Emerson Copeland Scroll ZH13 KVE Instruction Manual

Scroll compressors with
vapour injection for
Dedicated Heat Pumps
ZH13 KVE & ZH18 KVE
Application Guidelines

C6.2.17/1004/E 1
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, Z ZH H1 13 3K KV VE E … … Z ZH H1 18 8K KV VE E
1Introduction ..........................................................................................................................................................2
2Safety Instructions................................................................................................................................................2
3EVI Theory of Operation ......................................................................................................................................3
4Nomenclature.......................................................................................................................................................5
5Qualified Refrigerant ............................................................................................................................................5
6Application Envelope ...........................................................................................................................................5
7System Configuration...........................................................................................................................................6
7.1 Liquid Extraction .............................................................................................................................................6
7.2 Heat Exchanger Piping Arrangements ...........................................................................................................6
8System Design Guidelines:..................................................................................................................................7
8.1 Heat Exchanger sizing using Select ...............................................................................................................8
8.2 Liquid and Vapour Injection Line Sizing..........................................................................................................8
8.3 Heat Exchanger TXV Sizing ...........................................................................................................................8
8.4 Solenoid valve.................................................................................................................................................9
9Lubrication............................................................................................................................................................9
10 Accumulators .....................................................................................................................................................10
11 Crankcase Heaters ............................................................................................................................................10
12 Discharge Temperature Protection....................................................................................................................11
13 Standard Motor Protection.................................................................................................................................11
14 Low Ambient Cut-Out ........................................................................................................................................11
15 Pressure Controls ..............................................................................................................................................11
16 Shut-Off..............................................................................................................................................................11
17 Starting...............................................................................................................................................................11
18 Deep-Vacuum Operation ...................................................................................................................................11
19 Electrical Installation ..........................................................................................................................................12
20 High Potential Testing........................................................................................................................................13
21 Compressor Functional Check ..........................................................................................................................13
22 Excessive Liquid Floodback ..............................................................................................................................14
23 Continuous Floodback .......................................................................................................................................14
24 Repeated Floodback during Defrost..................................................................................................................14
25 Installation..........................................................................................................................................................14
26 Service ...............................................................................................................................................................15
27 New Installations................................................................................................................................................15
28 Field Service ......................................................................................................................................................15
29 Shut-off Valves and Adaptors ............................................................................................................................16
30 Shell Temperature .............................................................................................................................................16
31 System Charging Procedure..............................................................................................................................16
32 Unbrazing System Components ........................................................................................................................16
33 Suction Line Noise and Vibration.......................................................................................................................17

1 Introduction
This guideline describes the operating characteristics of the scroll compressors with vapour injection (ZH EVI) for
dedicated heat pumps: ZH13KVE to ZH18KVE. Liquid injection is not approved for these models at this time.
EVI Compressor systems benefit over standard refrigeration compressor systems of equivalent capacity due to the
following:
• Capacity Improvement
The capacity is improved by increasing the enthalpy difference in the system rather than increasing mass flow. This is
accomplished without increasing displacements.
• Increased COP
The efficiency improves due to the fact that the gain in capacity is greater than the increase in power that the
compressor consumes.
• Cost and Energy Advantage
Because a smaller size compressor can be used to achieve the same capacity as a larger conventional model, there
is an inherent cost advantage
2 Safety Instructions
Only qualified personnel should install and repair COPELAND compressors.
• Refrigerant compressors must be employed only for the use they are made for.
C6.2.17/1004/E 2
• Only approved refrigerant and refrigerating oils must be used.
• Do not start the compressor until it is charged with refrigerant.
• Correctly used, the compressor and the pressure line piping may reach temperatures that may
cause burning if touched.
• Wear safety goggles when working on open systems.
• If the refrigerant needs to be removed from the system, do not disperse it in the environment, use
the correct equipment & method of removal.
• For storage, use original packaging and avoid collisions and tilting.
• Trained electrical personnel must connect the compressor and its accessories.
• All valid standards for connecting electrical and refrigeration equipment must be observed.
• Limit values for the supply voltage of the unit may not be exceeded.
• It is not allowed to run a test without the compressor being connected to the system and without
refrigerant. It is of vital importance that the discharge stop valve has been fully opened before the
compressor is started. If the discharge stop valve is closed or partly closed an unacceptable
pressure with accordingly high temperatures may develop. When operating with air the so-called
diesel effect may occur, i.e. the air sucked in is mixed with oil gas and can explode due to the high
temperature, and thereby destroy the compressor.

3 EVI Theory of Operation
Copeland EVI Scroll compressors are equipped with a vapour injection connection for Economizer Operation.
Economizing can be accomplished by utilising a subcooling circuit similar to the circuit shown in Figure 1. This
increases the refrigeration capacity and the system efficiency. The benefits provided will increase as the compression
ratio increases.
The schematic shows a system configuration for the economizer cycle. A heat exchanger is used to provide additional
subcooling to the refrigerant before it enters the evaporator. This subcooling process provides the increased capacity
gain measured in the system. During the subcooling process, a certain amount of refrigerant is evaporated. This
evaporated refrigerant is injected into the compressor and provides additional cooling at higher compression ratios,
similar to liquid injection.
The P-h diagram (Figure 2) shows the theoretical gain in system performance acquired by using the economizer
cycle. The extension outside of the vapour dome provides the enthalpy increase, enhancing system performance.
Although power increases due to the vapour injection into the compressor, there is still an efficiency gain because the
capacity gain exceeds the power increase.
Figure 1. EVI Schematic
C6.2.17/1004/E 3

P
h
m
.
i
im
.+
∆TSC = TLI - TLO
Subcooling in
Heat Exchanger
TLI
TSI
TLO
x
TVO
∆THX
Temp Diff,
TLO - TSI
Superheat at H/X Outlet
Condenser Subcooling
Figure 2. EVI P-h chart
Definition(s) Description
Tc Condensing Temperature
Tli Liquid temperature entering H/X
Tlo Subcooled liquid leaving H/X
Pi Intermediate Pressure
Tsi Saturated temperature at intermediate pressure
Tvo Vapour temperature leaving H/X
Tvi Vapour temperature entering H/X
Tsc Liquid subcooling in H/X
M Evaporator Mass Flow
I Vapour Injection Mass Flow
∆THX Liquid temp out H/X-Liquid- Saturated temperature at intermediate pressure
∆TSC Liquid temp in to H/X- subcooled liquid temp out H/X
C6.2.17/1004/E 4

4 Nomenclature
The model numbers of Copeland Scroll™ compressors have been designed to include a coded nominal capacity at
ARI operating conditions in BTU/h at 60 Hz without vapour injection
All scroll compressors for dedicated heat pumps are charged with ester oil, which is indicated by the letter “E”.
Model Designation ZH18K V E- T W D - 5 24
1 2 3 4 5 6 7
1- Z = Compressor family: Z = Scroll
2- H = Dedicated heat pump compressor
3- Nominal capacity [kW] @ 50 Hz and –7°C evaporating/ 50°C condensing temperatures
4 - Vapour Injection for EVI operation
5 - POE Oil
6 - Motor version
7 - Bill of Material Number
5 Qualified Refrigerant
R407C has been qualified for the scroll compressors with vapour injection for dedicated heat pumps.
6 Application Envelope
R407C Mid-point
Cond
Temp °C
Evaporating
Tem
p
°C
Figure 3. Application envelope of EVI compressors
C6.2.17/1004/E 5

7 System Configuration
7.1 Liquid Extraction
Upstream liquid extraction (before the heat exchanger) is recommended as it optimises the heat exchanger
performance. The TXV regulates the flow of subcooled refrigerant out of the condenser and into the heat exchanger
(Figure 4). Minimum level of condenser natural subcooling has to be guaranteed at the TXV inlet to avoid flash gas,
which would cause the valve to hunt.
Figure 4. Upstream Extraction
7.2 Heat Exchanger Piping Arrangements
Best subcooling effect is assured if counter flow of gas and liquid is provided as shown (see figure 5). In order to Best
subcooling effect is assured if counter flow of gas and liquid is provided as shown (see figure 5). In order to guarantee
optimum heat transfer, the plate heat exchanger should be mounted vertically and vapour should exit it at the top.
VI
VO LI
LO
VO = Vapour temperature leaving H/X
VI = Vapour temperature entering H/X
LI = Liquid temperature entering H/X
LO = Subcooled liquid leaving H/X
Figure 5 H/X Piping Arrangement
C6.2.17/1004/E 6

8 System Design Guidelines:
The following sections discuss system design guidelines for the EVI product.
Please use Copeland Selection Software (SELECT), where all parameters are given for selecting a single heat
exchanger. The Copeland Selection Software can be downloaded from www.eCopeland.comT.
The key parameter in determining the proper heat exchanger size is the Saturated Injection Temperature (Tsi). The
Tsi has been determined through extensive testing. This value can vary for each compressor and should be obtained
from Copeland Selection Software.
After determining the Tsi, a 5K condenser natural subcooling, 5 K heat exchanger ∆THX and 5 K heat exchanger
superheat are targeted. This is done to optimise system performance while maintaining system reliability and
functionality at the same time. Once these parameters are known, the heat exchanger capacity (kW) can be
determined, which gives the required heat exchanger size. (See Figure 6 below)
Figure 6. Heat Exchanger Details
C6.2.17/1004/E 7

8.1 Heat Exchanger sizing using Select
Figure 7 is an extract from SELECT which gives details of Economiser/heat exchanger load (kW) saturated
intermediate temperature (Tsi) and sub-cooled liquid out of heat exchanger.
4K Natural Subcooling in
Condenser
**
*
*Tsi temperature
** T
lo Liquid temperature leaving the heat exchanger
Figure 7. Details on EVI performance given by SELECT software.
Heat exchangers should be sized for nominal operating conditions with adequate design margin to allow for the entire
range of system operation.
8.2 Liquid and Vapour Injection Line Sizing
The liquid line from the heat exchanger to the evaporator should be insulated and kept as short as possible in order to
maximise the subcooling effect.
The vapour injection line from the heat exchanger to the compressor should be 3/8” – 1/2.
8.3 Heat Exchanger TXV Sizing
The heat exchanger expansion device should be designed for maximum load while taking into account partial load
conditions.
C6.2.17/1004/E 8

8.4 Solenoid valve
A liquid line solenoid valve is required to prevent migration of refrigerant to the compressor when it is switched off.
For Multiple compressor application, a solenoid valve in the vapour injection line of each individual compressor is
required. Each solenoid valve has to be energised in parallel to the compressor contactor.
In the case of a single compressor application, the solenoid valve could be placed either on the liquid line before the
Heat exchanger TXV or on the vapour injection line to the compressor. For cost reasons, it is advisable to have the
solenoid valve on the liquid side entering the heat exchanger expansion device.
9 Lubrication
The oil level should be maintained at mid-point of the sight glass. If an oil regulator is being used the level should be
set within the top half of the sight glass. The compressor is supplied with an initial charge of polyolester (POE)
lubricant. In the field the oil level could be topped up with Mobil EAL Arctic 22 CC. The recharge values can be taken
from Copeland Selection Software.
The compressors must be operated with these specific oils only. Under no circumstances are ester oils to be mixed
with mineral oil and/or alkyl benzene when used with chlorine-free refrigerants.
Although there is no flexible mounting of the internal compressor parts, the number of start/stop cycles should be
limited to 10 per hour. A high cycling rate will pump oil into the system and may lead to lubrication failure. Oil leaves
the compressor at start-up regardless of the low oil carry over of the Copeland Scroll. The short running time is
insufficient to return the oil to the compressor and possibly results in a lack of lubricant.
It must be considered that the entire system will be coated with oil to some extent. Oil viscosity changes with
temperature. System gas velocity changes depending on temperature and load. In low load conditions gas velocity
may not be high enough to return oil to the compressor. System piping should be designed to return oil under all
operating conditions.
For proper lubrication the minimum differential between bottom shell (tb) and evaporating (te) temperatures should be
carefully observed as laid out in . On the other hand, the maximum bottom shell temperature should never exceed
93°C, measured close to the bottom center of the compressor.
Figure 8. Minimum bottom shell temperature (tb)
One characteristic of POE is that it is far more hygroscopic than mineral oil (Figure 9). Only brief exposure to ambient
air is needed for POE to absorb sufficient moisture to make it unacceptable for use in a refrigeration system. Since
POE retains moisture chemically it is not possible to completely remove it through the use of vacuum.
Compressors supplied by Copeland contain oil with a low moisture content, and this may rise during the system
assembling process. Therefore it is recommended that a properly sized filter-drier is installed in all POE systems. This
will maintain the moisture level in the oil to less than 50 ppm. If oil is charged into a system it is recommended to
charge systems with POE containing no more than 50 ppm moisture content. If the moisture content of the oil in a
refrigeration system reaches unacceptable high levels, corrosion and copper plating may occur.
C6.2.17/1004/E 9

The system should be evacuated down to 0.3 mbar or lower. If there is uncertainty, as to the moisture content in the
system, an oil sample should be taken and tested for moisture. Sight glass/moisture indicators currently available can
be used with the HFC refrigerants and lubricants; however, the moisture indicator will just show the moisture contents
of the refrigerant. The actual moisture level of POE would be higher than the sight glass specifies. This is a result of
the high hygroscopicity of the POE oil. Oil samples would have to be taken from the system and analyzed to
determine the actual moisture content of the lubricant.
Figure 9. Absorption of moisture in ester oil in comparison to mineral oil in [ppm] by weight at 25°C and 50% relative
humidity. h = hours.
10 Accumulators
An accumulator is normally not required in dedicated heat pump applications.
Durability is ensured by the Copeland Scroll’s inherent ability to handle liquid
refrigerant in flooded start and defrost cycle operation. However, large volumes of
liquid refrigerant which repeatedly flood back to the compressor during normal off
cycles or excessive liquid refrigerant floodback during steady operation can dilute the
oil in any compressor to the point where bearings become inadequately lubricated and
wear may occur. If an accumulator is fitted, and there is no crankcase heater, it should
be piped to allow free liquid drainage during the off cycle as shown in Figure 10.
Recommended tests are described in section 22 to 24.
Figure 10. Accumulator
11 Crankcase Heaters
No crankcase heater (CCH) is required when the system charge does not
exceed 4.5 kg. A CCH is to prevent refrigerant migrating into the shell during
standstill periods. It is recommended to fit a CCH if the compressor is located
outside the building, the system charge is above the limits shown. For correct
mounting location of a CCH please see Figure 11.
Figure 11. Crankcase heater
C6.2.17/1004/E 10

12 Discharge Temperature Protection
Internal discharge temperatures reached under some extreme operating conditions (such as loss of charge or
extremely high compression ratio caused by failure of condenser fan) can cause compressor damage. In order to
guarantee positive compressor protection the compressor must be equipped with an external discharge temperature
sensor. This thermostat is not insulated and the equivalent set point for an insulated sensor is 120°C maximum. A
thermostat should be positioned as shown in Figure 12 below.
Figure. 12. Discharge line thermostat
13 Standard Motor Protection
Conventional inherent internal line break motor protection is provided with models ZH13KVE and ZH18KVE.
14 Low Ambient Cut-Out
A low ambient cut-out may be required for systems using air as a heat source.
15 Pressure Controls
A high pressure cut-out may be required according to individual national regulations and is strongly recommended
with three-phase compressors due to their capabilities of pumping to high pressures once the discharge is obstructed.
For the low-pressure side a minimum working pressure setting of 0.3 bar is recommended.
16 Shut-Off
A check valve in the discharge connection of the compressor prevents the compressor from running backwards for
more than a second or two. This momentary reversal of direction of the scrolls has no effect on compressor durability
and is entirely normal. Additionally there is a dynamic discharge valve mounted on the fixed Scroll, which effectively
eliminates reverse rotation.
17 Starting
During the very brief start-up, a short metallic sound is audible, resulting from initial contacting of the spirals and is
normal. Due to the design of the Copeland Scroll, the internal compression components always start unloaded even if
system pressures are not balanced. In addition, since internal compressor pressures are always balanced at startup,
low-voltage starting characteristics are excellent for Copeland Scroll compressors.
18 Deep-Vacuum Operation
The danger of pulling deep vacuums is avoided due to an internal low vacuum protection which prevents the scrolls
pumping (unloads) when the pressure ratio exceeds approximately 20:1. In order to avoid nuisance trips, it is
recommended to set the low-pressure control as described in Section 15 above.
C6.2.17/1004/E 11

19 Electrical Installation
Independently from the internal motor protection, fuses F6...8 have to be installed before the compressor as shown in
Figure 14 and Figure 15. Selection of fuses has to be carried out according to VDE 0635 or DIN 57635 or IEC 269-1
or EN60-269-1. Motor insulation material class is “B” for models ZH13KVE and ZH18KVE according to IEC 34-1 or
DIN 57530.
The fusite connections are marked as in Figure 13. Recommended wiring diagrams are shown in Figure 14 and
Figure 15. Single-phase compressors are connected to the common (C), start (S) and run (R) connections as usual.
Three-phase models are connected (L1,L2,L3) to T1, T2 and T3.
C
S
R
T1
T3
T2
E.2.09.00
Figure 13. Motor terminal connections
Scroll compressors, like several other types of compressors, will only compress in one rotational direction. Direction of
rotation is not an issue with single-phase compressors since they will always start and run in the proper direction
(except as described in Section 16). However, three-phase compressors will rotate in either direction depending upon
phasing of the power to L1, L2 and L3. Since there is a 50/50 chance of connecting power in such a way as to cause
rotation in the reverse direction, it is important to include notices and instructions in appropriate locations on the
equipment to ensure proper rotation direction is achieved when the system is installed and operated. Verification of
proper rotation direction is made by observing that suction pressure drops and discharge pressure rises when the
compressor is energized. Reverse rotation results in a sound level above that with correct rotation direction, as well
as substantially reduced current draw compared to tabulated values and after several minutes of operation the
compressor’s internal protector will trip.
All three-phase compressors are wired identically internally. As a result, once the correct phasing is determined for a
specific system or installation, connecting properly phased power leads to the same terminals should maintain proper
rotation direction.
Figure 14. Power circuit single phase Figure 15. Power circuit three phase
C6.2.17/1004/E 12

C6.2.17/1004/E 13
20 High Potential Testing
Copeland subjects all motor compressors to a high voltage test after final assembly. This is carried out according to
IEC-34-1.
Since high voltage tests lead to premature aging of the winding insulation we do not recommend additional tests of
that nature. They may also be carried out with new machines only.
If it has to be done for any reason disconnect all electronic devices (e.g. motor protection module, fan speed control,
etc.) prior to testing. The test voltage of 1000 V plus twice the nominal voltage is applied for 1 - 4 seconds between
motor winding (each one of the phases) and the compressor shell: The maximum leak current limit is approximately
10 mA. Repeated tests have to be performed at lower voltages.
Caution: Do not carry out high voltage or insulation tests if the compressor housing is under 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-hermetics (which have horizontal motors
partially submerged in oil and refrigerant). When Copeland Scroll compressors are high potential tested with liquid
refrigerant in the shell they can show higher levels of leakage current than compressors with the motor on top
because of the higher electrical conductivity of liquid refrigerant than refrigerant vapour and oil. However, this
phenomenon can occur with any compressor when the motor is immersed in refrigerant. The levels of current leakage
do 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 high potential tested again.
21 Compressor Functional Check
It is not desirable to perform functional compressor tests where the compressor is turned on with the suction service
valve closed to check how low the compressor will pull suction pressure. Rather, the following diagnostic procedure
should be used to evaluate whether the Copeland Scroll compressor is functioning properly.
1. Proper voltage to the unit should be verified.
2. The normal checks of motor winding continuity and short to ground should be made to determine if the
internal overload motor protector of a ZH13KVE or ZH18KVE model has opened or if an internal short to
ground has developed. If the protector has opened, the compressor must be allowed to cool sufficiently to
allow it to reset.
3. Proper indoor and outdoor fan/blower operation should be verified.
4. With service gauges connected to suction and discharge pressure fittings, turn on the compressor. If suction
pressure falls below normal levels the system is either low on charge or there is a flow blockage in the
system.
5. If suction pressure does not drop and discharge pressure does not rise to normal levels, reverse any two of
the compressor power leads and reapply power to make sure compressor was not wired to run in reverse
direction. If pressures still do not move to normal values, the compressor is faulty.
6. If the reversing valve (if so equipped) checks out satisfactorily, then the compressor current draw must be
compared to published compressor performance data at the compressor operating conditions (pressures and
voltages) and significant deviations (more than ±15%) from published values may indicate a faulty
compressor.

22 Excessive Liquid Floodback
The following tests are for those Air/Water system configurations and charge levels, which need special testing to
verify exemption from the need of an accumulator.
23 Continuous Floodback
To test for excessive continuous liquid refrigerant floodback, it is necessary to operate the system in a test room at
conditions where steady state floodback may occur (low ambient air/water heating). Thermocouples should be
attached to the suction and discharge lines of the compressor (approximately 150 mm from the shell) and insulated. If
the system is designed to be field charged it should be overcharged by 15 % in this test to simulate overcharging
commonly found in field installations.
The system should be operated at an indoor temperature of 20°C and outdoor temperature extremes (-18°C or lower)
which produce floodback conditions. The compressor suction and discharge pressures and temperatures should be
recorded. The system should be allowed to frost up for several hours (disabling the defrost control and spraying water
on the outdoor coil may be necessary) to cause the saturated suction temperature to fall to -30°C or below. The
compressor sump temperature must remain above the saturated suction temperature as determined from Figure 8 or
design changes must be made to reduce the amount of floodback. If an accumulator is used an oil return orifice size
of 1,4 mm is recommended.
24 Repeated Floodback during Defrost
For systems using hot gas bypass defrost, and having refrigerant charge levels above the limits given in Section 11 it
may be necessary to fit an accumulator to trap a certain amount of the returning liquid. A good indication of liquid
return can be low sump temperatures. Obtain a sample compressor with a side sight tube to measure liquid level in
the compressor. Set the system up in a configuration with the indoor unit elevated approximately 1 m above the
outdoor unit with approximately 7 m of connecting tubing with no traps between the indoor and outdoor units. If the
system is designed to be field charged, the system should be overcharged by 15% in this test to simulate
overcharging commonly found in field installations. Record the height of the liquid in the compressor during each
cycle, any protector trips, or any compressor stalls during each test. Review all test results with Copeland Application
Engineering to determine if an accumulator is required for the application.
25 Installation
Four vibration absorber grommets are supplied with each compressor (see Figure 16). They dampen the start-up
surge of the compressor and prevent sounds and vibrations from being transmitted to the compressor base during
operation to a large extent. The metal sleeve inside is intended as a guide to hold the grommet in place. It is not
designed as a load-bearing member, and excessive torquing can crush the sleeve. Its inner diameter is approximately
8.5 mm to fit e.g. an M8 screw. The mounting torque should be 13 ± 1 Nm. It is critically important that the grommet is
not compressed. A clearance space of approximately 2-mm between the bottom of the washer and the top of the
grommet spacer is recommended (see Figure 16).
2mm
Figure 16. Mounting Parts
C6.2.17/1004/E 14

26 Service
Copeland Scroll compressors have copper plated steel suction and discharge tubes. These tubes are far more robust
and less prone to leaks than copper tubes used on other compressors. Due to the different thermal properties of steel
and copper, brazing procedures may have to be changed from those commonly used. For brazing of the tubes see
Figure 15 and the following procedures. Since the discharge stub contains a check valve, care must be taken not to
overheat it as well as to prevent brazing material from flowing into it.
27 New Installations
 The copper-coated steel tubes on scroll compressors can be brazed in approximately the same manner as
any copper tube. Recommended brazing materials: Any silfos material is recommended, preferably with a
minimum of 5% silver. However, 0% silver is acceptable.
 Be sure tube fitting inner diameter and tube outer diameter are clean prior to assembly.
 Using a double-tipped torch apply heat in area
 As the tube approaches brazing temperature, move the torch flame to area 2.
 Heat area 2 until braze temperature is attained, moving the torch up and down and rotating around the tube
as necessary to heat the tube evenly. Add braze material to the joint while moving the torch around the joint
to flow braze material around the circumference.
 After the braze-material flows around the joint, move the 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.
Figure 17. Suction tube brazing
28 Field Service
To disconnect:
 Heat joint areas 2 and 3 slowly and uniformly until the braze material softens and the tube can be pulled out
of the fitting.
To reconnect:
 • Recommended brazing-materials: Silfos with minimum 5% silver or silver braze used on other compressors.
Due to the different thermal properties of steel and copper, brazing procedures may have to be changed from
those commonly used. For brazing of the tubes see Figure 17 and the following procedures.
Since the discharge stub contains a check valve, care must be taken not to overheat it as well as to prevent brazing
material to flow into it.
C6.2.17/1004/E 15

29 Shut-off Valves and Adaptors
Scroll compressors ZH13KVE and ZH18KVE are delivered with brazing connections. Rotalock type shut-off valves
can also fit compressors with braze connections (by the mean of Rotalock adaptors). Rotalock-shut-off valves are
available for the suction as well as the discharge side (see Figure 18 & spare parts list “ZH”).
Torque settings for Rotalock connections:
Torque [Nm]
Rotalock 1"-12UNF 70 – 80
Rotalock 1"1/4-12UNF 110-135
It is strongly recommended to periodically retorque all pipe and fixing connections to the original setting
after the system has been put into operation.
(1) pressure control connection
(2) gauge connection
c
b
a
d
Z.8.09.00
Figure 18. Shut-off valves and adaptors
30 Shell Temperature
Under rare circumstances caused by failure of system components such as the condenser or evaporator fan, or loss
of charge, and depending on the type of expansion control, the top shell and discharge line can briefly but repeatedly
reach temperatures above 177°C as the compressor cycles on its internal protection devices. Care must be taken to
ensure that wiring or other materials, which could be damaged by these temperatures, do not come into contact with
the shell.
31 System Charging Procedure
Rapid charging on only the suction side of a single-phase Scroll equipped system or condensing unit can occasionally
result in a temporary no-start condition for the compressor. The reason for this is that if the flanks of the spirals
happen to be in a sealed position, rapid pressurization of the low side without opposing high side pressure can cause
the spirals to seal axially. As a result, until the pressures eventually equalize, the spirals can be held tightly together,
preventing rotation. The best way to avoid this situation is to charge on both the high and the low side simultaneously
at a rate which does not result in axial loading of the spirals. The maximum charging rate can be determined through
simple tests.
32 Unbrazing System Components
If the refrigerant charge is removed from a scroll-equipped unit by bleeding the high side only, it is sometimes
possible for the scrolls to seal preventing pressure equalization through the compressor. This may leave the low side
shell and suction line tubing pressurized. If a brazing torch is the applied to the low side while the low side shell and
suction line contains pressure, the pressurized refrigerant and oil mixtures could ignite when it escapes and contacts
the brazing flame. To prevent this occurrence, it is important to check both the high and the low side with gauges
before unbrazing, or in the case of repairing a unit on an assembly line, bleed refrigerant from both the low and the
high side. Instructions should be provided in appropriate product literature and assembly (line repair) areas.
C6.2.17/1004/E 16

33 Suction Line Noise and Vibration
Copeland Scroll compressors inherently have low sound and vibration characteristics. However, in some respects, the
sound and vibration characteristics differ from reciprocating compressors and, in rare instances, could result in
unexpected sound complaints.
One difference is that the vibration characteristic of the Scroll compressor, although low, includes two very close
frequencies, one of which is normally isolated from the shell by the suspension of an internally suspended
compressor. These frequencies, which are present in all compressors, may result in a low level “beat” frequency that
can be detected as noise coming along the suction line into a house under some conditions. Elimination of the “beat”
can be achieved by attenuating either of the contributing frequencies. This is easily done by using one of the common
combinations of design configuration described below.
A second difference of the Copeland Scroll compressor is that under some conditions the normal starting motion of
the compressor can transmit an “impact” noise along the suction line. This phenomenon, like the one described
above, also results from the lack of internal suspension, and can be easily avoided by using standard line isolation
techniques as described below.
Recommended configuration (Figure 19):
 Tubing configuration: small shock loop
 Service valve: “angled valve” fastened to unit/wall
 Suction muffler: not required
Alternative configuration:
 Tubing configuration: small shock loop
 Service valve: “straight-through” valve fastened to unit/wall
 Suction muffler: may be required
Figure 19. Suction tube design
C6.2.17/1004/E 17

Notes

C6.2.17 / 1004/E
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a trademark of Copeland Corporation. All other trademarks are the property of their respective owners. Information contained in this brochure is subject to change without notification.
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