life cycle cost of selecting chiller equipment...
TRANSCRIPT
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Life Cycle Cost Of Selecting Life Cycle Cost Of Selecting Chiller Equipment:Chiller Equipment:
Manufacturer’s ViewpointManufacturer’s Viewpoint
Daryl ShowalterChillerApplications Manager
McQuay International
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EquipmentEquipmentn Using Different Kinds Of
Equipment Or Different Performance Equipment Can Improve Cost
n Difficult Part Is To Evaluate Life Cycle Analysis
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Air Cooled Vs. Water CooledAir Cooled Vs. Water Cooled
n Water Cooled Will Be More Energy Efficient
n It Usually Costs Less To Operate– Maintenance And Water
Costs
nn For Optimization Go Water For Optimization Go Water CooledCooled
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Water Cooled Water Cooled -- Optimizing SelectionsOptimizing Selections
n Enter Design Data Into The Program
– Start The Processu Choose The Chiller
After A Large Vertical Drop
u Look At The Number Of Selections And Prioritize
uAnalyze Options
Not Good
Good Selection
Cost
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Review ComponentsReview ComponentsIn Selecting The Chiller Look At:
– Vessel Length Changes
– Vessel Diameter Changes
– Vessel Tube Count
– Compressor / Gear Selection-If Appropriate
– Motor Size
– Number Of Passes
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Conditions Of Service:
– Use Lower Entering Condenser Water Temp
– Use Higher Leaving Chilled Water Temp
– 1/2 Degree Anywhere Makes a BIG Difference !!
– MINIMIZE LIFT
Optimizing PerformanceOptimizing Performance
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Range Vs. Supply Water TemperatureRange Vs. Supply Water Temperaturen Declining Supply Water Temperature (44 To 38F)n Increase Chilled Water Range From 10 To 24Fn Annual Energy Analysis
Run C.W. Range C.W. S.T. Chiller Pumps Tower Fan S.A. Fan Total(°F) (°F) ($/yr) ($/yr) ($/yr) ($/yr) ($/yr)
1 10 44 26,074 15,175 1,591 28,275 71,1152 12 44 26,096 13,784 1,593 28,560 70,0333 16 44 26,211 12,055 1,597 29,350 69,2133 14 42 27,733 12,790 1,593 28,573 70,6894 16 42 27,779 12,039 1,593 28,570 69,9815 18 40 29,371 11,462 1,594 28,584 71,0116 20 40 29,351 11,002 1,596 28,872 70,0817 22 38 30,365 10,623 1,596 28,881 71,465
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99% Of All Operating 99% Of All Operating Hours Are At Part LoadHours Are At Part Load
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The New Industry ARI StandardThe New Industry ARI Standard --1998 1998
Part Load Analysis (IPLV)Part Load Analysis (IPLV)
% Load Old % Hrs New % Hrs100 17 175 39 4250 33 4525 11 12
Systems Solution
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n High Glycol = Low Heat Transfer:
– Propylene Glycol Has Really Bad Heat Transfer Properties –Increases Head On Compressor
– Utilize Less % Of Glycol - Even 0.5% Can Make A Difference– ASHRAE Fundamentals: Physical Properties Of Secondary
Coolants
n Don’t Limit Input Values – Run Selections Multiple Ways
Optimizing SelectionsOptimizing Selections-- Glycol!Glycol!
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n High Pressure Drops?– Look At 1 Pass Vessels– Look At Reducing Evaporator Or
Condenser Length– Tube Thickness Can Increase
Pressure Drop
n Conversely - High Temperature Difference?– Look At (3) Pass– Look At Series Flow With 1, 2,
Or 3 Pass
VesselsVessels
Single Pass
Two Pass
Three Pass
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n Low NPLV Or IPLV: Look At Multiple Compressor Or VFD– Sort By NPLV/IPLV – Lowest NPLV Is Not Normally The Lowest Full Load kW/Ton – Slight Decrease In Full Load KW/TR Can Dramatically Increase
Cost And Actually Increase NPLV/IPLV!
Optimizing SelectionsOptimizing Selections-- F.L. Vs. IPLVF.L. Vs. IPLV
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Various 500 Ton ChillersVarious 500 Ton Chillers
.6
.5
.4
.3WSC WDC WDC w/VFDWSC w/VFD
.505
.403
.365.337
IPLV
Notes: WSC = Single Compressor Centrifugal ChillerWDC = Dual Compressor Centrifugal ChillerVFD = Variable Frequency Drive
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n Multiple Chillers On A Job?– High Temperature Difference Across The Evaporator?
u Look At Series / Counterflow Arrangementsu 1 Multiple Compressor Instead Of 2 Singles
System ConsiderationsSystem Considerations
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Cooling Tower ConsiderationsCooling Tower Considerations
n Oversize Tower To Lower Condenser Water Supply Temperaturen Chiller Stays Same Price, Efficiency Improves 11%n Tower Capital And Operating Cost Up Slightlyn 3% Annual Savings
Run Cond .W.S.T. Chiller Chiller Pumps Tower Fan S.A. Fan Total(°F) kW/Ton ($/yr) ($/yr) ($/yr) ($/yr) ($/yr)
1 85 0.547 24,435 15,209 1,441 24,512 65,5972 84 0.535 23,842 15,207 1,463 24,508 65,0203 83 0.524 23,425 15,205 1,482 24,505 64,6174 82 0.514 23,055 15,203 1,501 24,502 64,2615 81 0.492 22,147 15,199 1,526 24,496 63,3686 80 0.483 21,848 15,197 1,548 24,942 63,535
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Annual WB In Major US CitiesAnnual WB In Major US Cities
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10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0
Janu
ary
Febru
aryMarc
hAp
rilMay
June Ju
ly
Augus
t
Septe
mber
Octobe
r
Novem
ber
Decem
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Los Angeles Washington DC Atlanta Chicago Miami
Strong Candidates ForVFD Chillers
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Optimizing Starter SelectionsOptimizing Starter Selections
n Try Different Starters– Solid State Starters Have Different Size Breaks
Than Wye Delta Starters– Solid State Starters Are Now Cheaper In Most
Cases - Try Both Ways Depending Upon Size Breaks
– Try Unit Mounted And Free Standing - Size Breaks Can Make Different Selections Appear
– Check VFD Sizing –Expensive At Very Bottom Of Amp Rating
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Variable Flow Vs. Constant FlowVariable Flow Vs. Constant Flow
0
50000
100000
150000
200000
250000
300000
350000
400000
450000
500000
Chillers Pumps Towers Fans
kWh
Variable Primary Flow 2 Chiller Primary/Secondary Flow 2 Chiller Parallel Flow
Notice Pump WorkHalf Chiller Work!
Pump Work Cut In Half
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WrapWrap--upup
n Many Ways To Solve An Application
n Selection Is Only As Good As The Data Given
n Optimize Your Selections