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7/22/2019 CVHF Presentation_Basic Operation
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Familiarization and Basic Operation of CVHF Chiller
Date
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TOPICSTOPICS
Overview
Typical View
Refrigeration System Operating Principle
u r ca on o or oo ng ys em
Purge System
Chiller Control System a n enance
Questions
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OverviewOverview
CVHF Feature
> Single compressor, CENTRIFUGAL type water cooled liquid chillers
> Uses R-123 as refrigerant and Trane Oil 0022
Model Number Coding System
CVH F 049 D A 2 P 0 L C N 2 7 1 8 W B E 8 R B C00
Digits
1,2 CV Unit type Centravac Hermetic 14 C Control Interface, UCP3
3 H Drive Type, Direct Driv 15 N Comp KW, CPKW
, , ,
5,6.7 049 Nominal Tonnage,770Ton Comp Impeller Cutback
Design tons 751.75 1st 2nd
8 D Voltage, 460/60/3 27.6 27.6
9 A Unit type, Cooling Condenser
10,11 2P Design Sequence 19 8 Evap Shell Size, 080 long shel12 0 Hotgas bypass, without 20 W Evap tube bundle size,800 Nom
13 L Purge Purifier
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Typical View of a CVHF ChillerTypical View of a CVHF Chiller
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Major Components of the Chil lerMajor Components of the Chil ler
Compressor It is the heart of the vapor compression system. It provides the pressure increase necessary to facilitate the
transfer of heat.
Condenser
Meterin Device
It receives superheated refrigerant from the compressor andremoves the superheat and liquefy the refrigerant (sub cooling).
Evaporator
refrigerant to the evaporator.
It transfer heat from a substance being cooled to a boilingrefri erant.
It is a devices intended to reduce energy consumption, or toerform another useful function like reheatin a fluid.
Purge The purgeis designed to remove non-condensable gases andwater from the refrigeration system.
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Refri eration S stemRefri eration S stem
, ,
personnel spaces. The systems do this with refrigerantsthat remove heat from the heat source and discharge it
to a heat sink.
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Basic RefrigerationBasic RefrigerationCycleCycle
Cooling
Tower
Superheated vaporSub-cooled liquid
CONDENSER 23
Metering
DeviceCOMPRESSOR
EVAPORATOR 14
LP Vapor l ine
Saturated vaporMixture
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COOLHEAT
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OPERATING PRINCIPLESOPERATING PRINCIPLES
Evaporator Componentstube bundletube bundle
liquidliquidrefrigerantrefrigerant
chilledchilled
waterwaterreturnreturn
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orifice systemorifice system
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CENTRIFUGAL COMPRESSOR COMPONENTSCENTRIFUGAL COMPRESSOR COMPONENTS
Inlet Guide Vanes Impellers
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Inlet Guide Vanes
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Condenser
95
Condenser
85
1
Water In
De-su erheats and Condenses Refri erant
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1
Vapor
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Metering Orif ice
The Metering Orifice MetersRefrigerant Flow
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CVHF Refrigeration Cycle with EconomizerCVHF Refrigeration Cycle with Economizer
2-Stage Refrigerant Flow
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ONOMIZ R
o n a ge
Elim inator
Orifice
FromCondenser
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CVHF Refrigeration CycleCVHF Refrigeration Cycle
2-Stage P-H Diagram
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Efficiency
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General Assembly Oil/Refrigeration System Schematic
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Purge SystemPurge SystemPurge SystemPurge System
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Refrigerant ReportRefrigerant Report
Purge Operating ModesPurge Operating Modes(Stop, On, Auto, Adaptive)
Purge Operating ModesPurge Operating Modes(Stop, On, Auto, Adaptive)
1. Sto The ur e condensin unit will not1. Sto The ur e condensin unit will notrun.
2. On - The purge condensing unit runs
run.
2. On - The purge condensing unit runs
operational status.
3. Auto - the purge condensing unit runs when
operational status.
3. Auto - the purge condensing unit runs when
4. Adaptive The purge condensing unitoperation is totally dependent on past purge
4. Adaptive The purge condensing unitoperation is totally dependent on past purge
activity. Purge monitors its 1.) daily pumpouttime with the chi ller ON or OFF, over the last 24
hours and 2.) average daily pumpout time with
the chil ler ON or OFF, over the last 7days.
activity. Purge monitors its 1.) daily pumpouttime with the chi ller ON or OFF, over the last 24
hours and 2.) average daily pumpout time with
the chil ler ON or OFF, over the last 7days.
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Advantages of Adaptive ModeAdvantages of Adaptive Mode
Objectives of operating the unit in the AdaptiveObjectives of operating the unit in the Adaptive
Operating the purge refrigeration circuit to effectively
accumulate non-condensables with or without the
Operating the purge refrigeration circuit to effectively
accumulate non-condensables with or without the
c er runn ng.
Provide information to the operator as to whether
leakage is on the high-pressure or low-pressure side of
c er runn ng.
Provide information to the operator as to whether
leakage is on the high-pressure or low-pressure side of.
Decrease energy usage by running the purge
refrigeration c ircuit only when needed to remove non-
.
Decrease energy usage by running the purge
refrigeration c ircuit only when needed to remove non-
, ., .
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Purge SystemPurge System
RR--404a Condensing Unit404a Condensing UnitRR--404a Condensing Unit404a Condensing Unit
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System ContaminationSystem ContaminationSystem ContaminationSystem Contamination
Equipment LeaksEquipment Leaks
Poor EvacuationPoor Evacuation
Introducing Contaminated RefrigerantIntroducing Contaminated Refrigerant
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Earthwise Purge SystemEarthwise Purge System
Condensing Unit
Condenser
Expansion
CompressorCarbon Tank
Temp Sensor
Exhaust
Pressure ReliefDevice
Device
Com ressor Suction
PumpoutSolenoid Valve
To Chiller
Vent Line
Solenoid ValveRestrictor
To Chiller
Purge
Tank
Temp Sensor Pump-out
Compressor
RegenerationSolenoid Valve
Isolation
Evaporator
Carbon
TankHeater
Finned
Heater Well
a ve
FloatSwitch
Liquid Drain
Line
apor
Pick-up Line
Filter/DrierChiller
Condenser
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Valves
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Purge Condenser RPurge Condenser R--404a Circuit404a CircuitPurge Condenser RPurge Condenser R--404a Circuit404a Circuit
CONDENSER
R-404a EVAP
COMPRESSOR 85 F LIQUID
TEMP SENSOR -16 F LIQUID
> 60 F Vapor
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AEV-
INLETR-123
OUTLET
R-123
OUTLET
75 F LIQUID
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No Air in purge tankNo Air in purge tank
-Mixture from EXV (-16 o F)
Purge coi l area availablefor superheating
R404a Gas tocondensingunit Chiller refrigerant
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suction (90 F)
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Air of Purge TankAir of Purge Tank
R404a Liquid/Vapor Mixture from
EXV (-16F)
Purge coil area
available for Air
superheating
Chiller refrigerant vapor (100F)
R404a Gas to Condensing
Unit compressor Suction
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Air fills Purge TankAir fills Purge Tank
R404a Liquid/Vapor Mixture from
EXV (-16F)
No coil area
available for
superheating
R404a Gas to condensing unit
compressor Suction (-16F)
Air
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onon-- on ensa e emovaon ensa e emova
When sufficient non-condensable have accumulated in the purge tank to
decrease the compressor suction temperature below the pump out initiateset point a pump out cycle has begun. The cycle will be terminated when the
compressor suction temperature sensor increases above the pump out
terminate set-point.
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Control SystemControl System
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MaintenanceMaintenance
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Maintenance
After the first 6 months or 1000 hours operation, whichever comes first, it is
recommended to change the oil and filter. After this oil change,
recommendations are to subscribe to an annual oil analysis program rather
than automatically change the oil as part of scheduled maintenance.
Proper Water TreatmentThe use of untreated or improperly treated water in a CenTraVac may result
in scaling, erosion, corrosion, algae or slime. It is recommended that the
services of a qualified water treatment specialist be engaged to determine
equipment failures which result from untreated or improperly treated water, orsaline or brackish water.
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Basic Maintenance ItemsBasic Maintenance Items
Daily
Monitorin of Chiller Re uired Parameters
Oil Level visual check (using sight glass)
Quarterly
Cleaning of water strainers (Piping)
Semi-Annually
Lubrication of Vane Control System (bearings, ball joints,...)
Annually a rat on o ontro s re ays, sensors,
Measure Compressor Motor Winding resistance
Oil Change and Oil Analysis
Other Maintenance Requirements
Inspect and clean condenser tubes if necessary
-
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Compressor Motor ProblemCompressor Motor Problem
Voltage And Current Unbalance
100 X the Sum of the Deviation of the Voltages, (Currents),
v e y e verage
The Unbalance Should Not Exceed 2% Voltage or 10 % Current
Example:
Measured Voltages :
480 Volts
Sum of the Deviation:
480 - 470 = 10
470 Volts460 VoltsAverage: = 470 Volts
-
470 - 460 = 1020 X 100 = 2,000
, : = .
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Other Important ItemsOther Important Items
CAUSES OF SURGE
Too hi h condensin tem erature
Too much incondensable in a low pressure unit :
don't operate unit at full load if purge unit is not stabilized ( pay attention
to leaks of refrigerant through purge unit )
Cooling tower temperature too high :
too much refrigerant
dirty tubes too low water flow rate
Lack of refrigerant
too long part load operation
un m g surge ur ng a ong me a par oa o , s en
recommended to reduce condenser inlet water temperature of 1F per
10% load reduction
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Other Important ItemsOther Important Items
CAUSES OF SURGE SURGE CONSE UENCES
Liquid refrigerant carry over
Loss of performance
too high evaporator water
temperature
Oil carr over
Amperage peaks
Vibrations and noise
noisy compressor
amperage fluctuations
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Normal ParametersNormal Parameters
Normal Operating Conditions
Description Condition
vapora or ressure o g acuum
Condenser Pressure 0 to 10 psigOil Sump Temperature
Unit Not Runnin 140 to 145F
Unit Running 62 to 162F
Differential Oil Pressure 18 to 22 psid
Discharge Oil Pressure 7 to 15 psig
Condenser Approach Temp = Sat Cond Temp - Lvg Cond Water Temp
Evaporator Approach Temp = Lvg CHW Temp - Sat Evap Temp
Notes: 1. ARI Conditions are: cond water - 85F & 3 gpm/xxx tons
Evaporator Water: 54 to 44F2. Condenser pressure is dependent on condenser water temp and
should equal the saturation pressure of HCFC-123 at a temp above that of leaving
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.
3. Std. Cond App Temp: 0 to 5F ; Std Evap App Temp: 0 to 4F
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QuestionsQuestions
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an youan you
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