saturator. The air is cooled and humidified to saturation, and exits at $25^{\circ}C$ with an absolute humidity of 0.02 kg water per kg dry air. Use latent heat of vaporization of water as 2450 kJ. $kg^{-1}$, and average specific heat capacity for dry air and water, respectively as 1.01 kJ.$kg^{-1}K^{-1}$ and 4.18 kJ. $kg^{-1}K^{-1}$. If the absolute humidity of air entering the adiabatic saturator is $H \times 10^{-3}$ kg water per kg dry air, the value of $H$ is ________ (rounded off to two decimal places).
The dry-bulb temperature of air in a room is $30 \ \degree C$. The Antoine equation for water is given as
$ln \ P^{sat} = 12.00 - \frac{4000}{T-40}$
where $T$ is the temperature in $K$ and $P^{sat}$ is the saturation vapor pressure in $bar$. The latent heat of vaporization of water is $2000 \ kJ \ kg^{-1}$, the humid heat is $1.0 \ kJ \ kg^{-1} \ K^{-1}$, and the molecular weights of air and water are $28 \ kg \ kmol^{-1}$ and $18 \ kg \ kmol^{-1}$, respectively. If the absolute humidity of air is $Y' \ kg$ moisture per $kg$ dry air, then for a wet-bulb depression of $9 \ \degree C$, $1000 \times Y' = $ _________ (rounded off to one decimal place).
The humidity of air at a dry-bulb temperature of $65^{\circ}C$ is $0.025 \; kg \; water/kg \; dry \; air$. The latent heat of vaporization of water at $0 ^{\circ}C$ is $2500 \; kJ/kg$. The psychrometric ratio of air is $0.95 \; kJ \; (kg \; dry \; air)^{-1} \; K^{-1}$. Considering $0 ^{\circ}C$ as reference temperature, the enthalpy of air (in kJ/kg) at its adiabatic saturation temperature of $35 ^{\circ}C$ is ________ (rounded off to two decimal places).