Chapter 8 Balances on Nonreactive Processesshoukat.buet.ac.bd/psychrometricchart.pdf ·...

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Chapter 8 Balances on Nonreactive Processes PSYCHROMETRIC CHART

Transcript of Chapter 8 Balances on Nonreactive Processesshoukat.buet.ac.bd/psychrometricchart.pdf ·...

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Chapter 8Balances on Nonreactive Processes

PSYCHROMETRIC CHART

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Figure 8.4-1 (p. 385)

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Terminologies

• Absolute Humidity• % Relative Humidity• % Relative Humidity • Dew Point

H id V l• Humid Volume• Dry-bulb Temperature

b lb• Wet-bulb Temperature• Specific Enthalpy of Saturated Air (Enthalpy

D i ti t b id d)Deviation to be considered)

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• Absolute Humidityrefers to the kg water (vapor)

ah =moisture content of air

kg DAah

• Relative HumidityRatio of partial 1002H O

*rp

h = ×Ratio of partial pressure to vapor of liquid at gas t t d

2*H O( )

rp T

% RH f (T P)temperature and pressure

% RH = f (T, P)

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Dew Point Temperature

• Temperature at which water vapor starts to condense out of the air– water vapor starts to condense out of the air

– air becomes completely saturated– humid air becomes saturated if it is cooled athumid air becomes saturated if it is cooled at

constant temperature– first liquid droplet forms

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Dry Bulb Temperature

• The Dry Bulb Temperature refers basically to the ambient air temperaturethe ambient air temperature

• It is called "Dry Bulb" because the air temperature is indicated by a thermometertemperature is indicated by a thermometer not affected by the moisture of the air

• Dry-bulb temperature can be measured usingDry bulb temperature can be measured using a normal thermometer freely exposed to the air but shielded from radiation and moisture

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Wet Bulb Temperature

• Function of temperature and humidityy

• Hygrometers are instruments comprising both wet-bulb and d b lb the momete sdry-bulb thermometers

• Temperature shown when environment just adjacent to j jbulb is just saturated

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Hygrometer

Hygrometer by masons

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• Humid Volume - Volume occupied by (1 Kg DA + ha kg water vapor that accompanies it)DA + ha kg water vapor that accompanies it)

• Specific Enthalpy of saturated air: Reference state: liquid water and air both atReference state: liquid water and air both at 0 oC and 1 atm.

• Enthalpy deviation: For enthalpy of non-• Enthalpy deviation: For enthalpy of nonsaturated air, enthalpy deviation must be added to the enthalpy of saturated air.py

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Psychrometric chart• plot of several properties of a gas-vapor mixture

– Air – Water system at 1 atm : Figure 8.4-1• DOF• DOF

– F = C – P + 2 = 2 –1 + 2 = 3 – P : 1 atm for pychrometric chart – Other 2 varibles :

• Tdb and Twb

• Tdb or h• Tdb or hr , ….• How to read psychrometric chart ?

– 2 varibles needed to locate a point in the chart : • Tdb and Twb• Tdb or hr , ….

– H : add enthalpy deviation to the H at saturation

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H : add enthalpy deviation to the H at saturation• See example 8.4-5 for reading the psychrometric chart

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Figure 8.4-1 (p. 385)

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Psychrometric Chart

EnthalpyWet Bulb &Saturation Curve

G

A Absolute

D

Dew Point E

pyF G

A AbsoluteHumidity Axis

DRelative

Dew Point E

B Specific VolumeC Dry Bulb Axis

RelativeHumidity

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Dry Bulb Axis

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Psychrometric Chart / Humidity Chart

TYH

UM

IDIT

LUTE

H

DEWPOINT

AB

SO

Ref. state

H2O (L, 00C, 1 atm)

DRY BULB TEMPERATURE Dry Air (00C, 1 atm)

F =??

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Example 8.4-5

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Figure 8.4-1 (p. 385)

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Figure 8.4-2 (p. 386)

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• For a saturated air, the dry – bulb, wet – bulb and dew – point temperature are identical.

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CT – 3Tuesday (10/7/2012) at 1 pmTuesday (10/7/2012) at 1 pmSyllabus: Chapter 8O B kOpen Book

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8.4e Adiabatic Humidification

• Adiabatic humidificationevaporation of a liquid into gas-liquid mixture– evaporation of a liquid into gas-liquid mixture

– latent heat required to evaporate liquid is provided by the sensible heat lost by the gas phase.

– drying of solid product– production of humid air

• For air-water system, adiabatic saturation curve coincide with the constant wet-bulb t t litemperature line.

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Adiabatic Cooling

• Spray cooling, spray humidification• Spray dehumidification• Spray dehumidification• Drying

S d ivisit visit

• Spray drying

l 8 d b h d f

Unit Operation LabUnit Operation Lab

Example 8.4-7: adiabatic humidification

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During evaporative cooling the wet bulb• During evaporative cooling the wet bulb temperature remains constant.

• Cooling with humidification• Cooling with humidification

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Heating with Humidification

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Cooling with Dehumidification

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Example 8.4-6

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Figure 8.4-2 (p. 386)

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Class Test - 3A continuous rotary dryer is used to dry wet wood chips. The dryer operates at 1 atm pressure. The wet chips containing 42 wt% water enter the dryer at 20 oC and when leave the dryer the moisture content must be less than 10%. Hot dry air at 100 oC is fed to the dryer. The dry bulb temperature of the exiting air is found to be 38 oC and the wet bulb temperature is 30 oC.The air exits from the dryer at a rate of 14 m3 / Kg of wet chips entering the dryer.

• Draw a block diagram of the process and completely label it.• Calculate the moisture content of the exiting chips and check• Calculate the moisture content of the exiting chips and check

whether it meets the design specification, i.e., the moisture content is less than 10%.If th d i ti di b ti ll h t i th it• If the dryer is operating adiabatically, what is the exit temperature of the dry chips. Given: Specific heat of bone dry wood chips is 2 kJ/(kg oC), specific heat of liquid water is 4.18

fkJ/(kg oC) and the molecular weight of air 29. Show all steps clearly (include input - output enthalpy table). 34

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