Question

Air at 45O​C (dry bulb) and 10% relative humidity is to be humidified adiabatically to 70%...

Air at 45O​C (dry bulb) and 10% relative humidity is to be humidified adiabatically to 70% relative humidity.

(a) Use the psychrometric chart to estimate the adiabatic saturation temperature of the air.

(b) Estimate the final temperature of the air and the rate at which water must be added to humidify 15 kg/min of the entering air.

(c) What have you assumed in carrying out this calculation?

Homework Answers

Answer #1

a) From the psycometric chart, the adiabatic saturation temperature for air at Dry bulb = 45C and 10% Relative humidity(RH) is Twet bulb =Twb= 21 C

Absolute humidity under these condition = 0.006 Kg H2O/Kg dry air

b) The absolute humidity of exit gas determined from the chart under the following conditions:

Twb = 21 C and RH = 70%

i.e the intersection of the Twb and RH curve leading to the absolute humidity value = 0.014 Kg HO/Kg dry air

Find flow rate of inlet Dry air = 15 /1.0026 = 14.96 kg dry air/min

Amount of water that must be evaporated = 14.96 (0.014-0.006) = 0.119 Kg H2O/min

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
The air in a building has a dry bulb temperature of 72F and 50% relative humidity....
The air in a building has a dry bulb temperature of 72F and 50% relative humidity. Final dry bulb should be 65F and a relative humidity of 40%. The building is 60’ long, 45’ wide, and has a 12’ ceiling. Find the quantity of water required to raise the relative humidity to 65%
Air at 1oC dry bulb and 80% percentage saturation mixes adiabatically with air at 18oC dry...
Air at 1oC dry bulb and 80% percentage saturation mixes adiabatically with air at 18oC dry bulb, 40% percentage saturation, in ratio of 1 to 3 by volume. Calculate the temperature and percentage saturation of the mixture. Take the barometric pressure at 1.01325 bar.
An air-water vapor mixture containing 20% ​​humidity at a dry thermometer temperature of 40 ° C...
An air-water vapor mixture containing 20% ​​humidity at a dry thermometer temperature of 40 ° C A tunnel is fed to the dryer by being heated to 70 ° C. Red pepper samples It is dried in adiabatic conditions. Leave the dryer system saturated For the mixing air-water vapor mixture, find the following. a) 10000 m3 of moist air at 40 ° C (air-water vapor mixture) warmth Required heat to increase to 70 ° C b) Air temperature at dryer...
Compare the sea level relative humidity, enthalpy, specific volume, wet-bulb temperature, and dew point using (a)...
Compare the sea level relative humidity, enthalpy, specific volume, wet-bulb temperature, and dew point using (a) steam tables and ideal gas mixture relations and (b) the psychrometric chart for the following conditions: (a) 16°C dry-bulb, W = 0.001. (b) 32°C dry-bulb, W = 0.002. (c) 32°c dry-bulb, W = 0.001.
In a low temperature drying system, air at 60°C and 10% Relative humidity passes over a...
In a low temperature drying system, air at 60°C and 10% Relative humidity passes over a bed of diced carrots at 20 kg-dry air/sec. The rate of water removal from the carrots Is measured by difference in total weight over time and found to be approximately .16 kg-water/sec. In the system described above, calculate the temperature and relative humidity of the air exiting the drying system.
Problem #2 Air at 80°F and 80% relative humidity are cooled to 51°F at a constant...
Problem #2 Air at 80°F and 80% relative humidity are cooled to 51°F at a constant pressure of 1 atm. Use the psychrometric chart to calculate the fraction of water that condenses, and the rate at which heat must be removed to deliver 1,000 ft3 /min of humid air at the final conditions.
Air at 95°F, 1 atm, and 10% relative humidity enters an evaporative cooler operating at steady...
Air at 95°F, 1 atm, and 10% relative humidity enters an evaporative cooler operating at steady state. The volumetric flow rate of the incoming air is 1765 ft3/min. Liquid water at 68°F enters the cooler and fully evaporates. Moist air exits the cooler at 70°F, 1 atm. There is no significant heat transfer between the device and its surroundings and kinetic and potential energy effects can be neglected. a)Determine the mass flow rate of the dry air in lb(dry air)/min....
Air from outside (5 deg-C, 50% relative humidity) is heated by an electrical heater to a...
Air from outside (5 deg-C, 50% relative humidity) is heated by an electrical heater to a temperature of 35 deg-C at a mass flow rate of 10 kg/s (dry air). Determine the relative humidity of the conditioned air at the exit
Air at T1 = 32°C, p1 = 1 bar, 50% relative humidity enters an insulated chamber...
Air at T1 = 32°C, p1 = 1 bar, 50% relative humidity enters an insulated chamber operating at steady state with a mass flow rate of 3 kg/min and mixes with a saturated moist air stream entering at T2 = 7°C, p2 = 1 bar. A single mixed stream exits at T3 = 17°C, p3 = 1 bar. Neglect kinetic and potential energy effects A) Determine mass flow rate of the moist air entering at state 2, in kg/min. (Answer...
Atmosphric air at 40 F and 50% relative humidity enters the heating section of an airconditioning...
Atmosphric air at 40 F and 50% relative humidity enters the heating section of an airconditioning device at a volumetric flow rate of 100ft^3/min. Water vapor is added to the heated air to increase the relative humidity to 55%. The temperature after the heating section is 72F and the temperature at the exit is 74F. Using the appropriate fomulas: a) determine the rate of the heat transfer in Btu/min. b) determine the mass flow of water vapor in lbm/min.