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© 2016 Emerson Climate Technologies, Inc.

AE4-1402 R4

Assembly Line Brazing Procedure

WARNING

Personal safety equipment must be used during 

brazing operation. Heat shields should be 

used to prevent overheating or burning nearby 

temperature sensitive parts. Fire extinguishing 

equipment should be accessible in the event of a 

fire. 

Figure 5 

discusses the proper procedures for brazing 

the suction and discharge lines to a scroll compressor. 

NOTICE It is important to flow nitrogen through the 

system while brazing all joints during the system 

assembly process.

 Nitrogen displaces the air and 

prevents the formation of copper oxides in the system. 

If allowed to form, the copper oxide flakes can later 

be swept through the system and block screens such 

as those protecting capillary tubes, expansion valves, 

and accumulator oil return holes. Any blockage of oil 

or refrigerant may damage the compressor resulting 

in failure.

Pressure Testing

WARNING

Never pressurize the compressor to more than 

475 psig (33 bar) for leak checking purposes. 

Never pressurize the compressor from a nitrogen 

cylinder or other pressure source without an 

appropriately sized pressure regulating and relief 

valve.

The pressure used on the line to meet the U.L. burst 

pressure requirement must not be higher than 475 

psig (33 bar). Higher pressure may result in permanent 

deformation of the compressor shell and possible 

misalignment or bottom cover distortion.

Assembly Line System Charging Procedure

Systems should be charged with liquid on the high side 

to the extent possible. The majority of the charge should 

be pumped in the high side of the system to prevent low 

voltage starting difficulties, hipot failures, and bearing 

washout during the first-time start on the assembly line. 

If additional charge is needed, it should be added as 

liquid

 to the low side of the system with the compressor 

operating. Pre-charging on the high side and adding 

liquid on the low side of the system are both meant to 

protect the compressor from operating with abnormally 

low suction pressures during charging. 

NOTICE:

 

Do 

not operate the compressor without enough system 

charge to maintain at least 55 psig (3.8 bar) suction 

pressure. Do not operate the compressor with the 

low pressure cut-out disabled. Do no operate with 

a restricted suction or liquid line. 

Depending on the 

discharge pressure, allowing pressure to drop below 

55 psig (3.8 bar) for more than a few seconds may 

overheat the scrolls and cause early drive bearing 

damage. 

NOTICE

 

Do not use the compressor to test 

the opening set point of a high pressure cutout. 

Bearings are susceptible to damage before they have 

had several hours of normal running for proper break in.

'Hipot' (AC High Potential) Testing

CAUTION

Use caution with high voltage and never hipot 

test when compressor is in a vacuum.

Copeland Scroll compressors are configured with the 

motor down and the pumping components at the top 

of the shell. As a result, the motor can be immersed 

in refrigerant to a greater extent than hermetic 

reciprocating compressors when liquid refrigerant is 

present in the shell. In this respect, the scroll is more 

like semi-hermetic compressors that have horizontal 

motors partially submerged in oil and refrigerant. When 

Copeland Scroll compressors are hipot tested with liquid 

refrigerant in the shell, they can show higher levels of 

leakage current than compressors with the motor on 

top. This phenomenon can occur with any compressor 

when the motor is immersed in refrigerant. The level of 

current leakage does not present any safety issue. To 

lower the current leakage reading, the system should 

be operated for a brief period of time to redistribute 

the refrigerant to a more normal configuration and the 

system hipot tested again. See 

AE4-1294

 for megohm 

testing recommendations. 

Under no circumstances 

should the hipot test be performed while the 

compressor is under a vacuum.

U.L. sets the requirement for dielectric strength testing 

and they should be consulted for the appropriate voltage 

and leakage values. 

Final Run Test

Customers  that  use  a  nitrogen  final  run  test  must 

be careful to not overheat the compressor. Nitrogen 

is not a good medium for removing heat from the 

compressor, and the scroll tips can be easily damaged 

Summary of Contents for Copeland Scroll ZPV063

Page 1: ...or Overload Protection 7 Oil Type 7 Maximum Tilt Angle 7 Contaminant Control 7 Refrigerant Piping 8 Discharge Check Valve 8 Suction and Discharge Tube Design 8 Compressor Mounting 9 Discharge Mufflers 9 Airborne Sound Control 9 Expansion Devices 9 Reversing Valves 9 Accumulators 10 Off Cycle Migration Control 10 Manifolded Compressors 10 Manifolded Applications 10 Application Tests General Applica...

Page 2: ...e compessor You are strongly advised to follow these safety instructions Safety Icon Explanation DANGER indicates a hazardous situation which if not avoided will result in death or serious injury WARNING indicates a hazardous situation which if not avoided could result in death or serious injury CAUTION used with the safety alert symbol indicates a hazardous situation which if not avoided could re...

Page 3: ...ectrically locking out the system Use only approved refrigerants and refrigeration oils Personal safety equipment must be used Failure to follow these warnings could result in serious personal injury BURN HAZARD Do not touch the compressor until it has cooled down Ensure that materials and wiring do not touch high temperature areas of the compressor Use caution when brazing system components Perso...

Page 4: ...ying conductors RLA MCC 1 4 Max Operating Current The maximum input current to the drive at nominal voltage when the compressor is running inside any one of the operating envelopes at the speed range designated for that envelope Please refer to Table 1 for more technical data for the compressor Power Supply The compressor and drive are an integral and optimized combination The drive will convert t...

Page 5: ...1 drive includes an oil boost cycle when the compressor operates between 1000 and 1800 RPM The oil boost cycle starts once the compressor operates for two hours between 1000 and 1800 RPM During the oil boost cycle the drive forces the compressor to run for five minutes at 3600 RPM After operating for five minutes at 3600 RPM the drive allows the compressor to operate between 1000 and 1800 RPM Figu...

Page 6: ...t in oil pump out if the system has long interconnecting piping Customers that choose to operate in these higher evaporating temperature areas should use a compressor sample with a sight tube during system development testing to ensure that an adequate level of oil is maintained in the compressor sump Sight tubed compressors for monitoring the oil level are available by contacting Application Engi...

Page 7: ...r protective equipment gloves eye protection etc must be used when handling POE lubricant POE must not come into contact with any surface or material that might be harmed by POE and spills should be cleaned up quickly with paper towels soap and water Maximum Tilt Angle Applications such as transportation air conditioning or mobile radar applications may require the compressor to operate at some an...

Page 8: ...of the sight glass The compressor oil level should be checked with the compressor off to avoid the sump turbulence when the compressor is running These compressors are available to the OEM with a production sight glass that can be used to determine the oil level in the compressor in the end use application These compressors are also available to the OEM with an oil Schrader fitting on the side of ...

Page 9: ... not have the ability to control the refrigerant flow across a wide range of operating pressures and flow rates required by the variable capacity system To better control superheat an electronic expansion valve EXV is recommended Electronic expansion valves have the ability to more precisely control superheat at lower settings over a wider operating range than a TXV They also have the capability t...

Page 10: ...d to at least 100 Watts when the compressor is off To use fewer than 100 Watts or to comply with future DOE requirements for off cycle power consumption off cycle migration testing must be performed A 70 watt crankcase heater may be used instead of the motor windings to provide heat to the base CAUTION Stator heat for off cycle migration must not be energized when the system is in a vacuum or if t...

Page 11: ...w system designs should be evaluated throughout the entire expected operating range of the unit to ensure the system will perform reliably throughout the life of the product Test data taken throughout the operating range of the unit should be closely scrutinized to help identify gross errors in system design that may produce conditions that could lead to compressor failure General Application Test...

Page 12: ...rmally low suction pressures during charging NOTICE Do not operate the compressor without enough system charge to maintain at least 55 psig 3 8 bar suction pressure Do not operate the compressor with the low pressure cut out disabled Do no operate with a restricted suction or liquid line Depending on the discharge pressure allowing pressure to drop below 55 psig 3 8 bar for more than a few seconds...

Page 13: ...damage to the drive Measuring the current in the three individual wires feeding the compressor will provide no useful information to the service technician other than to show that each winding of the compressor is drawing current The more appropriate measurement is the current input to the drive Current input to the drive can be compared to the published values of MCC and RLA Compressor Replacemen...

Page 14: ...ndem Cubic Centimeters Per Revolution 3 numeric characters Optional E POE Oil P POE R410A 1st Generation VS Only K1 Nominal Capacity Capacity at Rating Condition Multiplier 2 3 numeric characters K 1 000 M 10 000 C SCFM VARIABLE SPEED COMPRESSOR NOMENCLATURE Application Range Code Application Refgn Substance Compressed P AC HP R 410A B H Heat Pump Optimized R410A Figure 1 Compressor Nomenclature E...

Page 15: ...75 80 85 90 Tcond F Tevap F ZPV063 Operating Envelope 20 F 11 C SH 15 F 8 C SC 95 F 35 C Ambient Solid Line Boundaries OEM tes ng is required to monitor the DLT in the dashed line boundaries 2600 6000 RPM 2200 6000 RPM 1800 7200 RPM Tcond C Tevap C DLT 275 F 1000 7200 RPM An Oil Boost Cycle Is Required For Speeds 1000RPM 1800RPM Cycle Parameters 1000RPM 1800RPM For 2 Hours Ramp To 3600RPM For 5 Mi...

Page 16: ...ise superheat A cold sump may result in high refrigerant migration after shut down Figure 4 Oil Dilution Chart 30 25 20 15 10 5 0 5 10 24 14 4 6 16 26 36 10 0 10 20 30 40 50 60 70 80 90 100 110 20 10 0 10 20 30 40 50 Evaporating Temperature C Compressor Sump Temperature C Compressor Sump Temperature F Evaporating Temperature F 200 F 93 3 C Max Oil Temp Acceptable Unacceptable Too Much Refrigerant ...

Page 17: ... Add braze material to the joint while moving torch around joint to flow braze material around circumference After braze material flows around joint move torch to heat Area 3 This will draw the braze material down into the joint The time spent heating Area 3 should be minimal As with any brazed joint overheating may be detrimental to the final result Field Service WARNING Remove refrigerant charge...

Page 18: ...18 2016 Emerson Climate Technologies Inc AE4 1402 R4 Figure 6 ...

Page 19: ...arge Thermistors Fluid Brake Sight Glass Floating Seal 7 8 22 3mm Discharge Fitting 1 1 8 28 7mm Fixed Scroll BPM Motor Orbiting Scroll Counterweight Cup for Oil Circulation Positive Displacement Oil Pump Suction Fitting Management Figure 8 ZPV063 Cross Sectional View ...

Page 20: ...E 1 E 9 X X X First Character Second Character Third Character Follows VS Motor Type VS Fixed Tandem Follows Fixed Electrical Code E E E E F Z E W Y X E B X F C X W G Examples 2E9 TFD 2ZD 3X9 TF7 3C7 4E9 TE5 4E5 5X9 TEE 5BE Figure 9 Electrical Nomenclature For Multiples ...

Page 21: ...scharge Line Thermistor 085 0261 00 ZPV063 Fits 7 8 Tube Discharge Line Thermistor Molex Connector 085 0211 00 ZPV063 Fits 7 8 Tube Thermistor Clip 032 0688 04 ZPV063 7 8 Clip Suction Discharge Discharge Rotalock O Ring Seal 020 0028 02 ZPV063 Suction Rotalock O Ring Seal 020 0028 03 Discharge Rotalock Service Valve 7 8 998 0510 90 Suction Rotalock Service Valve 1 1 8 998 0510 99 Discharge Rotaloc...

Page 22: ... 1 Motor Poles 6 Motor Input Frequency Hertz 50 360 Recommended Switching Frequency Hertz 6 000 Table 2 Compressor Motor Specifications Drive Model EVC1150B K1 114 EVC1150B L1 114 EVC1150B J1 114 Compressor Model ZPV0631E 4E9 ZPV0631E 4E9 ZPV0631E 5E9 Drive Voltage Input 380 480 500 575 200 240 Drive Nominal Power 15 KW 15 KW 15 KW Drive Max Continuous Output Current 31 Amps 27 Amps 58 Amps NOTE C...

Page 23: ...s kg ZPV063 15 7 18 8 18 8 Charge allowance for system Speed Range RPM Default RPM Acceleration RPM Sec Deceleration RPM Sec Notes Range Default Range Default Start 3600 7200 3600 400 1000 1 0 NA NA 1 Run 1000 7200 200 RPM S Stop 1000 7200 3600 or Envelope Minimum NA NA 50 500 2 0 2 3 4 Notes 1 Once the compressor reaches 3600 RPM hold for two minutes prior to accelerating or decelerating 2 If env...

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