energy efficiency in industrial refrigeration systems_r
TRANSCRIPT
Energy Efficiency in Industrial Energy Efficiency in Industrial Refrigeration SystemsRefrigeration Systems
Ahmad R. Ganji, Ph.D., P.EAhmad R. Ganji, Ph.D., P.EProfessor of Mechanical Professor of Mechanical
EngineeringEngineeringSan Francisco State UniversitySan Francisco State University
2008 IAC Directors Meeting2008 IAC Directors MeetingJuly 14July 14--15 200815 2008
IACIAC--SFSUSFSU 22
OutlineOutline
•• Brief Introduction of Vapor Compression Brief Introduction of Vapor Compression CyclesCycles
•• Major Components of Industrial Major Components of Industrial Refrigeration SystemsRefrigeration Systems
•• Potential Energy Efficiency OpportunitiesPotential Energy Efficiency Opportunities
IACIAC--SFSUSFSU 33
Industrial Refrigeration ApplicationsIndustrial Refrigeration Applications
•• Space CoolingSpace Cooling•• Food ProcessingFood Processing•• ChemicalsChemicals•• PharmaceuticalsPharmaceuticals•• ………….. …………..
IAC-SFSU 4
Vapor Compression CycleSingle Stage
Pres
sure
(psi
a)
Saturated Liquid Line 1
10
100
1000
1
Ammonia
23
4
Saturated Vapor Line
Compression
Enthalpy (Btu/lbm)400200 500300100-100 600 700 8000
Motor
Receiver
vapor
vaporliquid
Compressor
1
2
3
4
liquid
EvaporativeCondenser
Evaporator
IAC-SFSU 5
Vapor Compression CycleTwo-Stage
vapor
Evaporative Condenser
vapor
liquid
liquid
Process Chiller
Flooded Drum/Low Pressure Receiver
vapor
superheatedvapor
subcooled liquid
2nd StageReciprocating Compressor
1st Stage Reciprocating Compressors
Intercooler
High Pressure Receiver
Pres
sure
(psi
a)
Saturated Vapor Line
1
10
100
1000
1
Ammonia
45
7
3 2High-Stage
Low-Stage
Saturated Liquid Line
6
8 High Temperature Evaporators (30 F)
Low Temperature Evaporators (0 F)
Enthalpy (Btu/lbm)400200 500300100-100 600 700 8000
IAC-SFSU 6
High-Stage Reciprocating Compressors in 2-Stage System
IAC-SFSU 7
Low-Stage Screw Compressors in 2-Stage System
IACIAC--SFSUSFSU 88
Refrigeration System ComponentsRefrigeration System Components
•• CompressorCompressor–– ReciprocatingReciprocating–– Screw TypeScrew Type–– Rotary VaneRotary Vane
•• CondenserCondenser–– Air condensersAir condensers–– Evaporative CondenserEvaporative Condenser–– Cooling Tower/Heat ExchangerCooling Tower/Heat Exchanger
•• Evaporator/Chiller/Heat ExchangerEvaporator/Chiller/Heat Exchanger•• Receiver/AccumulatorReceiver/Accumulator
IACIAC--SFSUSFSU 99
Causes of Low Energy EfficiencyCauses of Low Energy Efficiency
•• Unnecessary High LoadUnnecessary High Load•• Unnecessary High System LiftUnnecessary High System Lift•• Poor PartPoor Part--Load PerformanceLoad Performance•• Poor/Outdated Control SystemsPoor/Outdated Control Systems•• Low Efficiency EquipmentLow Efficiency Equipment
IACIAC--SFSUSFSU 1010
Potential Energy Efficiency MeasuresPotential Energy Efficiency Measures
Refrigeration SystemRefrigeration System•• Insulate Suction Lines and Low Pressure ReceiversInsulate Suction Lines and Low Pressure Receivers•• Increase Ammonia System’s Suction PressureIncrease Ammonia System’s Suction Pressure•• Reduce Head Pressure Reduce Head Pressure •• Convert Ammonia Refrigeration to Floating Head Pressure Convert Ammonia Refrigeration to Floating Head Pressure •• Install High Efficiency Ammonia CompressorsInstall High Efficiency Ammonia Compressors•• Sequence Ammonia CompressorsSequence Ammonia Compressors•• Replace Single Stage Compressor with TwoReplace Single Stage Compressor with Two--Stage SystemStage System•• Use Use SubcoolingSubcooling to Reduce Compressor Powerto Reduce Compressor Power•• Recover Waste Heat from Ammonia Refrigeration SystemRecover Waste Heat from Ammonia Refrigeration System
IACIAC--SFSUSFSU 1111
Potential Energy Efficiency MeasuresPotential Energy Efficiency Measures
CondensersCondensers•• Increase Evaporative Condenser CapacityIncrease Evaporative Condenser Capacity•• Replace AirReplace Air--Cooled Condensers with Cooled Condensers with
WaterWater--Cooled CondensersCooled Condensers•• Install Adjustable Speed Drives on the Install Adjustable Speed Drives on the
Evaporative Condenser FansEvaporative Condenser Fans
IACIAC--SFSUSFSU 1212
Potential Energy Efficiency MeasuresPotential Energy Efficiency Measures
EvaporatorsEvaporators•• Control Evaporator Defrost Based on DemandControl Evaporator Defrost Based on Demand•• Control Evaporator Fans with VFDControl Evaporator Fans with VFD
IACIAC--SFSUSFSU 1313
Insulate Suction Lines/ReceiversInsulate Suction Lines/Receivers
•• Present Condition:Present Condition:The lines or receivers are bare or poorly insulated, and The lines or receivers are bare or poorly insulated, and ice formation on them is often visible.ice formation on them is often visible.
•• Remedy:Remedy:Insulate with appropriate insulation, based on Insulate with appropriate insulation, based on temperature temperature –– may need vapor barrier.may need vapor barrier.
•• Pay back:Pay back:Fairly short, depends on ambient and refrigerant Fairly short, depends on ambient and refrigerant temperaturetemperature
IACIAC--SFSUSFSU 1414
Increase Ammonia System’s Suction Increase Ammonia System’s Suction PressurePressure•• Present Condition:Present Condition:
The suction pressure/temperature is too low for the application,The suction pressure/temperature is too low for the application, i.e. i.e. ∆∆T between refrigerant and the refrigerated medium is too high. T between refrigerant and the refrigerated medium is too high. Typical values for Typical values for ∆∆T should be about 10T should be about 10--15 F. Other cause may be 15 F. Other cause may be pressure restriction in the suction line.pressure restriction in the suction line.
•• Remedy:Remedy:Decrease Decrease ∆∆T to 10T to 10--15 F, and make sure that evaporator/ heat 15 F, and make sure that evaporator/ heat exchanger can handle the new setting. Remove pressure restrictorexchanger can handle the new setting. Remove pressure restrictors.s.
•• Pay back:Pay back:Immediate, unless you need to change/add evaporatorImmediate, unless you need to change/add evaporator/ heat exchanger/ heat exchanger
1 F increase in the evaporator will increase the efficiency of t1 F increase in the evaporator will increase the efficiency of the he system about 2%!system about 2%!
IACIAC--SFSUSFSU 1515
Reduce Head PressureReduce Head Pressure•• Present Condition:Present Condition:
The head pressure/temperature is too high for the application, iThe head pressure/temperature is too high for the application, i.e. .e. ∆∆T between condensing refrigerant and the ambient (dry or wet T between condensing refrigerant and the ambient (dry or wet bulb temperature depending on the condensing system) is too highbulb temperature depending on the condensing system) is too high..
•• Remedy:Remedy:Decrease Decrease ∆∆T to 10T to 10--15 F, and make sure that the condenser can 15 F, and make sure that the condenser can handle the new setting. handle the new setting.
•• Pay back:Pay back:Immediate, unless you need to change/add condensing capacity.Immediate, unless you need to change/add condensing capacity.
Reducing condenser T by 1 F may increase compressor efficiency bReducing condenser T by 1 F may increase compressor efficiency by 1.5 to y 1.5 to 2%! Lowering the head pressure increases system capacity2%! Lowering the head pressure increases system capacity
IAC-SFSU 16
Reduce Head Pressure (cont.)
Reducing head pressure increases system capacity
Enthalpy (Btu/lbm)
Pres
sure
(psi
a)
Saturated Vapor Line
0-200
1
10
100
1000
100-100-300-500 -400 200 300 400 500
1
Ammonia
3
4
2
Saturated Liquid Line
3'
4'
2'
IACIAC--SFSUSFSU 1717
Convert Ammonia Refrigeration to Convert Ammonia Refrigeration to Floating Head PressureFloating Head Pressure•• Present Condition:Present Condition:
The head pressure setting is high to accommodate for high The head pressure setting is high to accommodate for high temperature ambient (temperature ambient (TTwbwb), but most of the time ), but most of the time TTwbwb is low.is low.
•• Remedy:Remedy:Add a floating head pressure controller and let the head pressurAdd a floating head pressure controller and let the head pressure e float based on ambient wet bulb temperature, with an approach float based on ambient wet bulb temperature, with an approach temperature of about 10temperature of about 10--15 F.15 F.
•• Pay back:Pay back:$30 k $30 k -- $50 k, will increase if additional condensing capacity is $50 k, will increase if additional condensing capacity is needed.needed.
Minimum pressure may become limited due to hot gas defrost, liquMinimum pressure may become limited due to hot gas defrost, liquid id injection or floor heating pressure requirements.injection or floor heating pressure requirements.
IACIAC--SFSUSFSU 1818
Install High Efficiency Ammonia Install High Efficiency Ammonia CompressorsCompressors
•• Present Condition:Present Condition:The compressor has poor performance especially at part The compressor has poor performance especially at part load (e.g. long unload periods, oversized, etc.)load (e.g. long unload periods, oversized, etc.)
•• Remedy:Remedy:Install a new reciprocating with cylinder unloading of Install a new reciprocating with cylinder unloading of VFD controlled screw VFD controlled screw compressor(scompressor(s).).
•• Pay back:Pay back:Several years, highly dependent on the specific case.Several years, highly dependent on the specific case.
IACIAC--SFSUSFSU 1919
Use Computer Control to Manage Use Computer Control to Manage Compressor SequencingCompressor Sequencing
•• Present Condition:Present Condition:Multiple Compressors are not sequenced properly and some of themMultiple Compressors are not sequenced properly and some of themwork partwork part--load or unloaded for significant periods of time.load or unloaded for significant periods of time.
•• RemedyRemedy::Properly sequence the compressors by computer control to minimizProperly sequence the compressors by computer control to minimize e partpart--load/unload operation for significant periods. This can be well load/unload operation for significant periods. This can be well accomplished with reciprocating compressor accomplished with reciprocating compressor unloadersunloaders and VFD and VFD controlled screw compressors.controlled screw compressors.
•• Pay back:Pay back:Immediate to a few yearsImmediate to a few years
IACIAC--SFSUSFSU 2020
Replace Single Stage Compressor with Replace Single Stage Compressor with TwoTwo--Stage SystemStage System
•• Present Condition:Present Condition:This is the case that there may be one or two refrigerated This is the case that there may be one or two refrigerated temperature levels, but a single stage system produces a large temperature levels, but a single stage system produces a large pressure ratio (lift, usually for subzero temperature levels) pressure ratio (lift, usually for subzero temperature levels)
•• Remedy:Remedy:Split the system into a two stage system with Split the system into a two stage system with intercoolingintercooling. Most . Most appropriate for multiappropriate for multi--level temperature systems.level temperature systems.
•• Pay back:Pay back:Can be several years because of the cost of compressor, vessels,Can be several years because of the cost of compressor, vessels,valvingvalving and controls.and controls.
IAC-SFSU 21
Vapor Compression CycleTwo-Stage
vapor
Evaporative Condenser
vapor
liquid
liquid
Process Chiller
Flooded Drum/Low Pressure Receiver
vapor
superheatedvapor
subcooled liquid
2nd StageReciprocating Compressor
1st Stage Reciprocating Compressors
Intercooler
High Pressure Receiver
Pres
sure
(psi
a)
Saturated Vapor Line
1
10
100
1000
1
Ammonia
45
7
3 2High-Stage
Low-Stage
Saturated Liquid Line
6
8 High Temperature Evaporators (30 F)
Low Temperature Evaporators (0 F)
Enthalpy (Btu/lbm)400200 500300100-100 600 700 8000
IACIAC--SFSUSFSU 2222
Use SubUse Sub--cooling to Reduce Compressor cooling to Reduce Compressor PowerPower
•• Present Condition:Present Condition:Saturated liquid refrigerant is expanded for evaporation.Saturated liquid refrigerant is expanded for evaporation.
•• Remedy:Remedy:Install an subInstall an sub--cooler through an intermediate stage cooler through an intermediate stage expansionexpansion
•• Pay back:Pay back:About one yearAbout one year
IAC-SFSU 23
Typical Subcooler
vapor
Liquid Ammoniafrom Evaporative
Condenser
Subcooled Ammonia toEvaporators
Intermediate-PressureAmmonia Vapor to
Intercooler
subcooledHPL
High-PressureReceivers
LiquidSubcooler
Expansion Valve
HPL
5
6
IACIAC--SFSUSFSU 2424
Recover Waste Heat from Ammonia Recover Waste Heat from Ammonia Refrigeration SystemRefrigeration System•• Present Condition:Present Condition:
No heat is recovered from hot compressor outflow. No heat is recovered from hot compressor outflow. Does not apply to cases with liquid injection!Does not apply to cases with liquid injection!
•• Remedy:Remedy:Install a heat exchanger to recover heat for any Install a heat exchanger to recover heat for any application in the plant (e.g. preheat boiler makeapplication in the plant (e.g. preheat boiler make--up up water, heat domestic water, water, heat domestic water, floorheatingfloorheating))
•• Pay back:Pay back:A couple of years depending on the need for thermal A couple of years depending on the need for thermal energy at low temperatureenergy at low temperature
IAC-SFSU 25
Recover Waste Heat from Ammonia Refrigeration System (cont.)
Schematic of Proposed Desuperheater
IACIAC--SFSUSFSU 2626
Potential Energy Efficiency MeasuresPotential Energy Efficiency Measures
CondensersCondensers•• Increase Evaporative Condenser CapacityIncrease Evaporative Condenser Capacity•• Replace AirReplace Air--Cooled Condensers with Cooled Condensers with
WaterWater--Cooled CondensersCooled Condensers•• Install Adjustable Speed Drives on the Install Adjustable Speed Drives on the
Evaporative Condenser FansEvaporative Condenser Fans
IACIAC--SFSUSFSU 2727
Increase Evaporative Condenser Increase Evaporative Condenser CapacityCapacity
•• Present Condition:Present Condition:The condenser does not have enough heat rejection capacity, thusThe condenser does not have enough heat rejection capacity, thusthe refrigerant condenses at high pressure/head pressure remainsthe refrigerant condenses at high pressure/head pressure remainshighhigh
•• RemedyRemedy::Increase the condensation capacity.Increase the condensation capacity.
•• Pay back:Pay back:From one to few years depending on the capacity needsFrom one to few years depending on the capacity needs
IACIAC--SFSUSFSU 2828
Replace AirReplace Air--Cooled Condensers with Cooled Condensers with WaterWater--Cooled CondensersCooled Condensers
•• Present Condition:Present Condition:The system has an air cooled condenser working based on heat The system has an air cooled condenser working based on heat rejection to rejection to TTdbdb, , which results in high head pressurewhich results in high head pressure..
•• Remedy:Remedy:Replace the air cooled condenser with an evaporator condenser (iReplace the air cooled condenser with an evaporator condenser (if f atmospheric conditions allows!) and lower the head pressure.atmospheric conditions allows!) and lower the head pressure.
•• Pay back:Pay back:A few yearsA few years
IACIAC--SFSUSFSU 2929
Install VFD on the Evaporative Install VFD on the Evaporative Condenser FanCondenser Fan
•• Present Condition:Present Condition:The evaporator condenser/cooling tower has constant The evaporator condenser/cooling tower has constant speed fans and works continuously or is on/off speed fans and works continuously or is on/off controlled.controlled.
•• Remedy:Remedy:Install VFD and control the speed based on water Install VFD and control the speed based on water temperature or head pressure.temperature or head pressure.
•• Pay back:Pay back:A couple of yearsA couple of years
IACIAC--SFSUSFSU 3030
Potential Energy Efficiency MeasuresPotential Energy Efficiency Measures
EvaporatorsEvaporators•• Control Evaporator Defrost Based on DemandControl Evaporator Defrost Based on Demand•• Control Evaporator Fans with VFDControl Evaporator Fans with VFD
IACIAC--SFSUSFSU 3131
Control Evaporator Defrost Based on Control Evaporator Defrost Based on DemandDemand
•• Present Condition:Present Condition:Defrosting of evaporators is timeDefrosting of evaporators is time--based, it is timer based, it is timer controlled.controlled.
•• Remedy:Remedy:Install demandInstall demand--based defrosting controller using defrost based defrosting controller using defrost sensors. DOE sponsored study shows 7sensors. DOE sponsored study shows 7--11% savings 11% savings
•• Pay back:Pay back:About a year, will greatly depend on the cold About a year, will greatly depend on the cold storage/freezer environment.storage/freezer environment.
IACIAC--SFSUSFSU 3232
Control Evaporator Fans with VFDControl Evaporator Fans with VFD
•• Present Condition:Present Condition:Evaporator fans are on all the time or they have onEvaporator fans are on all the time or they have on--off control. The off control. The environment temperature is usually controlled by refrigerant floenvironment temperature is usually controlled by refrigerant flow.w.
•• Remedy:Remedy:Install VFD on the evaporators to be controlled based on cold Install VFD on the evaporators to be controlled based on cold environment temperature.environment temperature.
•• Pay back:Pay back:A few years, will greatly depend on the cold storage/freezer loaA few years, will greatly depend on the cold storage/freezer load d variation.variation.
IACIAC--SFSUSFSU 3333
Potential Energy Efficiency Measures Potential Energy Efficiency Measures (cont.)(cont.)
Other MeasuresOther Measures•• Install thermoInstall thermo--siphon oil coolingsiphon oil cooling•• Optimize Intermediate Suction PressureOptimize Intermediate Suction Pressure•• Install Gas Engine Driven CompressorsInstall Gas Engine Driven Compressors•• Reduce Refrigeration Load by Various MeansReduce Refrigeration Load by Various Means
IACIAC--SFSUSFSU 3434
Some ReferencesSome References
Industrial Refrigeration Best Practices GuideIndustrial Refrigeration Best Practices GuideNorthwest Energy Efficiency Alliance, Dec. 2007Northwest Energy Efficiency Alliance, Dec. 2007
Industrial Refrigeration HandbookIndustrial Refrigeration HandbookWilbert F. Wilbert F. StoeckerStoecker, McGraw Hill, 1995, McGraw Hill, 1995