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CAE 331/513 Building Science Fall 2014 Week 6: September 30, 2014 HVAC thermodynamic and psychrometric processes Dr. Brent Stephens, Ph.D. Civil, Architectural and Environmental Engineering Illinois Institute of Technology [email protected] Advancing energy, environmental, and sustainability research within the built environment www.built-envi.com Twitter: @ built_envi
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CAE 331/513 Building Science - The Built Environment …built-envi.com/wp-content/uploads/2014/07/cae331_513… ·  · 2015-03-05CAE 331/513 Building Science Fall 2014 Week 6: September

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Page 1: CAE 331/513 Building Science - The Built Environment …built-envi.com/wp-content/uploads/2014/07/cae331_513… ·  · 2015-03-05CAE 331/513 Building Science Fall 2014 Week 6: September

CAE 331/513 Building Science Fall 2014 Week 6: September 30, 2014 HVAC thermodynamic and psychrometric processes

Dr. Brent Stephens, Ph.D. Civil, Architectural and Environmental Engineering

Illinois Institute of Technology [email protected]

Advancing energy, environmental, and sustainability research within the built environment www.built-envi.com Twitter: @built_envi

Page 2: CAE 331/513 Building Science - The Built Environment …built-envi.com/wp-content/uploads/2014/07/cae331_513… ·  · 2015-03-05CAE 331/513 Building Science Fall 2014 Week 6: September

ASHRAE Scholarships

•  8 regional/chapter and university-specific scholarships –  $3,000 to $5,000 each

•  12 undergraduate engineering scholarships –  $3,000 to $10,000 each

2

www.ashrae.org/scholarships

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HW 3 – Psychrometrics chart

•  Due Thursday

3

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Revisit example from last class

Moist air exists at 22°C dry-bulb temperature with 50% RH

Find the following: (a) the humidity ratio, W (b) dew point temperature, Tdew (c) wet-bulb temperature, Twb

(d) enthalpy, h (e) specific volume, ν (f) density, ρ

4

Also: (g) degree of saturation, µ

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Psychrometric equations

5

φ =pwpws

ln pws =C8T+C9 +C10T +C11T

2 +C12T3 +C13 lnT

W = 0.622pwp− pw

µ =WWs

Dew point temperature:

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Psychrometric equations

6

W =(2501− 2.326Twb )Ws@Twb

−1.006(T −Twb )2501+1.86T − 4.186Twb

= actual W

Wet bulb temperature (iterative solver):

v = RdaTp− pw

=RdaT (1+1.6078W )

pv ≈ 0.287042(T + 273.15)(1+1.6078W ) / p

ρ =mda +mwV

=1v1+W( )

*where T is in °C

h ≈1.006T +W (2501+1.86T )

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•  d

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Relative Humidity φ ≈ 50%

Dry Bulb Temp T = 22°C

Dew Point Temp Tdew ≈ 11.7°C

Wet Bulb Temp Twb ≈ 15.5°C

Humidity Ratio W ≈ 8.2 g/kgda

(i.e., 0.0082 kg/kg)

Enthalpy h ≈ 44 kJ/kgda

Specific Volume v ≈ 0.848 m3/kgda

Density ρ ≈ 1/v ≈ 1.18 kgda/m3

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Revisit another example from two classes ago

Moist air exists at 30°C dry-bulb temperature with a 15°C dew point temperature

Find the following: (a) the humidity ratio, W (b) wet-bulb temperature, Twb

(c) enthalpy, h (d) specific volume, ν (e) relative humidity, ϕ

8

Also: (f) degree of saturation, µ (g) density, ρ

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Dew Point Temp Tdew ≈ 15°C

Dry Bulb Temp T = 30°C

Wet Bulb Temp tb≈ 20°C Humidity Ratio

W ≈ 10.7 g/kgda (i.e., 0.0107)

Enthalpy h ≈ 58 kJ/kgda

Specific Volume v ≈ 0.875 m3/kgda

Relative Humidity φ ≈ 40%

Saturation W Ws ≈ 0.27 kgw/kgda

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Humidity ratio

•  For a known Tdew = 15°C, we know that the actual humidity ratio in the air, W, is by definition the same as the saturation humidity ratio, Ws, at an air temperature of 15°C

W = 0.622pwp− pw @T=30°C

W@T=30°C =Ws@T=15°C = 0.622pwsp− pws @T=15°C

pws@15C = 1.7057 kPa

W@T=30°C =Ws@T=15°C = 0.6221.7057

101.325−1.7057= 0.01065

kgwkgda

Assume p = 101.325 kPa (sea level)

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Degree of saturation

•  Need the saturation humidity ratio @ T = 30°C:

11

µ =WWs

!

"#

$

%&@T=30°C

Ws@T=30°C = 0.622pwsp− pws @T=30°C

pws@15C = 4.2467 kPa

Ws@T=30°C = 0.6224.2467

101.325− 4.2467= 0.02720

kgwkgda

µ =WWs

=0.010650.02720

= 0.39

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Relative humidity

•  From previous:

12

φ =pwpws

pw@T=30°C = pws@T=15°C =1.7057kPa

pws@T=30°C = 4.2467kPa

φ =1.70574.2467

= 0.40 = 40%

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Enthalpy

13

*where T is in °C

h ≈1.006T +W (2501+1.86T )

h ≈1.006(30)+ (0.01065)(2501+1.86(30)) = 57.4 kJkg

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Specific volume and density

14

v ≈ 0.287042(T + 273.15)(1+1.6078W ) / p

v ≈ 0.287042(30+ 273.15)(1+1.6078(0.01065)) / (101.325)

v ≈ 0.873 m3

kgda

ρ =1v1+W( ) = 1

0.8731+0.01065( ) =1.157 kgm3

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Wet-bulb temperature

•  Wet-bulb temperature is the Twb that fits this equation:

Procedure: •  Guess Twb, calculate pws for that T, calculate Ws for that T

–  Repeat until W calculated based on those values (and original T) in equation above is equal to actual W (0.01065 in our case)

15

W =(2501− 2.326Twb )Ws@Twb

−1.006(T −Twb )2501+1.86T − 4.186Twb

= 0.01065

Ws@Twb=?= 0.622

pwsp− pws @Twb=?

where: T = 30°CTwb = ?°C

Twb = 20.1°C

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•  d

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Dew Point Temp Tdew ≈ 15°C

Dry Bulb Temp T = 30°C

Wet Bulb Temp tb≈ 20°C Humidity Ratio

W ≈ 10.7 g/kgda (i.e., 0.0107)

Enthalpy h ≈ 58 kJ/kgda

Specific Volume v ≈ 0.875 m3/kgda

Relative Humidity φ ≈ 40%

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PSYCHROMETRIC PROCESSES

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Use of the psychrometric chart for processes

We can use the psychrometric chart not only to describe states of moist air, but for a number of processes that are important for building science and HVAC applications

Examples: •  Sensible cooling or heating •  Warming and humidification of cold, dry air •  Cooling and dehumidification of warm, humid air

–  Sensible + latent cooling

•  Evaporative cooling •  Mixing of airstreams

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Page 19: CAE 331/513 Building Science - The Built Environment …built-envi.com/wp-content/uploads/2014/07/cae331_513… ·  · 2015-03-05CAE 331/513 Building Science Fall 2014 Week 6: September

Typical commercial HVAC system air handler

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Supply air

Fan

Heating coil Cooling coil Filters

Mixed RA + OA

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Typical forced air distribution system

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Common processes: •  Air mixing •  Heating •  Cooling •  Dehumidification •  Humidification

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Sensible and latent heat

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•  Sensible heat transfer –  Increases or decreases temperature of

a substance without undergoing a phase change

•  Latent heat transfer –  Heat transfer required to change the

phase of a substance (e.g., heat req’d to change liquid to vapor)

Qtotal

=Qsensible

+Qlatent

Qtotal

= mair (hexit − hinlet )

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Sensible heat transfer equation

22

Qsens

= mcp(Texit−T

inlet)= Vρc

p(Texit−T

inlet)

Qsens =Rate of sensible heat xfer [Btu/hr or ton or W]

m =mass rate of air flow [lbm/hr or kg/s]V = volumetric flow rate of air [ft3 /hr or cfm or m3 /s]

ρ = density of air [lbm/ft3 or kg/m3]cp = specific heat of air [Btu/(lbm-F) or J/(kg-K)]

Texit ,Tinlet = exit and inlet temperature [°F or °C]

Qsens > 0 for heating

Qsens < 0 for cooling

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Latent heat transfer equation

23

Qlat= !m

whfg

Qlat = rate of latent heat transfer [Btu/hr or ton or W]

Qlat is positive for humidification processes

!mw = rate of evaporation/condensation [lbm/hr or kg/s]

hfg = enthalpy of vaporization [Btu/lbm or J/kg]

also called latent heat of vaporization (hfg = 2260 kJ/kg for water)

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Heating and humidification of cold, dry air

•  Example: Heating and humidifying coils –  Process: Adding moisture and heat (sensible + latent heating)

24

8°C 40% RH 45°C

30% RH

Q1: What is the enthalpy change required? Q2: What is the split between sensible and latent load?

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•  d

25

2

1

Warming and humidification of cold, dry air

ΔW

Δhtotal

ΔT

Δhsensible = 46 - 16 = 30 kJ/kgda Δhtotal = 64 - 16 = 48 kJ/kgda

Δhsensible

SHR = 30/48 = ~0.62

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Sensible heat ratio (SHR)

•  The sensible heat ratio is defined as:

•  Allows for understanding sensible load relative to latent load

•  Typical SHR: 0.6 to 0.9

26

SHR =!qsens!qtotal

=!qsens

!qsens + !qlatent=ΔhsensΔhtotal

Here is a process with an SHR ≈ 0.4

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Cooling and dehumidification of warm, humid air

27

38°C 34% RH

13°C 90% RH

•  Example: Cooling coil •  Removing both moisture and heat

–  Sensible + latent cooling

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•  d

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1

2

Cooling and dehumidification of warm, humid air

ΔW

Δh SHR ~ 0.63

The red line is actually impossible… no moisture removal The blue line shows what really happens

ΔT

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Example: Sensible cooling

•  Moist air is cooled from 40°C and 30% RH to 30°C –  Q1: Does the moisture condense? –  Q2: What is the RH at W at the process end point? –  Q3: What is the rate of sensible heat transfer if the airflow

rate is 1000 ft3/min?

29

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•  d

30

1

Sensible cooling

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•  d

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1 2

Dew point is ~19°C New T = 30°C •  No condensation New RH is ~53% W does not change W1 = W2 = 0.014 kgw/kgda

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•  d

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1 2

h1 ≈ 76 kJ/kg h2 ≈ 66 kJ/kg Δh ≈ -10 kJ/kg SHR = 1.0

Dew point is ~19°C New T = 30°C •  No condensation New RH is ~53% W does not change W1 = W2 = 0.014 kgw/kgda

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Example: Sensible + latent cooling

•  Moist air is cooled from 40°C and 30% RH to 15°C –  Q1: Does the moisture condense? –  Q2: What is RH at W at the process end point? –  Q3: What is the rate of heat transfer if the airflow rate is

1000 ft3/min?

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•  d

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1

Sensible + latent cooling

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1

2 Dew point is ~19°C New T = 15°C •  There is condensation New RH is 100% W decreases to ~0.010

Two part cooling process: 1.  Constant humidity ratio cooling until sat. 2.  Constant RH cooling w/ moisture condensation

Δh = 42 – 76 = -34 kJ/kg

Sensible + latent cooling

SHR ~ 0.75

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Real data: ASHRAE RP-1299 Energy implications of filters

36

0.008

0.010

0.012

0.014

Hum

idity

ratio

, kg/

kg

0

10

20

30Te

mpe

ratu

re, C

6 PM 7 PM 8 PMHour

Temp - before coil Temp - after coilW - before coil W - after coil

AC on AC off

Temperature and humidity ratio differences across AC coils in homes

T before coil

T after coil

W before

coil W

after coil

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Real data: ASHRAE RP-1299 Energy implications of filters

37

What are we looking at?

Before coil

After coil

AC on/off

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Real data: ASHRAE RP-1299 Energy implications of filters

38

0

20

40

60

80

100

RH

, %

18 19 20hod

RH - before coil RH - after coil

AC on AC off

Relative humidity differences across AC coils in homes

RH before

coil

RH after coil

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•  d

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1

Sensible + latent cooling

2

Δh = 35 – 52 = -17 kJ/kg SHR ~ 0.85

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Mixing of air streams

•  Often in HVAC systems we mix airstreams adiabatically –  Adiabatically = Without the addition or extraction of heat –  e.g. outdoor air mixed with a portion of return/recirculated air

•  For most parameters, the outlet conditions end up being the weighted-averages of the input conditions –  Dry bulb temperature –  Humidity ratio –  Enthalpy –  (not wet-bulb temperature or RH though)

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Mixing of airstreams example

•  Hot, humid outdoor air is mixed with recirculated indoor air at an outdoor air fraction of about 35% –  Q1: What is T, W, RH, and h at the mixed condition?

41

20°C 40% RH

40°C 30% RH

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•  d

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2

Mixing of airstreams

1

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•  d

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2

Mixing of airstreams

1

3

T3 =mda1T1 + mda2T2mda1 + mda2

W3 =mda1W1 + mda2W2

mda1 + mda2

h3 =mda1h1 + mda2h2mda1 + mda2

T3 =0.65(20)+ 0.35(40)

1.0= 27°C

W3 =0.65(6)+ 0.35(14)

1.0= 8.8 gw

kgda

h3 =0.65(34)+ 0.35(77)

1.0= 49 kJ

kgda

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Evaporative cooling example •  Hot, dry outdoor air is cooled with an evaporative cooler, or “swamp

cooler” –  Q1: What is RH and W of the supply air? –  Q2: Why would we choose this system?

44

32°C 20% RH

17°C ?? RH

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•  d

45

1

Evaporative cooling

?

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•  d

46

1

Evaporative cooling

2

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•  d

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1

Evaporative cooling

2 Cooling occurs along constant wet bulb

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1

Evaporative cooling

2

RH near 100% W = ~12.2 gw/kgda Δh = 0

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1

Evaporative cooling

2

RH near 100% W = ~12.2 gw/kgda Δh = 0

This means no energy is required other than for fans (for air) and pumps (for water)