Frick HPSH Rotary Screw Compressor Installation Operation and Maintenance Guide

Type
Installation Operation and Maintenance Guide
This manual contains rigging, assembly, start-up, and maintenance
instructions. Read thoroughly before beginning installation. Failure
to follow these instructions may result in personal injury or death,
damage to the unit, or improper operation.
ROTARY SCREW COMPRESSOR
HPSH 2709/2712
Check www.FrickCold.com for the latest version of this publication.
Form 070.750-IOM2 (SEP 2019)
INSTALLATION–OPERATION–MAINTENANCE
File: SERVICE MANUAL–Section 070
Replaces: NOTHING
Dist: 3, 3a, 3b, 3c
070.750-IOM2 (SEP 19)
Page 2
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
Indicates an imminently hazardous situation which, if not avoided, will result in death or serious
injury.
Indicates a potentially hazardous situation or practice which, if not avoided, will result in death or
serious injury.
Safety Precaution Denitions
Indicates a potentially hazardous situation or practice which, if not avoided, will result in damage
to equipment and/or minor injury.
Indicates an operating procedure, practice, etc., or portion thereof which is essential to highlight.
Contents
General information
Preface .............................................................................3
Design limitations .............................................................3
Job inspection ..................................................................3
Standard bare compressor ............................................... 3
Transit damage claims ...................................................... 3
Compressor identication ................................................ 3
Long-term storage ............................................................ 5
Preparing compressor for storage ................................ 5
Maintaining compressor (in storage) ............................ 5
Description ........................................................................5
HPSH compressor ........................................................ 5
Compressor lubrication system ................................... 6
Oil pump (optional) .......................................................6
Construction details ..........................................................6
Design limits .................................................................7
Vibration and sound data .................................................. 7
Installation
Outline dimensions ...........................................................9
Holding charge and storage .............................................. 9
Rigging and handling .........................................................9
Foundation ....................................................................... 9
Customer connections ....................................................10
Vi and effective orice sizes ....................................... 10
Compressor oil ................................................................ 10
Oil pump .........................................................................11
Motor mounting (foot mounted only) .............................. 11
Compressor/Motor coupling requirements .................11
Coupling alignment requirements
(foot mounted only) ....................................................11
Oil heaters - Heating wires and insulation ..................... 12
Oil lters .........................................................................12
Oil cooling requirements ................................................. 12
Dehydration / evacuation test .........................................12
Electrical installation .......................................................12
Operation
Operation and start-up instructions ............................... 13
Low ambient operation .................................................. 13
Initial start-up ................................................................13
Initial start-up procedure ..........................................13
Normal start-up procedure ........................................13
Control system ................................................................ 13
Maintenance
General information .......................................................15
Normal maintenance operations ....................................15
General maintenance .....................................................15
Changing oil ....................................................................15
Recommended maintenance program .......................15
Maintenance schedule .....................................................16
Recommended spare parts ............................................. 16
Vibration analysis ......................................................17
Oil quality and analysis ..............................................17
Operating log ............................................................17
Troubleshooting guide ....................................................17
Abnormal operation analysis and correction .................. 17
Troubleshooting the hpsh compressor ............................ 18
Bare compressor replacement ...................................18
Shutdown due to improper oil pressure ..................... 18
Forms
Compressor prestart checklist .........................................19
Alignment log ..................................................................20
Drive train alignment ....................................................... 20
Operating log sheet ........................................................20
Vibration data sheet ........................................................21
Compressor port locations .............................................. 22
Warning
Caution
Danger
Notice
070.750-IOM2 (SEP 19)
Page 3
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
The information contained in this document is
subject to change without notice
General information
PREFACE
This manual describes the installation, operation, and main-
tenance procedures of HPSH Rotary Screw Compressors.
Notice
FRICK screw compressor repair must only be done by
skilled mechanics who have completed training at FRICK
screw compressor school.
It is most important that these compressors be properly
applied to an adequately controlled refrigerant or gas
system. Consult your authorized Johnson Controls-FRICK
representative for expert guidance in this determination.
Proper performance and continued satisfaction with these
units is dependent upon:
Correct Installation
Proper Operation
Regular, Systematic Maintenance
Proper Package and System Engineering
To ensure correct installation and application, the equip-
ment must be properly selected and connected to a
properly designed and installed system. The engineering
plans, piping layouts, for example, must be detailed in ac-
cordance with the best practices and local codes, such as
those outlined in ASHRAE and EN codes.
A screw compressor is a vapor pump. To ensure that
working uid in the liquid state is not being ingested, per-
form the following steps:
Select controls carefully. Make sure they are in good
operating condition.
Properly size piping and correctly arrange traps, if they
are necessary.
Check that the suction line has an accumulator or slug-
ging protection.
Know the load surges and make provisions for control.
Check that operating cycles and stand still periods are
reasonable.
Size high side components within system and compres-
sor design limits.
HPSH compressors have small clearances and the com-
pressor package and system must be built with a very
high degree of cleanliness.
DESIGN LIMITATIONS
HPSH compressors are designed for operation within the
pressure and temperature limits, which are specied by
Johnson Controls-FRICK and the Johnson Controls-FRICK
selection software CoolWare. They are primarily used for
compressing refrigerant gas and most hydrocarbon gasses.
If your application is for sour gas, there are special require-
ments to protect the compressor. Contact Johnson Con-
trols-FRICK Compressor Engineering for application details.
JOB INSPECTION
Immediately upon delivery examine all crates, boxes, and
exposed compressor and component surfaces for damage.
Unpack all items and check against shipping lists for any
discrepancy. Examine all items for damage in transit.
STANDARD BARE COMPRESSOR
Items not included with bare compressor that are available
as sales order options:
Motor mount
Connection ttings
Coupling
Solenoid valve manifold block assembly
TRANSIT DAMAGE CLAIMS
All claims must be made by consignee. This is an ICC
requirement. Request immediate inspection by the agent
of the carrier and be sure the proper claim forms are ex-
ecuted. Report damage or shortage claims immediately to
Johnson Controls-FRICK Sales Administration Department,
in Waynesboro, PA.
COMPRESSOR IDENTIFICATION
Each compressor has an identication data plate, contain-
ing compressor model and serial number mounted on the
compressor body.
Notice
When inquiring about the compressor or unit, or order-
ing repair parts, provide the model and serial numbers
from the data plate. See Figure 1.
Figure 1: Identication data plate
COMPRESSOR SHAFT
CLOCKWISE ROTATION
R22
COMPRESSOR OPERATES ON AND IS
COMPATIBLE WITH THE FOLLOWING
REFRIGERANTS
R290, R1270, NATURAL GAS
COMPRESSOR OPERATES ON AND IS
COMPATIBLE WITH THE FOLLOWING
REFRIGERANTS
R50, R134a, R170, R290, R404A, R410A, R507,
R513A, R600, R600A, R717, R728, R729, R744,
R1150, NATURAL GAS
COMPRESSOR OPERATES ON AND IS
COMPATIBLE WITH THE FOLLOWING
REFRIGERANTS
534C2933H01
USA
US2430129999900010
10241A89999999R
100 CUMBERLAND VALLEY AVENUE
WAYNESBORO, PA 17268
ROTARY SCREW COMPRESSOR
MODEL NO.
MAX DRIVER SPEED MAX ALLOWABLE PRESSURE
PART NO.
RPM PSIG BARG
ASSEMBLED IN
FROM FOREIGN AND DOMESTIC MATERIALS
SERIAL NO.
89.6
1300
3800
HPSH 2709A
070.750-IOM2 (SEP 19)
Page 4
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
The compressor model number designates the size of the
compressor and its Vi conguration.
Example: HPSH 2709 A
Rotary screw compressor serial numbers identify the
factory that the compressor was manufactured in and its
build date. They are dened by the following information:
HPSH 27 09 A
MODEL / SERIES
HPSH = High Pressure Screw
ROTOR DIAMETER
27 = 273 mm
ROTOR LENGTH DESIGNATION
09
12
Vi CONFIGURATION
A = 2.2 – 5.0
B = 1.7 – 3.0
C = 1.3 – 1.96
Rotor Length ÷ Diameter x 10
Example: 1024 0 A 9 0000015 Z
Plant Decade Month Year
Global Additional
Seq no. Remarks
1024 0 A 9 0000015 Z
Month:
A = JAN, B = FEB, C = MAR, D = APR, E = MAY, F = JUN,
G = JUL, H = AUG, K = SEP, L = OCT, M = NOV, N = DEC
Additional Remarks:
R = Remanufactured
R1 = Rebuild
R2 = Rebuild Plus
Z = Deviation from base conguration.
The name plates in Figure 2 show which refrigerants are
compatible with the compressor as manufactured.
Figure 2: Refrigerant nameplates
COMPRESSOR SHAFT
CLOCKWISE ROTATION
R22
COMPRESSOR OPERATES ON AND IS
COMPATIBLE WITH THE FOLLOWING
REFRIGERANTS
R290, R1270, NATURAL GAS
COMPRESSOR OPERATES ON AND IS
COMPATIBLE WITH THE FOLLOWING
REFRIGERANTS
R50, R134a, R170, R290, R404A, R410A, R507,
R513A, R600, R600A, R717, R728, R729, R744,
R1150, NATURAL GAS
COMPRESSOR OPERATES ON AND IS
COMPATIBLE WITH THE FOLLOWING
REFRIGERANTS
534C2933H01
USA
US2430129999900010
10241A89999999R
100 CUMBERLAND VALLEY AVENUE
WAYNESBORO, PA 17268
ROTARY SCREW COMPRESSOR
MODEL NO.
MAX DRIVER SPEED MAX ALLOWABLE PRESSURE
PART NO.
RPM PSIG BARG
ASSEMBLED IN
FROM FOREIGN AND DOMESTIC MATERIALS
SERIAL NO.
89.6
1300
3800
HPSH 2709A
Table 1: Geometrical swept volume
HPS
rpm
HPSH 2709 HPSH 2712 2%*
2709/2712
m3/h (cfm) m3/h (cfm) Lpm
1450 398 (676) 530 (901) 133/177
1750 480 (816) 640 (1088) 160/213
2950 809 (1,375) 1079 (1833) 270/360
3550 974 (1655) 1298 (2206) 325/433
* Oil ow as a % of swept volume.
Table 2: Compressor Long Term Storage Log
Model Serial no.
Compressor, motor oil
pump & refrigerant pump
shaft rotation 1½ turn
Rotor
housing
charge Charge
added
Visual
inspec-
tion Charge Checked
by Date
070.750-IOM2 (SEP 19)
Page 5
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
Figure 3: Nameplate and Vi locations
LONG-TERM STORAGE
Long-term storage (6 months to 5 years) provisions are
required, regardless of storage environment, if start-up
and useful operation does not occur within six (6) months
of equipment shipment. Special provisions may be re-
quired for storage of less than six (6) months if the storage
area is subject to environments with high humidity, large
changes in temperature, dusty atmosphere, or other un-
usual environmental conditions.
The standard Johnson Controls-FRICK Warranty for an
HPSH screw compressor covers 12 months from start-up
or 18 months from shipment, whichever comes rst. It is
recommended that arrangements be made with the local
Johnson Controls-FRICK service organization (arranged
through factory service) regarding surveillance and main-
tenance during the storage period. It is the customer’s
responsibility to submit a monthly report showing the
condition of the unit and noting any discrepancies to the
guidelines listed herein. Failure to comply with this Long
Term Storage Recommendation may void the warranty.
Long term storage of equipment may lead to the deterio-
ration of components over the period of time. Synthetic
components in the compressor may deteriorate over time
even if they are kept ooded with oil. A warm and dry
environment is essential to minimize environmental and
corrosion damage.
The following guidelines must be followed to maintain the
Screw Compressor Warranty.
PREPARING COMPRESSOR FOR STORAGE
1. Evacuate compressor to remove moisture.
2. Connect the evacuation line to the one Schrader valve
provided with the compressor which is connected to
the SD-1 port on the rotor housing.
2. Break vacuum with dry nitrogen and bring pressure to
0 psig.
3. Pump oil into the same ports mentioned in step 1.
Johnson Controls-FRICK recommends break-in oil P/N
111Q0831809 for storage purposes. The amounts of oil
needed for each compressor are:
HPSH 2709/2712 – 25 gal
4. After the compressor is oil charged, pressurize
compressor 0.3 bar to 1.0 bar (5 psig to 15 psig) with
nitrogen.
MAINTAINING COMPRESSOR (IN STORAGE)
1. Ensure that the 0.3 bar to 1.0 bar (5 psig to 15 psig)
nitrogen charge is maintained with 1.0 bar (15 psig)
preferred.
2. Rotate the male rotor shaft monthly. Mark the shaft to
ensure the rotor does not return to the original posi-
tion.
3. Store the compressor inside a dry building environ-
ment.
4. Grease the male rotor shaft to prevent rust.
5. Record all information in a Compressor Long Term
Storage Log (see Table 2).
Contact Johnson Controls-FRICK Service with any ques-
tions regarding long term storage.
DESCRIPTION
HPSH COMPRESSOR
The FRICK HPSH rotary screw compressor uses mating
asymmetrical prole helical rotors to provide a continuous
ow of vapor and is designed for high-pressure applica-
tions. The compressor incorporates the following features:
Designed for variable speed drive with a range of 600
rpm to 4200 rpm; but can also be operated with a xed
speed motor drive at 2950 rpm and 3550 rpm or a xed
speed engine drive at 1200 rpm.
The HPSH 273 compressor models uses stepless capac-
ity control providing innite unloading capacity down to
about 20% of full load capacity.
The HPSH 273 compressor models have a moveable
slide stop with three Vi ranges offered as standard:
- 2.2 to 5.0
- 1.7 to 3.0
- 1.3 to 1.96
High capacity roller bearings to carry radial loads are
used at both inlet and outlet ends of the compressor.
The High pressure compressor models use heavy duty
four point ball bearings to carry the axial loads on the
rotor for the HPSH 273 compressor models.
The high pressure compressor models uses balance
piston assemblies to limit the axial bearing loads. HPSH
273 compressor models use one at the male and female
inlet ends that require pressure regulation on the oil
supply.
The housings for the HPSH 273 compressor models are
designed for 89 bar (1300 psig) working pressure.
The HPSH 273 compressor models are designed with
multiple ports, including:
Economizer port located at 1.34 Vi.
Liquid injection port located at 1.27 Vi.
Two main oil injection ports - SM2 (1.05 Vi ) for the
two lower Vi ranges (1.3 to 1.96 and 1.7 to 3.0) and
SM1 (1.3 Vi) for the 2.2 Vi to 5.0 Vi range.
All bearing and control oil is vented to lower pressure
locations inside the compressor allowing operation
without an oil pump for most applications.
NAMPLATE
COMPRESSOR
VOLUME RATIO Vi,
STAMPED
070.750-IOM2 (SEP 19)
Page 6
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
The shaft seal is designed with a seal ring made of
silicon carbide mated against a similar material, with
carbon and graphite added to the matrix to provide
self-lubrication, especially for startups.
The shaft seal housing is designed to maintain operat-
ing pressure on the seal much lower than discharge
pressure for increased seal life.
Oil injected into the compressor is directed between
the rotor threads to maintain good volumetric and
adiabatic efciency.
The shaft rotation is clockwise when facing the com-
pressor drive end and is suitable for all types of drives.
Warning
Compressor rotation is clockwise when facing the com-
pressor drive shaft. Never operate the compressor in
reverse rotation as this can result in damage.
The suction and discharge anges are ANSI B16.1 Class
600 type for the HPSH 273 compressor models.
Suction strainers for the HPSH 273 compressor models
are external to the compressor. The strainer specied
must meet the following requirements as a minimum:
Filter Cloth: SS 304, 30 x 150 Mesh, plain Dutch
Weave with 0.009 in. WARP diameter and 0.007 in.
WEFT diameter
Filter Cloth Support: 6 mesh with 0.035 in. wire
diameter, 0.132 in. openings with 62.7% open area
COMPRESSOR LUBRICATION SYSTEM
The lubrication system on a HPSH screw compressor unit
performs several functions:
Provides lubrication to bearings, seal, and rotors.
Provides a cushion between the rotors to minimize
noise and vibrations.
Helps keep the compressor at the proper temperature
and prevents overheating.
Provides oil supply to hydraulically operate the slide
valve and slide stop for the HPSH 273 to provide capac-
ity and volume control.
Provides oil pressure to the balance piston assemblies
to help increase bearing life.
Provides an oil seal between the rotors to prevent rotor
contact or gas bypassing.
Volumizer variable volume ratio control
The FRICK compressor includes a method of varying the
internal volume ratio to match the system pressure ratio.
Control of the internal volume ratio eliminates the power
penalty associated with over- or under-compression. Vol-
ume ratio control is achieved by the use of a slide stop, a
movable portion of the rotor housing assembly that moves
axially with the rotors to control discharge port location.
Stepless capacity control
Capacity control is achieved by use of a movable slide
valve. The slide valve moves axially under the rotors to
provide fully modulated capacity control from 100% to ap-
proximately 20% minimum load capacity.
Approximate minimum load capacity varies slightly with
compressor model, pressure ratio, discharge pressure
level, and rotor speed.
The slide valve is positioned by hydraulic movement of its
control piston. When in the unloaded position, gas is by-
passed back to suction through a recirculation slot before
compression begins and any work is expended, providing
the most efcient unloading method available for part-
load operation of a screw compressor.
OIL PUMP (OPTIONAL)
A demand oil pump is required for low differential pressure
applications (CoolWare provide a warning when the oil
differential pressure is too low). Oil being supplied to the
compressor from the oil separator is at system discharge
pressure. Within the compressor, oil porting to all parts of
the compressor is vented back to a location in the com-
pressor’s body that is at a lower pressure than compres-
sor discharge pressure. All oil entering the compressor
is moved by the compressor rotors, out the compressor
outlet, and back to the system oil separator.
CONSTRUCTION DETAILS
Housing
All HPSH screw compressor castings are 60-40-18 ductile
iron to ensure structural integrity and mechanical and
thermal stability under all operating conditions.
Rotors
The rotors are made from quality, wear-resistant rolled
steel to the exacting tolerances of the latest industry
standard asymmetric prole. The six-lobed male rotor is
directly connected to the driver. The eight-lobed female
rotor is driven by the male on a thin oil lm.
Bearings
Antifriction bearings with L10 rated life in excess of 10,000
hours (using FRICK SuperFilters) at design conditions are
used for reduced frictional horsepower and superior ro-
tor positioning, resulting in reduced power consumption.
Cylindrical roller bearings are provided to handle the radial
loads and the thrust loads are absorbed by preloaded
angular contact ball bearings or four point ball bearings
depending on the compressor model.
Balance piston
The high pressure compressors are equipped with balance
piston assemblies to reduce load on the axial bearings. Oil
pressure is regulated by a modulating pressure regulating
valve and provides the force, and therefore, must remain
as specied by Coolware for specic operating conditions.
Shaft seal
The compressor shaft seal is a single-face balanced type
with a spring-loaded, silicon carbide stationary hardened
surface riding against a rotating seat. Carbon and graph-
ite are added to both surfaces to provide self-lubrication.
During operation it is vented to low pressure to provide
extended life. The compressor can be tted with either
shaft seals as an option.
need to update (table)
070.750-IOM2 (SEP 19)
Page 7
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
Motor mount
The HPSH 273 series compressor is a foot mounted, open
drive model which can be paired with an electric, engine,
or turbine drive.
DESIGN LIMITS
Use CoolWare to determine the limits for a specic
application.
Notes for design limits:
1. CR = Compression Ratio. Absolute discharge pressure
divided by absolute suction pressure.
Figure 4: HPSH 273 Viscosity Requirement as function
of speed
2. Maximum discharge temperature depends on oil type
used - normally 150°C (300°F). Refer to FRICK oil data
for more detail.
3. If oil ow is more than 1.5% of swept volume and the
turndown is more than 3, regulation of the main oil
ow must be used. Turndown is the actual maximum
speed/minimum speed. Coolware calculates the oil ow
in Lpm. See Table 1.
4.
The UNISAB and Quantum panels have several lay-
ers of control functions to secure reliable operation.
Depending on many operating conditions, they unload
the slide valve and reduce or increase speed to keep
the compressor running in a safe way. Only as the last
resort do they initiate an alarm and ultimately stop the
compressor.
This is particularly true for the HPSH 273 compressor
models on applications with high suction pressure, like
fuel gas boosting. The concern is that the high internal
thread pressure may lead to excessive rotor deection
and unwanted contact with the rotor housing. For this
reason, proper calibration of the slide valve and slide
stop is essential.
Note: For 1.3 to 1.96 and 1.7 to 3.0 Vi range machines, the
main oil injection occurs at lower Vi port locations than
compressors operating with the 2.2 to 5.0 Vi range. This
means the UNISAB and Quantum use lower values for
the safeties.
5. In CO2 applications using miscible oil types POE and
PAG, it is extremely critical to keep water content to
the lowest possible - down to 10 ppm is the goal. The
installation must have large lter dryers with replace-
able elements that can be effectively serviced and
vacuum dried before being put back in service.
6. If the temperature difference becomes greater than or
equal to 180°F (355 K) between suction and discharge
the slide valve must be unloaded immediately.
7. The minimum discharge temperature must be a mini-
mum 30°F difference above the maximum dewpoint of
the discharge gases. This applies to part load condi-
tions as well as full load operation.
VIBRATION AND SOUND DATA
The rotors balance grade is G 2.5 according to ISO 1940.
The male rotor drive end of the HPSH 273 compressor is
keyless.
Effective vibration velocity must not exceed 8 mm/s RMS
(0.32 in./s) anywhere on the compressor. Alarm level is 12
mm/s RMS.
Table 3: Critical frequencies
Male rotor, # of lobes 6 Main exciting
frequencies (Hz)
Female rotor, # of lobes 8
Driver speed, rpm typical
Exiting member/event 3000 3600 4200
Male rotor, rotational, 1st order 50 60 72
Male rotor, rotational, 2nd order 100 120 144
Female rotor, rotational, 1st 37.5 45 54
Female rotor, rotational, 2nd 75 90 108
Discharge gas pulsation, 1st 300 360 432
Discharge gas pulsation, 2nd 600 720 864
Vibration level on the package can be higher, especially
on piping elements, and when the natural frequency of an
element falls together with one of the exciting frequen-
cies. If the vibration level gets too high, a skip frequency
function in the control system is activated. When acti-
vated, the motor runs through the critical speed very fast,
not causing any continuously high vibration.
Shaft speed, rpm
1000
20
15
10
5
002000 3000 4000 5000
Viscosity Min., cst
070.750-IOM2 (SEP 19)
Page 8
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION - OPERATION - MAINTENANCE
070.750-IOM2 (SEP 19)
Page 9
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION
Installation
RIGGING AND HANDLING
The compressor can be moved with rigging, using a crane
or forklift, by hooking into the two lifting rings at each end
of the main housings. Only use the compressor lifting rings
to lift the compressor itself.
Figure 5: Lifting Rings
FOUNDATION
Each HPSH Rotary Screw Compressor is shipped mounted
on a wooden skid. Remove before installing the unit.
Caution
Allow proper spacing for servicing (see Dimensional
Outline Drawing).
The rst requirement of the compressor foundation is that
it must be able to support the weight. The weights of the
HPSH 2709 and HPSH 2712 assemblies respectively, are
2132 kg (4700 lb) and 2241 kg (4940 lb).
Screw compressors are capable of converting large quan-
tities of shaft power into gas compression in a relatively
small space. The compression process creates relatively
high frequency vibrations that require sufcient mass
in the base to effectively dampen them. Refer to FRICK
070.210-1B Screw Compressor Foundations.
The best insurance for a trouble-free installation is to
rmly anchor the compressor to a suitable foundation
using proper bolting and by preventing piping stress from
being imposed on the compressor. After the compressor
is rigged into place, its feet must be shimmed to level it.
There must be absolutely no stresses transferred to the
compressor body due to bolting of the feet and anges.
In any screw compressor installation, support suction and
discharge lines in pipe hangers, preferably within 2 ft of
vertical pipe run, so that the lines won’t move if discon-
nected from the compressor. See Table 4 for Allowable
ange loads.
HPSH 273 compressors are designed to be driven with an
open drive, foot mounted motor. The rotor and bearing
design set limitations must not be exceeded (See Cool-
Ware). Refer to Johnson Controls-FRICK Compressor Con-
trol Panel instruction 090.040-O for additional information
on setpoint limits.
OUTLINE DIMENSIONS
Complete dimensions and connection information can be
found on the outline drawing which can be requested by
contacting Johnson Controls-FRICK Sales. See Compressor
Port Locations.
HOLDING CHARGE AND STORAGE
Every HPSH compressor is pressure and leak tested at the
Johnson Controls–FRICK Factory and thoroughly evacuated
and charged with dry nitrogen to ensure its integrity dur-
ing shipping and short term storage before installation.
Keep all compressors in a clean, dry location to prevent
corrosion damage. For compressors stored for more than
two months, check their nitrogen charge periodically. See
General Information for complete instructions and refer
to FRICK Form 020.050-W 2012 Screw Compressor Long
Term Storage for FRICK Bare Screw Compressors.
Warning
Holding-charge shipping gauges (if mounted) are rated
for 2.1 bar (30 psig) and are for checking the shipping
charge only. They must be removed before pressure
testing and operating the system. Failure to remove
these gauges may result in catastrophic failure of the
gauge resulting in serious injury or death.
Access valves are bronze and they must be replaced
with steel plugs when package is assembled.
Caution
This equipment has been pressurized with
nitrogen gas. Temporary valves and gauges have been
installed.
1. Relieve pressure before opening lines or making
eld connections.
2. Remove charging valves or gauges be pressurizing
system.
3. Refer to installation operation and maintenance
manual for additional information.
Escaping gas may cause injury
LIFTING RINGS
070.750-IOM2 (SEP 19)
Page 10
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION
CUSTOMER CONNECTIONS
In addition to the suction and discharge connections, the
following ports require piping for operation of the com-
pressor.
SB-2 and SB-2a Inlet Bearings and Balance Piston
SB-3 Shaft seal, outlet end bearings, and
unloader plug
SM-1 or SM-2 Main oil injection. SM-1 is only used for
2.2-5.0 Vi)
Vi AND EFFECTIVE ORIFICE SIZES
SM-2 is low Vi (1.05), and SM-1 is high Vi (1.3). If unsure,
connect main oil to SM-2. The HPSH 2709 and HPSH 2712
both have factory installed orice plugs (0.469 in. diam-
eter).
Other connections are available for instrumentation and
service as noted on the Dimensional Outline drawing.
The oil supply system for the compressor must be de-
signed for a total pressure drop of no more than 1 bar
(15 psi) with a new oil lter element. This is critical for the
proper operation of the balance piston which is used to
ensure the life of the male and female axial bearing.
If the speed turndown is more than 3, then automated
regulation of the main oil ow is required (in order to keep
a high discharge temperature at any speed and prevent oil
slugging at slow speeds).
COMPRESSOR OIL
Warning
DO NOT MIX OILS of different brands, manufacturers,
or types. Mixing of oils can cause excessive oil foaming,
nuisance oil level cutouts, oil pressure loss, gas or oil
leakage and catastrophic compressor failure. CoolWare
selects a specic FRICK oil for the refrigerant being
used. Depending on the application, a different oil can
be selected provided it is of the proper viscosity and
is compatible with the refrigerant and compressor
elastomers.
Figure 6: SM-1 and SM-2 Port Cutaways
A
A
B
B
SM-1
(Port SM-1 Orice Plug)
SM-2
(Port SM-2 Orice Plug)
070.750-IOM2 (SEP 19)
Page 11
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION
Notice
The FRICK oil charge shipped with the unit is the best
suited lubricant for the conditions specied at the time
of purchase. If there is any doubt due to the refrigerant,
operating pressures, or temperatures, refer to FRICK
Oil publication 160.802-SPC.
OIL PUMP
If your HPSH compressor application requires an oil pump,
it is recommended that a strainer be mounted upstream to
protect it. FRICK supplied pumps are a positive displace-
ment gear type that must have a safety relief valve to en-
sure the oil pressure does not go above 50 psi compressor
discharge pressure for all models.
Caution
If oil pressure exceeds 55 psi above compressor dis-
charge it could cause catastrophic compressor failure
due to axial bearing failure. See CoolWare for your
application’s requirements.
MOTOR MOUNTING (FOOT MOUNTED ONLY)
1. Thoroughly clean the motor feet and mounting pads of
grease, burrs, and other foreign matter to ensure rm
seating of the motor.
2. Attach the motor to the base using bolts and motor
raising blocks, if required.
3. Weld the four kick bolts (not included with compres-
sor) into place so that they are positioned to allow
movement of the motor feet.
4. After the motor has been set, check to see that the
shafts are properly spaced for the coupling being used.
Check the appropriate dimensional outline drawing for
the minimum clearance required between the shaft
ends to change the shaft seal.
COMPRESSOR/MOTOR COUPLING REQUIREMENTS
HPSH compressors are arranged for direct motor drive and
require a exible drive coupling to connect the compressor
to the motor. Coupling must be suitable for variable speed.
The HPSH 273 models use a keyless drive shaft.
For a foot mounted motor, it is essential to properly align
the coupling to ensure proper bearing and seal perfor-
mance:
1. Select and install coupling so that it doesn’t transmit
any axial load to the compressor shaft.
2. Set up the minimum distance between compressor
shaft and motor shaft to allow for seal removal (see
Outline drawings).
3.
Coupling must be able to take up any misalignment
between motor and compressor. It is critical to the
life of the shaft seal that misalignment is kept to the
minimum possible value. Be sure to follow the coupling
manufacturer’s guidelines for checking and correcting
any misalignment. See the next section for Johnson
Control–FRICK’s requirements.
COUPLING ALIGNMENT REQUIREMENTS
(FOOT MOUNTED ONLY)
Perform coupling alignment before start-up. After the
compressor has been installed on the job site, check align-
ment again and if necessary, correct before start-up. After
a few hours operation, the alignment must be checked
while the package is still hot. Correct hot alignment is
critical to ensure the life of the shaft seal and compressor
bearings.
Maximum radial runout is 0.004 in. total indicator
reading.
Maximum axial runout is 0.004 in. total indicator
reading.
Use a dial indicator or another appropriate measuring
device to determine the Total Indicator Runout.
Check indicator bracket sag as all brackets have some
exibility.
Table 4: Allowable ange loads
Noz. size
NPS
Moments -- ft-lbf (Nm) Load -- lbf (N)
Axial - MRVert. - MCLat. - MLAxial - P Vert. - VCLat. - VL
1 25 (34) 25 (34) 25 (34) 50 (222) 50 (222) 50 (222)
1.25 25 (34) 25 (34) 25 (34) 50 (222) 50 (222) 50 (222)
1.5 50 (68) 40 (54) 40 (54) 100 (445) 75 (334) 75 (334)
2 100 (136) 70 (95) 70 (95) 150 (667) 125 (556) 125 (556)
3 250 (339) 175 (237) 175 (237) 225 (1001) 250 (1112) 250 (1112)
4 400 (542) 200 (271) 200 (271) 300 (1334) 400 (1779) 400 (1779)
5 425 (576) 400 (542) 400 (542) 400 (1779) 450 (2002) 450 (2002)
6 1,000 (1356) 750 (1017) 750 (1017) 650 (2891) 650 (2891) 650 (2891)
8 1,500 (2034) 1,000 (1356) 1,000 (1356) 1,500 (6672) 900 (4003) 900 (4003)
10 1,500 (2034) 1,200 (1627) 1,200 (1627) 1,500 (6672) 1,200 (5338) 1,200 (5338)
14 2,000 (2712) 1,800 (2440) 1,800 (2440) 1,700 (7562) 2,000 (8896) 2,000 (8896)
070.750-IOM2 (SEP 19)
Page 12
HPSH ROTARY SCREW COMPRESSOR
INSTALLATION
The best way to measure this is to attach the dial indicator
and bracket on a pipe at the coupling span distance. Zero
the indicator in the 12:00 position, and rotate the pipe so
the indicator is in the 6:00 position. The reading on the
indicator in the 6:00 position is the bracket sag. This value
must be included in the dial indicator readings when af-
xed to the coupling for an accurate alignment.
OIL HEATERS - HEATING WIRES AND
INSULATION
Your package must be equipped with oil heaters that pro-
vide sufcient heat to prevent condensation from occurring
during startup and shutdown cycles. Insulate the whole
system.
OIL FILTERS
Use of lter elements other than Johnson Controls-FRICK
must be approved in writing by Johnson Controls-FRICK
Engineering or a warranty claim may be denied. Typical oil
lter specication b5 = 75 according to ISO 4572 is required
to obtain the recommended oil cleanliness class 16/14/11
according to ISO 4406.
OIL COOLING REQUIREMENTS
Compressor oil needs to be cooled to control the dis-
charge temperature, maintain proper oil viscosity, and to
preserve the life of the oil. The discharge temperature
depends on application and operation condition (see
CoolWare). For a CO2 compressor, it is typically about
60°C (140°F). For an ammonia heat pump, it can be
120°C (250°F) or higher.
There are applications that it is normal to have discharge
temperatures as high as 150°C (300°F) An ammonia heat
pump is one example. The higher discharge temperature
permits higher process uid temperatures to be achieved.
Another application that typically requires higher discharge
temperatures as high as 150°C (300°F) is natural gas gath-
ering at the wellhead. Moisture is normally present in the
gas and it is imperative that the discharge temperature be
at least 17°C (30°F) higher than the discharge dew point
temperature for the gas.
Notice
The discharge temperature requirement is at any loading
and capacity, any speed, not only at full load.
Run CoolWare with the Water Saturated block checked
to get the discharge dew point temperature for your ap-
plication. Oil temperatures as high as 130°C (266°F) can
be used to achieve the necessary discharge temperature
to prevent moisture from condensing in the oil separator.
Contact Johnson Controls–FRICK for additional information
for natural gas compression.
The main oil injection line that is connected to port SM-1
or SM-2 must have a regulating valve to permit adjust-
ment of the oil ow to maintain the desired discharge
temperature at all times. A non-return valve is also
required in order to prevent gas from owing backward
into the oil system under start-up and transition of
operating conditions
The regulating valve may need to have a motor so the
actual opening/ow can be controlled by the control panel.
This is often needed for heat pumps where a certain
capacity, water temperature, and efciency is expected.
It may also be a requirement when the speed turndown is
signicant (from 4200 rpm to 1000 rpm, for example) as
the relative oil ow may get too high at the lower speed
range. Turndown above 3 requires an automatic valve.
Consult Coolware and the factory.
When considering minimum supply oil temperature, the
use of a thermostatic three-way bypass mixing valve is not
recommended. For alternate methods consult FRICK
Engineering.
Warning
For high temperature applications, consult factory.
Some of the 3-way thermostatic valves do not work at
high temperatures and damage to thermostatic mixing
valves can occur.
A three-way mixing valve, or one of the alternate meth-
ods, provides warm oil to the compressor quickly, reducing
the pressure drop caused by cold, viscous oil. This ensures
proper oil ow and temperature over the full range of oper-
ating conditions. For some applications this valve needs to
be a motor-operated valve controlled by the control panel.
This is needed for a heat pump where the oil is cooled to a
lower temperature than the condensing temperature.
An ideal oil temperature is the same as the condensing tem-
perature, for example 80°C (176°F).
In a heat pump application there is a risk the discharge
temperature gets too low at low speed, therefore some hot
oil must bypass the oil cooler. Discharge temperature must
be a minimum of 10°C (18°F) above condensing tempera-
ture. Consult Coolware and factory, also study PID diagram
examples (see Table of Contents).
DEHYDRATION / EVACUATION TEST
Evacuate the system to 1500 microns. Valve off the
vacuum pump and hold vacuum for one hour.
Pass: Vacuum cannot rise above the 2000 micron level
during a one hour hold period.
Fail: Vacuum reading goes above the 2000 micron
level during a one hour hold period. Identify and
repair any system leaks. Repeat vacuum test until
requirements are met.
ELECTRICAL INSTALLATION
The only electrical connection to be made to the com-
pressor is for the solenoid operated capacity control valve.
070.750-IOM2 (SEP 19)
Page 13
HPSH ROTARY SCREW COMPRESSOR
OPERATION
Operation
INITIAL START-UP
Before the start-up, the prestart check must be accom-
plished. See Forms section for Prestart Checklist.
INITIAL START-UP PROCEDURE
After performing the prestart check, the compressor unit
is ready for start-up. In low ambient conditions, have oil
heaters and heating wires on for 24 hours before start-up.
It is important that an adequate gas load be available to
load test the unit at normal operating conditions. Keep the
following points in mind during initial start-up:
1. For proper and safe operation, the compressor must be
run at the proper speed and discharge pressure. At any
speed, exceeding design conditions creates a potential
hazard.
2. Immediately after start-up, adjust the oil cooling sys-
tem. Adjust it again after 1 to 3 hours when operating
condition are within expected parameters.
3. Pull and clean suction strainer after 24 hours of opera-
tion. If it is excessively dirty, repeat every 24 hours
until the system is clean. Otherwise, follow the normal
maintenance schedule.
4. Perform vibration analysis if preventive maintenance is
required. If performing a vibration analysis, it is neces-
sary to establish a baseline when the system is running
at normal conditions.
NORMAL START-UP PROCEDURE
1. Conrm system conditions permit starting the com-
pressor.
Notice
Ambient temperatures need to be high enough to
prevent excessive condensing; otherwise, initiate oil
heaters and heat tracing 24 hours before start-up.
2. Start the unit.
3. Observe the compressor unit for mechanical tight-
ness of the external piping, bolts, and valves. Ensure
that the machine has no oil and vapor leaks. If any of
these occur, shut down the compressor and correct the
problem as necessary using good safety precautions.
CONTROL SYSTEM
The HPSH compressor and package requires a dedicated
control system, either Quantum or UNISAB. For details on
operation of these control systems, refer to the respective
IOM manuals.
OPERATION AND START-UP INSTRUCTIONS
The FRICK HPSH Rotary Screw Compressor is a compo-
nent in an integrated system. As such, the compressor
operation requires some specic conditions to ensure
trouble-free running.
The information in this section of the manual provides the
logical step by step instructions to properly start up and
operate the HPSH Rotary Screw Compressor in your unit.
Only matters which may inuence the proper operation of
the FRICK HPSH compressor are included.
The following subsections must be read and understood
before attempting to start or operate the unit.
LOW AMBIENT OPERATION
Warning
Everything must be heat traced and insulated - even the
compressor.
It is recommended that package oil separators, the oil pip-
ing, and the oil lter be insulated as a minimum require-
ment to preserve the heat generated by the oil heaters,
to prevent condensation, and to secure lubrication at
start-up.
Heat pump and fuel gas compression applications must
always have the oil separator insulated. Heat pumps often
require the complete suction line to be insulated in order
to prevent condensation and possible slugging. In these
cases, heating wires are required.
With an automated valve, regulate oil ow to the main
oil port being used (SM-2 or SM-1) in order to continu-
ously achieve the highest possible discharge temperature
needed.
070.750-IOM2 (SEP 19)
Page 14
HPSH ROTARY SCREW COMPRESSOR
OPERATION
070.750-IOM2 (SEP 19)
Page 15
HPSH ROTARY SCREW COMPRESSOR
MAINTENANCE
Maintenance
nitrogen or oil. It is also necessary to rotate the shaft
monthly to keep the seal faces lubricated. This is par-
ticularly true on systems known to contain water vapor.
Preventive maintenance is recommended including
measuring of vibration and performing oil analyses.
Inspection is recommended any time a compressor
exhibits a noticeable change in vibration level, noise, or
performance.
CHANGING OIL
Warning
Do not mix oils of different brands, manufacturers, or
types. Mixing of oils may cause excessive oil foaming,
nuisance oil level cutouts, oil pressure loss, gas or oil
leakage and catastrophic compressor failure.
Shut down the unit when changing oil. At the same time,
all oil lter cartridges must be changed and all oil strainer
elements removed and cleaned. The procedure is as fol-
lows:
1. Stop the compressor unit.
2. Lock out the motor starter.
3. Close the suction and discharge service valves.
4. Using appropriate equipment, lower the compressor
pressure to 0 psig.
5. Open the drain valve(s) and drain oil into a suitable
container.
6. Drain the oil lter(s) and the oil coolers.
7. Remove the old lter cartridges, and install new ones.
8. Remove, clean, and reinstall elements in the strainers.
9. Evacuate the unit.
10. Open the suction service valve and pressurize the unit
to system suction pressure. Close the suction valve and
leak test.
11. Add oil.
12. Open the suction and discharge service valves.
13. Remove the lockout from the motor starter.
14. Start the unit.
RECOMMENDED MAINTENANCE PROGRAM
In order to obtain maximum compressor performance
and ensure reliable operation, follow a regular mainte-
nance program. Check the compressor regularly for leaks,
abnormal vibration, noise, and proper operation as well
as maintaining a log. Perform an oil analysis on a regular
basis. It is a valuable tool that can identify the presence
of moisture, acid, metallics, and other contaminants that
shorten compressor life if not corrected. In addition, peri-
odic vibration analysis can be useful in detecting bearing
wear and other mechanical failures.
GENERAL INFORMATION
This section provides instructions for normal maintenance,
a recommended maintenance program, troubleshooting
and correction guides, and typical P and I diagrams.
Warning
This section must be read and understood before at-
tempting to perform any maintenance or service to
the unit.
NORMAL MAINTENANCE OPERATIONS
When performing maintenance you must take several pre-
cautions to ensure your safety:
If the unit is running, press the STOP key.
Stop the motor and lock out starter before performing
any maintenance.
Wear proper safety equipment when the compressor
unit is opened to the atmosphere.
Ensure there is adequate ventilation.
Take necessary safety precautions required for the gas
being used.
GENERAL MAINTENANCE
Proper maintenance is important in order to ensure long
and trouble-free service from your screw compressor.
Some areas critical to good compressor operation are as
follows:
Keep oil clean and dry, and avoid moisture contamina-
tion. After servicing any portion of the refrigeration
system, evacuate to remove moisture before returning
to service. Water vapor condensing in the compres-
sor while running or more likely while shut down, can
cause breakdown of the oil and refrigerant, which can
generate corrosive agents. This can lead to the break-
ing down of bearings and other vital components in a
short time.
Keep the suction strainer clean. Check periodically,
particularly on new systems where welding slag or pipe
scale could nd its way to the compressor suction.
Excessive dirt in the suction strainer could cause it to
collapse, dumping particles into the compressor.
Keep oil lters clean. If lters show increasing pressure
drop, indicating dirt or water, stop the compressor and
change lters. Running a compressor for long periods
with high lter pressure drop can starve the compres-
sor of oil and lead to premature bearing failure. Dual
oil lters are recommended so that the lters can be
changed without shutting down the package.
Avoid slugging the compressor with liquids (refrigerant
and/or oil). While screw compressors are probably the
most tolerant (of any compressor type available today)
of the ingestion of some liquid, they are not liquid
pumps. Make certain a properly sized suction accumu-
lator is used to avoid dumping liquid into compressor
suction.
Protect the compressor during long periods of shut-
down. If the compressor sits for long periods without
running, evacuate to low pressure and charge with dry
070.750-IOM2 (SEP 19)
Page 16
HPSH ROTARY SCREW COMPRESSOR
MAINTENANCE
MAINTENANCE SCHEDULE
Follow this schedule to ensure trouble-free operation of the compressor unit.
Description HPSH 2709/2712
Complete Bearing Kit 534B2853G01
O-ring Kit, HBNR 534B2822H01
Shaft Seal Kit 534A1363G01
Seal Replacement Tool 534C2772G01
Balance Piston Kit 534A1364G01 (Male)
534A1365G01 (Female)
Compressor Tool Kit 534C2844G01
Notice
Refer to the Service Parts List manual, 070.750-
SPL1_HPSH, for detailed parts list.
a. Check bolts, shim packs, center inserts, keys, and all bolt torques.
b. Verify tightness of bolts on suction and discharge anges. See Table 5 for torque requirements.
c. Units with variable speed drives - check for excess vibration and skip frequencies anytime unit operating conditions change.
d. Check and torque all terminals in the processor and starter panel as stated in the specication posted in the enclosure.
e. Check calibration of Slide Valve, Slide Stop, pressures and temperatures. Conduct calibration with NIST certied devices.
f. BPR - Balance Piston Regulation
g. Vibration measurement must be carried out continuously to obtain optimum preventive control on bearings. If not continuously controlled,
then every 6 months, more frequently if levels increase.
Frequency or hours of operation (maximum)
Maintenance
200
1000
5000
8000
10,000
15,000
20,000
25,000
30,000
35,000
40,000
45,000
50,000
55,000
60,000
65,000
70,000
75,000
80,000
85,000
90,000
95,000
Change oil As Directed By Oil Analysis
Oil analysis nEvery 6 Months
Replace lters n n n n n n n n n n n
Clean oil strainers n n n n n n n n n n n
Clean liquid strainers n n n n n n n n n n n
Replace coalescers n n n
Check and clean suction strainer n n n n n n n n n n n
Check coupling (a) nAnnually Regardless of Operating Hours
Suction and disch ange bolts (b) n n n n n n n n n n n n n n n n n n n n n n
VFD units check skip frequency (c) n n n n n n n n n n n n n n n n n n n n n n
Check electrical connections (d) nn n n n n n n n n n n n n n n n n n n
Check sensor calibration (e) nn n n n n n n n n n n n n n n n n n n n
Check BPR function (f) n n n n n n n n n n n n n n n n n n n n n n
Vibration analysis (g) nEvery 6 Months, More Frequently If Levels Increase
Replace shaft seal When Leak Rate Exceeds 7 - 8 Drops a Minute (600 ml in 24 hours)
Compressor
model
Discharge ange to separator ange
6 in. Class 600 Suction ange
8 in. Class 400
Bolt size Torque* (ft-lb) Bolt size Torque* (ft-lb)
HPSH 2709/2712 1 in. 406 1 1/8 in. 647
* Based on: Gaskets-Garlock® Blue-Gard® 3300; Bolts-class 8.8 or stronger hex head bolts, lightly oiled and clean.
RECOMMENDED SPARE PARTS - CURRENT DESIGN
Table 5: Bolt sizes and torque
070.750-IOM2 (SEP 19)
Page 17
HPSH ROTARY SCREW COMPRESSOR
MAINTENANCE
VIBRATION ANALYSIS
Periodic vibration analysis can be useful in detecting
bearing wear and other mechanical failures. If vibration
analysis is used as a part of your preventive maintenance
program, take the following guidelines into consideration:
Always take vibration readings from exactly the same
places and at exactly the same percentage of load.
Use vibration readings taken from the new unit at start-
up as the base line reference.
Evaluate vibration readings carefully as the instrument
range and function used can vary. Findings can be eas-
ily misinterpreted.
Vibration readings can be inuenced by other equip-
ment operating in the vicinity, or connected to, the
same piping as the unit.
OIL QUALITY AND ANALYSIS
High quality and suitable oil is necessary to ensure com-
pressor longevity and reliability. Oil quality rapidly dete-
riorates in systems containing moisture and air or other
contaminants. In order to ensure the quality of the oil in
the compressor unit:
Only use FRICK oil or high quality oils approved by
Johnson Controls-FRICK for your application.
Only use FRICK SuperFilter™ elements. Substitutions
must be approved in writing by Johnson Controls-FRICK
Engineering or warranty claim may be denied.
Participate in a regular, periodic oil analysis program to
maintain oil and system integrity.
OPERATING LOG
The use of an Operating Log permits thorough analysis
of the operation of a system by those responsible for its
maintenance and servicing. Continual recording of gauge
pressures, temperatures, and other pertinent information,
enables the observer and serviceman to be constantly
familiar with the operation of the system and to recognize
immediately any deviations from normal operating condi-
tions. It is recommended that readings be taken at least
daily.
TROUBLESHOOTING GUIDE
Successful problem solving requires an organized approach
to dene the problem, identify the cause, and make the
proper correction. Sometimes it is possible that two
relatively obvious problems combine to provide a set of
symptoms that can mislead the troubleshooter. Be aware
of this possibility and avoid solving the wrong problem.
Warning
Avoid condensation of refrigerant, gases or water in
the compressor. Ambient conditions may require heat
tracing and insulation of the compressor package com-
ponents and piping.
Catastrophic failure may occur if condensation is present.
ABNORMAL OPERATION
ANALYSIS AND CORRECTION
Four logical steps are required to analyze an operational
problem effectively and make the necessary corrections:
1. Dene the problem and its limits.
2. Identify all possible causes.
3. Test each cause until the source of the problem is
found.
4. Make the necessary corrections.
The following list of abnormal system conditions can cause
abnormal operation of the HPSH compressor:
Oil ow too high at low speed.
Discharge temperature too close to condensing tem-
perature.
Insufcient or excessive gas load.
Excessively high suction pressure.
Excessively high discharge pressure.
Excessively high or low temperature coolant to the oil
cooler.
Excessive liquid entering the compressor (slugging).
Insufcient oil cooling.
Excessive oil cooling.
Incorrect gas line sizing.
Improper system piping.
Wrong operation of hydraulic operated plug valve.
Problems in electrical service to compressor.
Moisture present in the system.
Make a list of all deviations from normal compressor
operation. Delete any items that do not relate to the
symptom and separately list those items that might relate
to the symptom. Use the list as a guide to further investi-
gate the problem.
The second step in problem solving is to decide which
items on the list are possible causes and which items are
additional symptoms. High discharge temperature and high
oil temperature readings on a display may both be symp-
toms of a problem and not causally related.
The third step is to identify the most likely cause and take
action to correct the problem. If the symptoms are not
relieved, move on to the next item on the list and repeat
the procedure until you have identied the cause of the
problem. Once the cause has been identied and con-
rmed, make the necessary corrections.
070.750-IOM2 (SEP 19)
Page 18
HPSH ROTARY SCREW COMPRESSOR
MAINTENANCE
TROUBLESHOOTING THE HPSH COMPRESSOR
Notice
Unless the Service Technician has been certied by
Johnson Controls–FRICK to rebuild our compressors,
troubleshooting the compressor is limited to identi-
fying the probable cause. If a mechanical problem is
suspected, contact Johnson Controls–FRICK Service.
DO NOT ATTEMPT TO DISASSEMBLE COMPRESSOR.
BARE COMPRESSOR REPLACEMENT
The following procedure is required only when a bare com-
pressor is replaced in the eld:
1. Verify that main power to the unit is disconnected and
tag the switch.
2. Remove all tubing, piping, and wiring that is connected
to the compressor.
3. Disconnect the coupling from the motor shaft.
4. While supporting the motor and compressor assembly
with a crane, remove the bolts at the motor feet, and
then at the compressor feet.
5. Thoroughly clean the compressor and motor feet and
mounting pads of burrs and other foreign matter to
ensure rm seating of the compressor.
6. Thoroughly clean the new compressor and remove all
cover plates and protection.
7. Install new gaskets and sealing in all connections.
8. Set the new compressor in place and shim feet where
required.
9. Reattach the drive coupling.
10. The shaft alignment must be checked if a factory pro-
vided motor mount is not used.
11. Complete tubing, piping, and wiring.
Note: Refer to 070.660-SM - Bare Rotary Screw Compressor
Replacement when a motor tunnel is installed.
SHUTDOWN DUE TO IMPROPER OIL PRESSURE (HIGH
STAGE AND BOOSTER)
The compressor must not operate with incorrect oil
pressure.
Refer to relevant Control Setup.
070.750-IOM2 (SEP 19)
Page 19
HPSH ROTARY SCREW COMPRESSOR
FORMS
READ THIS FIRST: COMPRESSOR PRESTART CHECKLIST
The installer must check and complete the following items before the arrival of the FRICK Field Service
Supervisor. Details on the checklist can be found in this manual. Certain items on this checklist are reveried
by the FRICK Field Service Supervisor before the actual start-up.
Mechanical Checks
__ Package installed according to FRICK publication
070.210-IB, Screw Compressor Foundations.
__ Conrm that motor disconnect is open
__ Isolate suction pressure transducer
__ Pressure test and leak check unit
__ Evacuate unit
__ Remove compressor drive coupling guard
__ Remove coupling center and do not reinstall
(motor rotation must be checked without center)
__ Check for correct position of all hand, stop, and check
valves before charging unit with oil or refrigerant
__ Charge unit with correct type and quantity of oil
__ Lubricate electric drive motor bearings before
checking motor rotation
__ Check oil pump alignment (if applicable)
__ Check for correct economizer piping (if applicable)
__ Check separate source of liquid refrigerant supply (if
applicable, liquid injection oil cooling)
__ Check water supply for water-cooled oil cooler (if ap-
plicable, water cooled oil cooling)
__ Check thermosyphon receiver refrigerant level (if ap-
plicable, thermosyphon oil cooling)
__
Check for proper pipe supports and correct foundation
__ Check to ensure all piping including relief valves is
completed
After the above items have been checked and veried:
__ Close the main disconnect from the main power supply to the motor starter
__ Close the motor starter disconnect to energize the micro
__ Manually energize oil pump and check oil pump motor rotation
__ Leave micro energized to ensure oil heaters are on and oil temperature is correct for start-up
__ Do not energize compressor drive motor. Only authorized Factory Field Service Technicians are to perform this.
Summary:
Ensure the above items are completed before the FRICK Field Service Supervisor arrives
.
Ensure there is an
uncoupled compressor drive unit (to verify motor rotation and alignment) and energized oil heaters with the oil at the
proper standby temperatures
. Full compliance with the above items contributes to a quick, efcient, and smooth start-up.
The Start-up Supervisor:
1. Veries position of all valves
2. Veries all wiring connections
3. Veries compressor motor rotation
4. Veries oil pump motor rotation
5. Veries the percentage of FLA on the micro display
6. Veries and nalizes alignment (if applicable)
7. Calibrates slide valve and slide stop
8. Calibrates temperature and pressure readings
9. Corrects any problem in the package
10. Instructes operation personnel
Note: Customer connections are to be made as illustarated in the electrical diagram for the motor starter
listed under the installation section and the wiring diagram listed under the maintenance section of the IOM.
Complete and sign this form and fax to 717-762-8624 as conrmation of completion.
FRICK Sales Order Number: _____________________
Compressor Model Number: _____________________
Unit Serial Number: ____________________________
End User Name: _______________________________
Address of Facility: _____________________________
City, State, Zip: ________________________________
Print Name: ___________________________________
Company: _____________________________________
Job Site Contact: _______________________________
Contact Phone Number:_________________________
Signed: ______________________________________
Forms
070.750-IOM2 (SEP 19)
Page 20
HPSH ROTARY SCREW COMPRESSOR
FORMS
ALIGNMENT LOG – FOR ELECTRIC MOTOR DRIVER
Drive Train Alignment
Ambient Temperature at Time of Alignment _______ Oil Separator Temperature at Time of Alignment ________
Motor Coupling Type ___________ Size ___________ Distance Between Coupling Hub Faces __________
Soft Foot Check OK as Found Shimming Required Amount of Shims used to Correct __________
Indicator Readings in in./1000 mm Indicator Clamped to Motor Compressor
Indicator Readings Facing Compressor Motor Magnetic Center Checked Marked N/A
Compressor Coupling Hub Runout ___________ Motor Coupling Hub Runout ____________
Initial Cold Alignment Initial Hot Alignment Final Hot Alignment
Operating Log Sheet
Date
Time
Hour meter reading
Equipment room temp.
Suction pressure
Suction temperature
Suction superheat
Discharge pressure
Discharge temperature
Corresponding temperature
Oil pressure
Oil temperature
Oil lter pressure drop
Separator temperature
Slide valve position
Volume ratio (Vi)
Motor amps / FLA %
Capacity control setpoint
Oil level
Oil added
Seal leakage (drops/min.)
Face Rim
Thickness of Shims Added
Face Rim
Thickness of Shims Added
Face Rim
Thickness of Shims Added
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Frick HPSH Rotary Screw Compressor Installation Operation and Maintenance Guide

Type
Installation Operation and Maintenance Guide

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