Mass Transfer - Video Lectures
Topic outline
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Announcements Forum
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Humidity Chart Page
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Relation between Percentage and Relative Humidities Page
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Mixing Air of Different Relative Humidities Page
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Effect of Heating and Adiabatic Cooling Page1988-5-b-vi-mtAir with a dry bulb temperature \(t_{d1}\) and a wet bulb temperature \(t_{w1}\) is passed through a heater and then through an adiabatic cooler from which it emerges with dry and wet bulb temperatures of \(t_{d2}\) and \(t_{w2}\) respectively. Then
- always \(t_{w1} > t_{w2} \mbox { and } t_{d1} > t_{d2}\)
- always \(t_{w1} < t_{w2} \mbox { and } t_{d1} > t_{d2}\)
- always \(t_{w1} > t_{w2} \mbox { and } t_{d1} < t_{d2}\)
- \(t_{w1} < t_{w2} \mbox { and } t_{d1} \mbox { can be greater than, equal to or less than } t_{d2}\)
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Relative Humidity from Dewpoint and Vapor Pressure Data Page1994-9-mtAir at 30\(^\circ\)C and 150 kPa in a closed container is compressed and cooled. It is found that the first droplet of water condenses at 200 kPa and 15\(^\circ\)C. Calculate the percent relative humidity of the original air. The vapor pressures of water at 15\(^\circ\)C and 30\(^\circ\)C are 1.7051 kPa and 4.246 kPa respectively.
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Change in Relative Humidity of Air due to Heating Page
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Dry Bulb, Wet Bulb and Dew Point Temperatures Page2003-67-mtThe following plot gives the saturated humidity (\(H_e\)) versus Temperature (\(T\)).
Line joining \((H_1,T_1)\) and \((H_2,T_2)\) is the constant enthalpy line. Choose the correct one.- \(T_1\) - Dew point Temp; \(T_2\) - Dry bulb Temp; \(T_3\) - Wet bulp Temp.
- \(T_1\) - Dew point Temp; \(T_2\) - Wet bulb Temp; \(T_3\) - Wet bulp Temp.
- \(T_1\) - Wet bulb Temp; \(T_2\) - Dry bulb Temp; \(T_3\) - Dew point Temp.
- \(T_1\) - Dry bulb Temp; \(T_2\) - Wet bulb Temp; \(T_3\) - Dew point Temp.
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2004-21-22-mtAn air-water vapor mixture has a dry bulb temperature of 60oC and a dew point temperature of 40oC. The total pressure is 101.3 kPa and the vapor pressures of water at 40oC and 60oC are 7.30 kPa and 19.91 kPa, respectively.
- The humidity of air sample expressed as kg of water vapor/kg of dry air is _____ (0.048 / 0.079 / 0.122 / 0.152)
- The wet bulb temperature \(T_w\) for the above mixture would be ______
- less than 40oC
- 40oC
- 40oC < T_w < 60oC
- 60oC
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Constant Pressure Heating of Air Page1989-5-ii-e-f-mtAir is passed through a heater at constant pressure. The inlet and outlet conditions of the air are as follows:
Inlet:
Dry bulb temperature = 31.7\(^\circ \)C
Wet bulb temperature = 23.9\(^\circ \)C
Humidity = 30%
Outlet:
Dry bulb temperature = 70\(^\circ \)C-
The inlet air will have a dew point
- Equal to 23.9\(^\circ\)C
- Between 23.9\(^\circ\)C and 31.7\(^\circ\)C
- Greater than 31.7\(^\circ\)C
- Less than 23.9\(^\circ \)C
- In the above problem, the air from the heater will have a humidity:
- Equal to 30%
- Greater than 30%
- Less than 30%
- None of the above
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The inlet air will have a dew point
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Humid Volume of Air - Water-vapor Mixture PageAG-2019-25Air-water vapor mixture at 1 atmosphere pressure has 0.035 kg water vapor per kg dry air, and dry bulb temperature of 37oC. The value of Universal gas constant is 8.314 kJ/(kmol.K). The humid volume of this air-water vapor mixture in m3/kg dry air (rounded off to three decimal places) is ___________.
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Humid Heat of Gas Page1999-2-11-mtIf the specific heats of a gas and vapor are 0.2 kJ/kg.K and 1.5 kJ/kg.K respectively, and the humidity is 0.01, the humid heat in kJ/kg.K is _____ (0.017 / 0.107 / 0.215 / 0.310)
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Adiabatic Saturation of Air Page
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Humidity of Air from Wet-bulb Depression Data Page
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Enthalpy of Air from Psychrometric Ratio Page
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Mass and Energy Balances on Humid Air Page
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Dry-Bulb Temperature of Air from Wet-Bulb Temperature Data Page2000-11-mtAir at 1 atm is blown past the bulb of a mercury thermometer. The bulb is covered with a wick. The wick is immersed in an organic liquid (molecular weight = 58). The reading of the thermometer is 7.6\(^\circ\)C. At this temperature, the vapor pressure of the liquid is 5 kPa. Find the air temperature (in \(^\circ\)C), given that the ratio of heat transfer coefficient to the mass transfer coefficient (psychrometric ratio) is 2 kJ/kg.K and the latent heat of vaporization of the liquid is 360 kJ/kg. Assume that the air, which is blown, is free from the organic vapor.
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