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Compact Heat Exchangersin HVAC systems
ASHRAE meeting in Mxico City 2009-01-13
Martin CronaAlfa Laval Lund AB
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Compact heat exchangers for HVAC
Heat transfer characteristics
Topics of the presentation
Content
Alfa Laval Slide 2
CHE in HVAC applications CHE Components
Design guidelines
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Compact heat exchangers
in HVAC systems
Enables high energy efficiency
Close temperature approach
Small temperature losses
Increased temperature drop
Fast response times at regulation Limited footprint
Compact design
High thermal efficiency
Easy service
Openable for mechanical cleaning
Expansion of capacity possible
Alfa Laval Slide 3
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Compact heat exchangers
Gasketed plate heat exchangers
Brazed Heat Exchan ers
Alfa Laval Slide 4
All-welded heat exchangers
Fusion bonded heat exchangers
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Compact heat exchanger
Alfa Laval Slide 5
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PHE basic components Carrying bar
Frame plate
Pressureplate
Plate packTightening bolts
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Gasketed plate heat exchanger
Pack of corrugated plates sealed by gaskets
Possible to open for cleaning and extension
Pressure range 0-30 barg
Alfa Laval Slide 7
Temperature range -25 C to 180 C Flexible connections sizes (20mm) to 500mm
Flexibility in plate and sealing material selection
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Brazed heat exchangers
BHE = Brazed Heat Exchanger
Compact design
Corru ated stainless steel
BHE - design
Frame plate
Connections
Alfa Laval Slide 8
plates Cupper as brazing material
Main use in heating andrefrigeration duties
Max temperature: 225C
Max pressure: 32 barg
Foil
Heat transferplate
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Fusion bonded heat exchanger
FHE = Fusion bonded Heat Exchanger Compact design
100% stainless steel
FHE - design
Alfa Laval Slide 9
n corruga es p a es
Stainless steel as bonding material
Max temperature: 550C
Max pressure 32 barg
Main use in ammonia and corrosivemedias
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All-welded heat exchanger Gasket free HE for high temperatures or
pressures
Many types exist
Plate types
Plate & Shell
Alfa Laval Slide 10
Openable block type
Spiral heat exchangers
Steam condensation is primaryapplication in HVAC
Welded HE main use is in chemicalindustry
Plate type
Plate & shell
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Compact heat exchangerCharacteristic
Feature PHE BHE FHE WHE
Flow / Capacity Connection size 20mm 500mm 20mm 100mm 20mm 100mm 50mm 250mm*
Temperature Max temperature 180C 225C 550C 300C*
Pressure Max designpressure
30barg 32barg 32 barg 60barg*
Serviceability Mechanical Yes No No No / partly*cleaning
Cost efficiency Cost ratio 3 1 2 4-5*
Risk of fatigue(only relevant in steamduties)
Fatigueresistance
Excellent OK OK OK*
Medias to use Corrosionresistance
Flexibility in plateor gasketmaterial
Limited bycupper
Limited bystainless steel
Flexible in platematerial
Primary HVAC applications -all duties withintemp andpressure range
-small capacities-clean medias-freon duties
-ammonia duties-tap water
-steamcondensation
Alfa Laval Slide 11
*depend on WHE type
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HVAC applications Cooling interchanger
Free cooling
Pressure breaker
Condensor protection
Ice stora e
District cooling
Heat recovery
Domestic hot water
Pool Solar heating
Alfa Laval Slide 12
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Efficient heat transfer
Cold fluid in at T2 In
Mass flowrate m2
Cold fluid out at T2 OutMass flowrate m2
Hot fluid in at T1 InMass flowrate m1
Definitions
Q = Heat load, kBTU/h (W)
(rate of heat transfer)
m = Mass flow rate, lb/s(kg/s)
Cp= Specific heat, J/kgC(the energy needed
1 Out
Mass flowrate m1
Heat released by the hot fluid: Q1=m1*Cp1*(T1 In-T1 Out)
Heat absorbed by the cold fluid: Q2=m2*Cp2*(T2 Out -T2 In)
No heat loss Q1 = Q2
Heat transfer equation Q=u*A*LMTD
Pressure drop P=k*v2
to heat 1 kg of the fluidwith 1C)
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Heat transferred in a HE
The temperature profile at one point of the plate wall
Wall
Flow direction
T1, Bulk temperature on hot side
Hot side
T
T3
T2, Bulk temperature on cold side
Flow direction
Cold side
More turbulence Thinner laminar film
Increased u-value
Better Heat Transfer
1/u = 1/hot + 1/cold + /
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Close temperature approach
Thermal definitions
Ex. T
Tcold,out
Cold water to chiller
Water to A/C in house
Thot,out
Water return from house
Thot,in
1
2
T,in
T,hot
Alfa Laval Slide 15
2
1ln
21
=LMTD
Cold water from chiller
,
LMTD
TTNTU
outcoldincold
coldcold
,,
==LMTD
TT=NTU
outhotinhot
hothot
,,
=
Higher NTU means more difficult heat transfer
LMTDs possible down to 1F
Normal NTU in HVAC Cooling 6-7
NTU in district cooling upto 9
Increased NTU means increased area
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Energy efficiency
Q = 1700 kBTU/h
47F
57F
45F
55F
47F
57FCOP = 3,4
80F
90F
78F
88F
Qcond = 2200 kBTU/h
50F
40F
Alfa Laval Slide 16
Qcool (kBTU/h)
LMTD (F)
Qchiller (kW)
Loss
Direct
1700
-
146-
PHE
1700
2
154-5%
S&T
1700
7
174-18%
High energy efficiency with PHE
Less loss on condensor side
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HE comparisonCompact heat exchangeradvantages
Smaller foot print
Less weight
Less fouling risk
6ft
5ft
Alfa Laval Slide 17
20ft
No fouling factor needed indesign
Small hold-up volume
Easier maintenance
Easier installation
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System optimization
47F
57F
45F
55F
58F 60F
46F
56F
Alfa Laval Slide 18
Q = u * A * LMTD
Smaller LMTD give larger heat exchanger
LMTD 2 down to 1 give A up 250%
Smaller pressure drop give larger heat exchanger
P down from 7 to 3,5 psig give A up 40%
Larger temperature drop enables smaller flow
3F larger T mean 25% smaller flow
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Energy savings with chiller by-pass
Q = 1700 kBTU/h
47F
60F
45F
58FCOP = 3,4
80F
90F
78F
88F
Qcond = 2200 kBTU/h
45F
58F
Alfa Laval Slide 19
Low temperatures in winter time for cooling source
Low wet bulb temperature in cooling towers
Low water temperature in water cooling
When cooling temperature go below A/C temperature
Chiller by-pass is possible
156 kW is saved
Pay-back often within 1-2 years
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Venice Casino in Las Vegas
Alfa Laval Slide 20
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PHE full serviceability Carrying bar
Frame plate
Pressureplate
Plate packTightening bolts
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Corrosion factorsIn cooling and heating there is with some water qualities riskof crevice corrosion and pitting corrosion.
Basic condition is that free oxygen and chlorides must bepresent and the corrosion risk depends on the factors below
Alfa Laval Slide 22
Factor Change Influence
Chloride content
Temperature
pH Level
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Plate - materials Standard materials and typical uses AISI 304
Typically in clean water-water duties
Example, up to 50 ppm chlorides at 50C
AISI 316
Typically in water-water duties
254 SMO (high-alloy stainless steel) Many uses including high-chloride water-water duties
Example, up to 6000 ppm chlorides at 50C
Titanium
Most frequent use is for sea water (3.5% chlorides) Example, up to 130C in sea water
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Gasket - materials The choice of rubber material depends on Temperature
Required lifetime
Media
Rubber materials change properties due to
Time - the rubber relaxes
-
Hardening by attack of oxidising agents (e.g., oxygen in air)
Swelling or softening by absorption of chemicals in the fluids
Common gasket types
Nitrile
EPDM
FKMT
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Fi l te r
A filter for industrial coolingsystems using low-quality water
Protecting the heat exchanger
The Filter operates as an integralpart of a cooling system to removedebris which can foul and clog aplate heat exchanger or a tubularcondenser.
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Compact heat exchangers
in HVAC systems
Enables high energy efficiency
Close temperature approach Small temperature losses
Increased temperature drop
Fast response times at regulation
Limited footprint
Compact design
High thermal efficiency
Easy service
Openable for mechanical cleaning
Expansion of capacity possible
Alfa Laval Slide 26
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Thank you!
Alfa Laval Slide 27
Questions?