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AE4-1322

© 2002 Copeland Corporation
Issued 4-2002
Printed in U.S.A.

9

Expansion valve and evaporator

Expansion valve and evaporator

Expansion valve and evaporator

Expansion valve and evaporator

Expansion valve and evaporator

Expansion valve and evaporator have to be adjusted
using utmost care. This is especially important for
those systems that cover a large control range, e.g.
100% to 25%. In each case, sufficient suction gas
superheat and stable operating conditions must be
assured in full load as well as part load modes.
Depending on the evaporator’s design and performance
range several circuits may be necessary each with
separate expansion and solenoid valves.

3.3 Guidelines for special system variations

3.3 Guidelines for special system variations

3.3 Guidelines for special system variations

3.3 Guidelines for special system variations

3.3 Guidelines for special system variations

Pump down circuit

Pump down circuit

Pump down circuit

Pump down circuit

Pump down circuit

If the evaporator and / or the suction line can become
warmer than the compressor during shutdown, a “pump
down” cycle must be incorporated in addition to the oil
heater.

Additional check valve in the discharge line and

Additional check valve in the discharge line and

Additional check valve in the discharge line and

Additional check valve in the discharge line and

Additional check valve in the discharge line and
automatic sequence control

automatic sequence control

automatic sequence control

automatic sequence control

automatic sequence control

For systems with multi-circuit condensers and / or
evaporators, an increased danger exists when indi-
vidual circuits are shut off. During this period liquid
refrigerant can migrate into the evaporator (no tempera-
ture and pressure equalization possible). In these
cases an additional check valve must be installed in
the discharge line. In addition the compressors should
be operated with an automatic sequence control.

The same is also valid for individual systems without
temperature and pressure equalization during longer
shutdown. In extreme cases a suction accumulator or
“pump down” cycle can also become necessary.

Additional oil level control

Additional oil level control

Additional oil level control

Additional oil level control

Additional oil level control

The above guidelines also apply to systems with long
pipelines (suchas a remote evaporator and / or con-
denser). In addition the compressor must be equipped
with an oil level switch (accessory). For electrical
connection see Section 6.4.

Systems with reverse cycling and hot gas defrost

Systems with reverse cycling and hot gas defrost

Systems with reverse cycling and hot gas defrost

Systems with reverse cycling and hot gas defrost

Systems with reverse cycling and hot gas defrost

These system layouts require individually system
design review to protect the compressor against liquid
slugging and increased oil carry-over.  A suction

accumulator is recommended to protect against liquid
slugging. To effectively avoid increased oil carry-over
(such as due to a rapid decrease of pressure in the oil
separator), the oil temperature must remain at least
54° F above the condensing temperature during charge
over. In addition, it may be necessary to install a
pressure regulator immediately after the oil separator
to limit pressure drop. Under certain conditions it is
also possible to turn off the compressor shortly before
the change over procedure and to restart after pressure
equalization. It must however be assured that the
compressor is operating with the required minimum
pressure differential no longer than 30 seconds (see
application ranges Section 9).

3.4 Additional cooling by means of direct liquid

3.4 Additional cooling by means of direct liquid

3.4 Additional cooling by means of direct liquid

3.4 Additional cooling by means of direct liquid

3.4 Additional cooling by means of direct liquid
injection

injection

injection

injection

injection

Additional cooling is required in areas of high condens-
ing and / or low evaporating temperatures. A relatively
simple method is direct liquid inject at the economizer
connection.

The following criteria must be followed to ensure
reliable operation and to avoid excessive dilution of the
oil.

Liquid inject valve

Liquid inject valve

Liquid inject valve

Liquid inject valve

Liquid inject valve

Specially designed expansion valves are only suitable
for liquid injection. They must control the discharge
temperature to setting of 190°F (e.g. Danfoss TEAT20,
also series 935-101-B, Sporian Y1037).

The valve bulb must be mounted on the discharge line:

Clean the tubes surface carefully to bright metal.
Distance from discharge shut-off valve approx. 8 to
10 inches.

Apply heat transfer paste to the contact surface.

Fix the bulb firmly with adequate pipe clips. Mind
heat expansion!

Insulate the bulb and the section of discharge line

Содержание Copeland Screw SCA2

Страница 1: ...tegration into the refrigeration circuit 4 Integration into the refrigeration circuit 4 Integration into the refrigeration circuit 1 1 Mounting the compressor 1 2 System layout 1 3 Guide lines for special system variations 1 4 Additional cooling by liquid injection 1 5 Additional cooling by external oil cooler 5 Economizer operation 5 Economizer operation 5 Economizer operation 5 Economizer operat...

Страница 2: ... Minimal space requirements and convenient piping design piping design piping design piping design piping design Shortest installed length in its performance category shut off valves connections within compressor dimensions Suction and discharge gas connections can be rotated in 90 increments Terminal box accessible from top wire access from underneath Universal applications Universal applications...

Страница 3: ...process V 2 2 Compression process V 2 2 Compression process V 2 2 Compression process Vi i i i i control control control control control With screw compressors suction compression and discharge occur in one flow direction With this process the suction gas is pressed into the profile hollows by the profile peaks The volume is steadily reduced and it is thereby compressed The compressed gas is then ...

Страница 4: ...ecreases The slide is controlled by a hydraulic piston If the valve CR4 is opened the oil pressure in the pressure chamber increases The slide is moved to the suction side The cooling capacity increases If the valve CR1 CR2 or CR3 is opened the pressure on the hydraulic piston decreases By means of the discharge gas the slide is pressed to the discharge side The cooling capacity is reduced 2 5 Sta...

Страница 5: ...g 10 secs on 10 secs off Solenoid Coil Pulsing 10 secs on 10 secs off Solenoid Coil Pulsing 10 secs on 10 secs off Decreased cooling demand Decreased cooling demand Decreased cooling demand Decreased cooling demand Decreased cooling demand A decreased cooling demand falls below the lower set point operating point C The solenoid valve CR3 now opens for short intervals till the actual value is withi...

Страница 6: ...ing and the rotors The oil then flows together with the compressed vapor into the reservoir vessel Here oil and vapor are separated in a highly efficient process The oil collects in the lower part of the separator vessel and flows back into the compressor either direct or via an external oil cooler Depending on the operating conditions the circulating oil must be cooled with liquid injection or an...

Страница 7: ...e in extended systems is also possible for example with remotely installed condenser Systems with multiple compressors should preferably be designed with individual circuits Parallel compound is possible but requires a special oil equalizing system by means of oil level control 4 1 Mounting the compresso 4 1 Mounting the compresso 4 1 Mounting the compresso 4 1 Mounting the compresso 4 1 Mounting ...

Страница 8: ... espe cially in discharge and economizer lines Therefore critical pipe lengths 15 with their natural fre quencies being in resonance with the compressor pulsations must be avoided Among other things the operating conditions and the refrigerant sonic speed as well as the compressor s pulsation frequency must be considered in the calcula tion The base frequency of the compressor is approx 250Hz 50Hz...

Страница 9: ... systems with long pipelines suchas a remote evaporator and or con denser In addition the compressor must be equipped with an oil level switch accessory For electrical connection see Section 6 4 Systems with reverse cycling and hot gas defrost Systems with reverse cycling and hot gas defrost Systems with reverse cycling and hot gas defrost Systems with reverse cycling and hot gas defrost Systems w...

Страница 10: ...or vibration during operation Check for vibration during operation Check for vibration during operation Check for vibration during operation Calculating the cooling capacity of the liquid Calculating the cooling capacity of the liquid Calculating the cooling capacity of the liquid Calculating the cooling capacity of the liquid Calculating the cooling capacity of the liquid injection valve injectio...

Страница 11: ...e oil line This is to avoid oil migration into the compressor during shutdowns The solenoid valve must be installed close to the compressor s oil inlet connec tion and its electric control should be parallel to the contactor s normally open contact Recommended additional components Sight glass to check oil flow Manual shut off ball valves in both feed and return lines for ease of service Oil filte...

Страница 12: ...rature should be equal to or greater than 250 F As an example figure 11 shows a layout with a primary receiver after the condenser An alternative layout of the thermosyphon circuit as well as refrigerant circulation by means of a pump or an ejection is also possible information upon request 4 Economizer operation 1 1 General 1 1 General 1 1 General 1 1 General 1 1 General SCH2 SCA2 screw compresso...

Страница 13: ...peration with sub cooling circuit 5 3 Economizer operation with sub cooling circuit 5 3 Economizer operation with sub cooling circuit 5 3 Economizer operation with sub cooling circuit 5 3 Economizer operation with sub cooling circuit With this operation mode a heat exchanger is utilized as a liquid sub cooler A part of the refrigerant mass flow from the condenser enters the sub cooler via an expan...

Страница 14: ...pe diameters can be used SCH2 5000 to 9000 1 12 Rotolock SCA2 3500 to 7000 SCH2 11H0 to 14H0 1 12 Rotolock SCA2 9000 to 11H0 Pipe vibrations Due to the pulsations emitting from the profile area of the compressor critical pipe lengths must be avoided See also Section 4 2 5 6 Additional components 5 6 Additional components 5 6 Additional components 5 6 Additional components 5 6 Additional components...

Страница 15: ...rt current value in star mode 1 3 of The start current value in star mode 1 3 of The start current value in star mode 1 3 of The start current value in star mode 1 3 of The start current value in star mode 1 3 of the direct on line value is generally stated the direct on line value is generally stated the direct on line value is generally stated the direct on line value is generally stated the dir...

Страница 16: ...ing motors Part winding motors The following current values appear in the part wind ings PW1 PW2 50 50 Both of the contactors should be selected for at least 60 of the maximum operating current Star delta motors Star delta motors Star delta motors Star delta motors Star delta motors Calculate mains and delta contactor each to at least 60 start contactor to 33 of the maximum operating current Power...

Страница 17: ...rge and a subsequent time delay The layout of correction systems for motors with direct starting is similar CAUTION CAUTION CAUTION CAUTION CAUTION It is essential to observe the general It is essential to observe the general It is essential to observe the general It is essential to observe the general It is essential to observe the general design and layout instruction of the design and layout in...

Страница 18: ...and oil level controls are included CAUTION CAUTION CAUTION CAUTION CAUTION Make sure that the rotation monitoring is Make sure that the rotation monitoring is Make sure that the rotation monitoring is Make sure that the rotation monitoring is Make sure that the rotation monitoring is functioning T functioning T functioning T functioning T functioning Terminal D1 of the erminal D1 of the erminal D...

Страница 19: ...nds M1 Compressor Q1 Main switch R1 Oil heater R2 Oil temperature sensor PTC R3 8 Motor PTC sensor S1 On off switch S2 Fault reset motor discharge temperature and or direction of rotation S4 Fault reset oil level U Screening unit if required such as from Murr Elektronik Y1 SV capacity control Y2 SV capacity control Y3 SV capacity control Y4 SV capacity control Y5 SV liquid line Y6 SV refrigerant i...

Страница 20: ...AE4 1322 2002 Copeland Corporation Issued 4 2002 Printed in U S A 20 Figure22 Partwindingstartwith4 stepcapacitycontrol Figure23 Partwindingstartoptions ...

Страница 21: ...rameters pressure levels liquid tempera tures compared with data according to intermediate temperatures used so far As a consequence this results in a lower numerical value for cooling capacity and efficiency COP Liquid sub cooling Liquid sub cooling Liquid sub cooling Liquid sub cooling Liquid sub cooling With standard conditions no no no no no liquid sub cooling is considered Therefore the rated...

Страница 22: ... for ECO T T T T Technical data of a compressor echnical data of a compressor echnical data of a compressor echnical data of a compressor echnical data of a compressor Hit T Data Window Data appears in which the technical data are listed Further windows Dimensions dimensional drawing and Notes notes and legend Export all data with Print Print out at standard printer or Export asASCII file Export p...

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