USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
1 INTRODUCTION AND SAFETY
1.1 General
These instructions must always be kept
close to the product's operating location or
directly with the product.
Flowserve products are designed, developed and
manufactured with state-of-the-art technologies in
modern facilities. The unit is produced with great
care and commitment to continuous quality control,
utilising sophisticated quality techniques and safety
requirements.
Flowserve is committed to continuous quality
improvement and being at service for any further
information about the product in its installation and
operation or about its support products, repair and
diagnostic services.
These instructions are intended to facilitate
familiarization with the product and its permitted use.
Operating the product in compliance with these
instructions is important to help ensure reliability in
service and avoid risks. The instructions may not
take into account local regulations; ensure such
regulations are observed by all, including those
installing the product. Always coordinate repair
activity with operations personnel, and follow all plant
safety requirements and applicable safety and health
laws and regulations.
These instructions must be read prior to
installing, operating, using and maintaining the
equipment in any region worldwide. The
equipment must not be put into service until all
the conditions relating to safety, noted in the
instructions, have been met. Failure to follow and
apply the present user instructions is considered
to be misuse. Personal injury, product damage,
delay or failure caused by misuse are not covered
by the Flowserve warranty.
1.2 CE marking and approvals
It is a legal requirement that machinery and equipment
put into service within certai n regions of t he world shall
conform with the applicable CE Marking Directive s
covering Machinery and, where appli cable, Low V oltage
Equipment, Electromagnetic Compatibility (EMC),
Pressure Equipment Directive (PED) and Equipment for
Potentially Explosive Atmospheres (ATEX).
Where applicable, the Directives and any additional
Approvals, cover important safety aspects relating to
machinery and equipment and the satisfactory provision
of technical documents and safety instructions. Where
applicable this document incorporates information
relevant to these Directives and App rovals.
To confirm the Approvals applying and if the product is
CE marked, check the serial number plate markings
and the Certification. (See section 9, Certificatio n.)
1.3 Disclaimer
Information in these User Instructions is believed
to be reliable. In spite of all the efforts of
Flowserve Corporation to provide sound and all
necessary information the content of this manual
may appear insufficient and is not guaranteed by
Flowserve as to its completeness or accuracy.
Flowserve manufactures products to exacting
International Quality Management System Standards as
certified and audited by external Quality Assurance
organisations. Genuine parts and accessories have
been designed, tested and incorporated into the
products to help ensure their continued product quality
and performance in use. As Flowserve cannot test
parts and accessories sourced fr om other vendo rs the
incorrect incorporation of such parts and accessories
may adversely affect the performance and safety
features of the products. The failure to properly select,
install or use authorised Flow serve parts an d
accessories is considered to be misuse. Damage or
failure caused by misuse is not covere d by the
Flowserve warranty. In addition, any modification of
Flowserve products or removal of original components
may impair the safety of these products in their use.
1.4 Copyright
All rights reserved. No part of these instruction s may be
reproduced, stored in a retrieval syst em or transmitted
in any form or by any means without prior permission of
Flowserve.
1.5 Duty conditions
This product has been selected to meet the
specifications of your purchaser order. The
acknowledgement of these conditions has been sent
separately to the Purchaser. A copy should be kept
with these instructions.
The product must not be operated beyond
the parameters specified for the application.
If there is any doubt as to the suitability of the
product for the application intended, contact
Flowserve for advice, quoting the serial number.
If the conditions of service on your purchase order are
going to be changed (for ex ample li quid pum ped,
temperature or duty) it is requested that the user seeks
the written agreement of Flowserve before start up.
Page 4 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
1.6 Safety
1.6.1 Summary of safety markings
These User Instructions contain specific safety
markings where non-observance of an instruction would
cause hazards. The specific safety markings are:
This symbol indicates electrical safety
instructions where non-compliance will involve a high
risk to personal safety or the loss of life.
This symbol indicates safety instructions where
non-compliance would af fect personal safety and co uld
result in loss of life.
This symbol indicates “hazardous and toxic fluid”
safety instructions where non-compliance would af fect
personal safety and could result in loss of life.
This symbol indi cates safet y inst ruct ions
where non-compliance will involve some risk to safe
operation and personal safety and would dam age the
equipment or property.
This symbol indicates explosive atmosphere zone
marking according to ATEX. It is used in safety
instructions where non-compliance in the hazardous
area would cause the risk of an expl osion.
This symbol is used in safety instructions to
remind not to rub non-metallic surfaces with a dry
cloth; ensure the cloth is damp. It is used in safety
instructions where non-compliance in the hazardous
area would cause the risk of an explosion.
1.6.3 Safety action
This is a summary of conditions and actions to help
prevent injury to personnel and damage to the
environment and to equipment. For prod ucts used
in potentially explosive atmosphere s section 1.6.4
also applies.
NEVER DO MAINTENANCE WORK
WHEN THE UNIT IS CONNECTED TO POWER
DRAIN THE PUMP AND ISOLATE PIPEWORK
BEFORE DISMANTLING THE PUMP
The appropriate safety precautions should be taken
where the pumped liquids are hazardous.
FLUORO-ELASTOMERS (When fitted.)
When a pump has experienced temperatures over
250 ºC (482 ºF), partial decomposition of fluoroelastomers (example: Viton) will occur . In this
condition these are extremely dangerous and skin
contact must be avoided.
HANDLING COMPONENTS
Many precision parts have sharp corners and the
wearing of appropriate safety gloves and equipment
is required when handling these components. To lift
heavy pieces above 25 kg (55 lb) use a crane
appropriate for the mass and in accordance with
current local regulations.
NEVER OPERATE THE PUMP WITHOUT THE
COUPLING GUARD AND ALL OTHER SAFETY
DEVICES CORRECTLY INSTALLED
This sign is not a safety symbol but indicates
an important instructio n in the assembly pro cess.
1.6.2 Personnel qualification and training
All personnel involved in the operation, installation,
inspection and maintenance of the unit must be
qualified to carry out the work involv ed. If the perso nnel
in question do not already possess the necessary
knowledge and skill, appropriate training and inst ruction
must be provided. If required the operator may
commission the manufactur er/sup plier t o provide
applicable training.
Always coordinate repair activity with operations and
health and safety personnel, and follow all plant
safety requirements and applicable safety and health
laws and regulations.
Page 5 of 52 flowserve.com
GUARDS MUST NOT BE REMOVED WHILE
THE PUMP IS OPERATIONAL
HOT (and cold) PARTS
If hot or freezing components or auxiliary heating
supplies can present a danger to operators and
persons entering the immediate area action must be
taken to avoid accidental contact. If complete
protection is not possible, the machine access must
be limited to maintenance staff only, with clear visual
warnings and indicators to those entering the
immediate area. Note: bearing housings must not be
insulated and drive motors and bearings may be hot.
If the temperature is greater than 68 ºC (175 ºF) or
below 5 ºC (20 ºF) in a restricted zone, or exceeds
local regulations, action as above shall be taken.
NEVER APPLY HEAT TO REMOVE IMPELLER
This could damage the liner plus trapped lubricant or
vapor could cause an explosion.
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
1.6.4 Products used in potentially explosive
THERMAL SHOCK
atmospheres
Rapid changes in the temperature of the liquid within
the pump can cause thermal shock, which can result
in damage or breakage of components and should be
avoided.
The following instructions for pumps and pump
units when installed in potentially explosive
atmospheres must be followed to help ensure
explosion protection. The terminology and
HAZARDOUS LIQUIDS
When the pump is handling hazardous liquids care must
be taken to avoid exposur e to the l iquid by approp riate
siting of the pump, limiting personnel access and by
operator training. If the liquid is flammable and or
explosive, strict safety procedures must be applied.
procedures ensure that the installed pump is in
compliance with the European Directive 94/9/EC,
known as the ATEX Directive, which is mandatory in
Europe and may also be specified in other countries.
Where applicable, both electrical and non-electrical
equipment must meet the requirements 94/9/EC.
Even if the installation is in a region where ATEX is
PREVENT EXCESSIVE EXTERNA L
PIPE LOAD
Do not use pump as a support for piping. Do not mount
expansion joints, u nless all owed by Fl owserve i n writin g,
so that their force, due to internal p ressure, act s on t he
pump flange.
ENSURE CORRECT LUBRICATION
(See section 5, Commissioning, startup, operation and shutdown.)
NEVER EXCEED THE MAXIMUM
DESIGN PRESSURE (MDP) AT THE TEMPERATURE
SHOWN ON THE PUMP NAMEPLATE
See section 3 for pressure versus temperature
ratings based on the material of construction.
NEVER OPERATE THE PUMP WITH
THE DISCHARGE VALVE CLOSED
(Unless otherwise instructed at a specific point in the
User Instructions.)
(See section 5, Commissioning start-up, operation and shutdown.)
not the applicable regulation, the general measures
described shall be followed to ensure safe operation.
The measures are explained under the headings of:
• Avoiding excessive surface temperature
• Preventing build up of explosive mixtures
• Preventing the generation of sparks
• Preventing leakages
• Maintaining the pump to avoid hazard
1.6.4.1 Scope of compliance
Use equipment only in the zone for whi ch it is
appropriate. Always check that the driver , drive
coupling assembly, seal and pump equipment are
suitably rated and/or certifie d for the classi fication of the
specific atmosphere in which they are to be inst alled.
Where Flowserve has supplied only the bare shaft
pump, the Ex rating applies only to the pump. The
party responsible for assembling the pump set shall
select the coupling, driver and any additional
equipment, with the necessary CE Certificate/
NEVER RUN THE PUMP DRY OR
WITHOUT PROPER PRIME (Casing flooded)
Declaration of Conformity establishing it is suitable for
the area in which it is to be installed.
NEVER OPERATE THE PUMP WITH
THE SUCTION VALVE CLOSED
It should be fully opened when the pump is running.
The output from a variable frequency drive (VFD) can
cause additional heating effects in the motor and so,
for pumps sets with a VFD, the ATEX Certification for
the motor must state that it is covers the situation
NEVER OPERATE THE PUMP AT
ZERO FLOW OR FOR EXTENDED PERIODS
BELOW THE MINIMUM CONTINUOUS FLOW
where electrical supply is from the VFD. This
particular requirement still applies even if the VFD is
in a safe area.
THE PUMP SHAFT MUST TURN
CLOCKWISE WHEN VIEWED FROM THE MOTOR
END
It is absolutely essential that the rotation of the motor
be checked before installation of the coupling spa cer
and starting the pump. Incorrect rotation of the pump
for even a short period can unscrew the impeller,
which can cause significant damage.
Page 6 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
1.6.4.2 Marking
An example of ATEX equipment marking is shown
below. The actual classification of the pump will be
engraved on the nameplate.
II 2 GD c IIC 135 ºC (T4)
Equipment Group
I = Mining
II = Non-mining
Category
2 or M2 = high level protection
3 = normal level of protection
Gas and/or dust
G = Gas
D = Dust
c = Constructional safety
(in accordance with EN13463-5)
Gas Group (Equipment Category 2 only)
IIA – Propane (typical)
IIB – Ethylene (typical)
IIC – Hydrogen (typical)
Maximum surface temperature (Temperature Class)
(see section 1.6.4.3.)
1.6.4.3 Avoiding excessive surface temperatures
ENSURE THE EQUIPMENT TEMPERATURE
CLASS IS SUITABLE FOR THE HAZARD ZONE
Pump liquid temperature
Pumps have a temperature class as stated in the
ATEX Ex rating on the nameplate. These are based
on a maximum ambient of 40 ºC (104 ºF); refer to
Flowserve for higher ambient temperatures.
The surface temperature on the pump is influenced
by the temperature of the liquid handled. The
maximum permissible liquid temperature depends on
the temperature class and must not exceed the
values in the table applicable below. The temperature
rise at the seals and bearings and due to the
minimum permitted flow rate is taken into account in
the temperatures stated.
Temperature
class to
EN13463-1
T6
T5
T4
T3
T2
T1
Maximum
surface
temperature
permitted
85 °C (185 °F)
100 °C (212 °F)
135 °C (275 °F)
200 °C (392 °F)
300 °C (572 °F)
450 °C (842 °F)
Temperature limit of liquid
handled (* depending on
material and construction
variant - check which is lower)
Consult Flowserve
Consult Flowserve
115 °C (239 °F) *
180 °C (356 °F) *
275 °C (527 °F) *
400 °C (752 °F) *
The responsibility for compliance with the
specified maximum liquid temperature is with the
plant operator.
Temperature classification “Tx” is used when the liquid
temperature varies and when the pump is requir ed to be
used in differently classified potentially explosive
atmospheres. In this case the user is responsible for
ensuring that the pump surface temperature does not
exceed that permitted in its actual installe d location.
Do not attempt to check the direction of rotation with the
coupling element/pins fitted due to the risk of sev ere
contact between rotating and stationary compo nents.
Where there is any risk of the pump being run against a
closed valve generating high liqui d and casing exte rnal
surface temperatures it is recommended that users fit
an external surface temperature protectio n device.
Avoid mechanical, hydraulic or electrical overlo ad by
using motor overload trips, temperature monitor or a
power monitor and perform rout ine vibrat ion monito ring.
In dirty or dusty environments, regular checks must
be made and dirt removed from areas around close
clearances, bearing housings and motors.
1.6.4.4 Preventing the build up of explosive
mixtures
ENSURE THE PUMP IS PROPERLY FILLED
AND VENTED AND DOES NOT RUN DRY
Ensure the pump and relevant suction and discharge
pipeline system is totally filled with liquid at all times
during the pump operation, so that an explosive
atmosphere is prevented. In addition it is essential to
make sure that seal chambers, auxiliary shaft seal
systems and any heating and cooling systems are
properly filled.
If the operation of the system cannot avoid this
condition the fitting of an appropriate dry run
protection device is recommended (for example liquid
detection or a power monitor).
To avoid potential hazards from fugitive emissions of
vapor or gas to atmosphere the surrounding area
must be well ventilated.
Page 7 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
1.6.4.5 Preventing sparks
To prevent a potential hazard from mechanical
contact, the coupling guard must be non-sparking.
To avoid the potential hazard from random induced
current generating a spark, the earth contact on the
baseplate must be used.
Avoid electrostatic charge: do not rub no n-metallic
surfaces with a dry cloth; en sure cloth is dam p.
When applicable the coupling must be selected to
comply with 94/9/EC and correct alignment must be
maintained.
Additional requirement for metallic pumps on
non-metallic baseplates
When metallic components are fitted on a nonmetallic baseplate they must be individually earthed.
1.6.4.6 Preventing leakage
The pump must only be used to handle liquids
for which it has been approved to have the correct
corrosion resistance.
Avoid entrapment of liquid in the pump a nd associat ed
piping due to closing of su ction an d discharg e valves,
which could cause dangerous excessiv e pressures to
occur if there is heat input t o the liqu id. This ca n occur if
the pump is stationary or running.
Bursting of liquid containing parts due to freezing
must be avoided by draining or protecting the pump
and ancillary systems.
Where there is the potential hazard of a lo ss of a seal
barrier fluid or external flush, the f luid must be monit ored.
If leakage of liquid to atmosphere can result in a
hazard, the installation of a liquid detection device is
recommended.
1.6.4.7 Maintenance of the centrifugal pump to
avoid a hazard
CORRECT MAINTENANCE IS REQUIRED TO
AVOID POTENTIAL HAZARDS WHICH GIVE A
RISK OF EXPLOSION
The responsibility for compliance of maintenance
and compliance during mainten ance with the
specified product is with the plant operator.
To avoid potential explosion hazards during
maintenance, the tools, cleaning and painting
materials used must not give rise to sparking or
adversely affect the ambient conditions. Where there
is a risk from such tools or materials, maintenance
must be conducted in a safe area.
It is recommended that a maintenance plan and
schedule is adopted. (See section 6, Maintenance.)
1.7 Nameplate and safety labels
1.7.1 Nameplate
For details of nameplate, see the Declaration of
Conformity and section 3.
1.7.2 Safety labels
Oil lubricated units only:
DurcoShieldTM (Splash/Shaft Guard) only:
THIS DEVICE IS NOT A CONTAINMENT
SYSTEM NOR A SEAL BACKUP SYSTEM
IT IS A LIMITED PROTECTION DEVICE.
IT WILL REDUCE BUT NOT ELIMINATE
THE PROBABILITY OF INJURY.
Page 8 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
1.8 Specific machine performance
For performance parameters see section 1.5, Dut y
conditions. Where performance data has been supplied
separately to the purchaser these should be obtained
and retained with these User Inst ructions if re quired.
1.9 Noise level
Attention must be given to the exposure of personnel
to the noise, and local legislation will define when
guidance to personnel on noise limitation is required,
and when noise exposure reduction is mandatory.
This is typically 80 to 85 dBA.
The usual approach is to control the exposure time to
the noise or to enclose the machine to reduce emitted
sound. You may have already specified a limiting
noise level when the equipment was ordered,
however if no noise requirements were defined, then
attention is drawn to the following table to give an
indication of equipment noise level so that you can
take the appropriate action in your plant.
Pump noise level is dependent on a number of
operational factors, flow rate, pipework design and
acoustic characteristics of the building, and so the
values given are subject to a 3 dBA tolerance and
cannot be guaranteed.
Similarly the motor noise a ssumed in t he “pump and
motor” noise is that typically exp ected f rom stand ard
and high efficiency motors when on load dire ctly driving
the pump. Note that a motor driven by an inverter may
show an increased noise at some speeds.
If a pump unit only has been purchased for fitting with
your own driver then the “pump only” noise levels in the
table should be combined with the level for the driver
obtained from the supplier. Consult Flowserv e or a
noise specialist if assistance is required in combining
the values.
It is recommended that where exposure approaches
the prescribed limit, then site noise measurements
should be made.
The values are in sound pressure level L
at 1 m
pA
(3.3 ft) from the machine, for “free field conditions
over a reflecting plane”.
1 The noise level of machine s in this range will most likely be of valu es which req uire no ise exposure control, but ty pical values are inappropr iate.
Note: for 1 180 and 960 r/min reduce 1 450 r/min values by 2 dBA. For 880 and 720 r/min reduce 1 450 r/min values by 3 dBA.
3 550 r/min 2 900 r/min 1 750 r/min 1 450 r/min
Pump
only
1
Pump and
Typical sound pressure level LpA at 1 m reference 20 µPa, dBA
motor
1
11
Pump
only
Pump and
motor
Pump
only
8587 8385
Pump and
motor
Pump
only
Pump and
motor
Page 9 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
2 TRANSPORT AND STORAGE
2.1 Consignment receipt and unpacking
Immediately after receipt of the equipment it must be
checked against the delivery/shipping documents for
its completeness and that there has been no damage
in transportation. Any shortage and or damage must
be reported immediately to Flowserve and must be
received in writing within thirty (30) calendar days of
receipt of the equipment. Later claims cannot be
accepted.
Check any crate, boxes or wrappings for any
accessories or spare parts that may be packed
separately with the equipment or attached to side
walls of the box or equipment.
Each product has a unique serial number. Check
that this number corresponds with that advised and
always quote this number in correspondence as well
as when ordering spare parts or further accessories.
2.2 Handling
Boxes, crates, pallets or cartons may be unloaded
using fork lift vehicles or slings dependent on their
size and construction.
2.3 Lifting
Pumps and motors often have integral
lifting lugs or eye bolts. These are intended for use in
only lifting the individual piece of equipment.
2.3.1.3 Bearing housing [3200]
Group A and 1
lower support ribs between the housing barrel an d
the casing attachment flange. Use a choker hitch
when slinging. (Make sure there are no sharp edges
on the bottom side of the ribs that could cut the sling.)
Group B, C and 2
through the lifting lug located on the top of the
housing.
2.3.1.4 Power end
Same as bearing housing.
2.3.1.5 Bare pump
Horizontal pumps
nozzle and around the outboar d end of th e bearing
housing with separate slings. Choker hitches must be
used at both attachment points and pulled tight. Make
sure the completion of the choker hitch on the discharge
nozzle is toward the coupling end of the pump shaft as
shown in Figure 2-1. The sling lengths should be
adjusted to balance th e load bef ore att achi ng the lift ing
hook. Pump models with non standard flanges can not
accommodate a sling around the discharge nozzle;
when lifting these pumps an in dividual trai ned in
properly lifting equipment must be consulted.
Figure 2-1
: insert a sling between the upper and
: insert either a sling or hook
: sling around the pump discharge
Do not use eye bolts or cast-in lifting
lugs to lift pump, motor and baseplate assemblies.
To avoid distortion, the pump unit
should be lifted as shown.
Care must be taken to lift components or
assemblies above the center of gr avity to prev ent the
unit from flipping. This is especially t rue with In -Line
pumps.
2.3.1 Lifting pump components
2.3.1.1 Casing [1100]
Use a choker hitch pulled tight around the discharge
nozzle.
2.3.1.2 Rear cover [1220]
Insert an eye hook in the drilled and tapped hole on
the face of the cover. Use either a sling or hook
through the eye bolt.
Page 10 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
2.3.2 Lifting pump, motor and baseplate assembly
If the baseplate has lifting holes cut in the sides at the
end (Type D and Type E base s) insert lifti ng S hook s at
the four corners and use slings or chains to connect to
the lifting eye. (Figure 2-1.) Do not use slings through
the lifting holes.
For other baseplates, sling around the pump discharge
nozzle, and around the outboard end of the motor
frame using choker hitches pulled tight. Pump models
with non standard flanges can not accommodate a
sling around the discharge nozzle; when lifting these
pumps an individual trained in properly lifting
equipment must be consulted. (Figure 2-1.)
The sling should be positioned so the weight is not
carried through the motor fan housing. Make sure the
completion of the choker hitch on the discharge
nozzle is toward the coupling end of the pump shaft
as shown in Figure 2-1.
2.4 Storage
Store th e pump in a clea n, dry locati on
away from vibration. Leave piping connectio n covers in
place to keep dirt and other foreign material out of pump
casing. T urn pump at int erv als to pr event brinel ling of
the bearings and the seal faces, if fitted, from sticking.
The pump may be stored as above for up to 6
months. Consult Flowserve for preservative actions
when a longer storage period is needed.
2.4.1 Short term storage and packaging
Normal packaging is designed to protect the pump
and parts during shipment and for dry, indoor storage
for up to six months or less. The following is an
overview of our normal packaging:
•All loose unmounted items are packaged in a
water proof plastic bag and placed under the
coupling guard
•Inner surfaces of the bearing housing, shaft (area
through bearing housing) and bearings are coated
with Cortec VCI-329 rust inhibitor, or equal.
2.4.2 Long term storage and packaging
Long term storage is defined as more than six
months, but less than 12 months. The procedure
Flowserve follows for long term storage of pumps is
given below. These procedures are in addition to the
short term procedure.
•Each assembly is hermetically (heat) sealed from
the atmosphere by means of tack wrap sheeting
and rubber bushings (mounting holes)
•Desiccant bags are placed inside the tack
wrapped packaging
•A solid wood box is used to cover the assembly
This packaging will provide protection for up to twelve
months from humidity, salt laden air, dust etc.
After unpacking, protection will be the responsibility of
the user. Addition of oil to the bearing housing will
remove the inhibitor. If unit s are to be idle fo r extende d
periods after addition of lubricants, in hibitor oils a nd
greases should be used. Every three months, the pump
shaft should be rotated approximately 10 revolution s.
2.5 Recycling and end of product life
At the end of the service life of the product or its
parts, the relevant materials and parts should be
recycled or disposed of using an environmentally
acceptable method and local requirements. If the
product contains substances that are harmful to the
environment, these should be removed and disposed
of in accordance with current regulations. This also
includes the liquids and/or gases that may be used in
the "seal system" or other utilities.
Make sure that hazardous substances are
disposed of safely and that the correct personal
protective equipment is used. The safety
specifications must be in accordance with the current
regulations at all times.
Bearing housings are not filled with oil
prior to shipment
•Regreasable bearings are packed with grease
(MOBIL POLYREX EM)
• Exposed shafts are taped with Polywrap
• Flange covers are secured to both the suction
and discharge flanges
•In some cases with assemblies ordered wit h
external piping, components may be
disassembled for shipment
•The pump must be stored in a covered, dry location
Page 11 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
3 DESCRIPTION
3.1 Configurations
PolyChem S-series chemical process pumps are
horizontal, end suction, single stage, centrifugal
pumps. The ISO version of this pump conforms
dimensionally to ISO 2858/5199 while the ANSI
model agrees dimensionally with ASME B73.1. Both
have centerline discharge.
3.2 Nomenclature
The pump size will be engraved on the nameplate
typically as below:
“2” = Nominal suction port size (in.)
“1” = Nominal discharge port size (in.)
“10” = Nominal (max) impeller diameter (in.)
“8.25” = Actual impeller diameter (in.)
Impeller style (ISO or ANSI):
CL = closed vane impeller
OP = Open impeller
Pump design variation (ANSI only):
HD = Heavy duty shaft which is available on all Group 2
pump models. The shaft increases from
47.63 mm (1.875 in.) to 53.98 mm (2.125 in.).
An example of the nameplate used on the PolyChem
pump is shown in Figure 3-1. This nameplate is
always mounted on the bearing housing.
Figure 3-1: Nameplate mounted to housing
Serial No.
Equipment No.
Purchase Order
Model
Material
Date DD/MMM/YY
Size
PS 2 X 1 - 10 / 8.25CL
MDP
3.3 Design of major parts
3.3.1 Pump casing
Removal of the casing is not required when
performing maintenance of the rotating element. The
rotating element is easily removed (back pull out).
3.3.2 Impeller
Depending on the pump size, the impeller is either
closed vane or open.
3.3.3 Shaft/sleeve
Solid and sleeved shafts are available, supported on
bearings, threaded impeller end and keyed drive end.
3.3.4 Pump bearings and lubrication
Ball bearings are fitted as standard and may be either
oil or grease lubricated.
3.3.5 Bearing housing
Large oil bath reservoir.
3.3.6 Seal chamber (cover plate)
The seal chamber has a spigot (rabbet) fit between
the pump casing and bearing housing (adapter) for
optimum concentricity. The design enables a number
of sealing options to be fitted.
3.3.7 Shaft seal
The mechanical seal(s), attached to the pump shaft,
seals the pumped liquid from the environment.
3.3.8 Driver
The driver is normally an electric motor. Different drive
configurations may be fitted such as internal combustion
engines, turbines, hydraulic motors et c drivin g via
couplings, belts, gearboxes, drive shafts etc.
3.3.9 Accessories
Accessories may be fitted when specified by the
customer.
Page 12 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
3.4 Performance and operation limits
This product has been selected t o meet th e
specification of your purchase order. See section 1.5.
The following data is included as additional information
3.4.2 Pressure-temperature ratings
PN 16 flanges are standard for the ISO model pump
while Class 150 flanges are standard for the ANSI
model. Refer to Figure 3-3A and 3-3B for each
pump’s pressure-temperature (P-T) ratings.
to help with your installation. It is typical, and factors
such as liquid being pumped, temperature, material of
construction, and seal type may influence this data. If
required, a definitive statement fo r your appli cation can
be obtained from Flowserve.
3.4.1 Material cross reference chart
Figure 3-2 is the material cross-reference chart for all
PolyChem S-series pumps.
The maximum discharge pressure must be less
than or equal to the P-T rating. Discharge pressure
may be approximated by adding the suction pressure
to the differential pressure developed by the pump.
3.4.3 Suction pressure limits
The suction pressure limits for PolyChem S-series
pumps are limited by the P-T rating.
Figure 3-2: Material cross-reference chart
Flowserve
material code
Z0L48 PFA lined Ductile iron (cast) DIPA None Note 1 1.0
E2025 Ductile Iron Casting 7043 None EN1563, Gr. JS 1025 1.0
E3020 Ductile Iron CastingDCI None A395, Gr. 60-40-18 1.0
D0005 Carbon Steel SR None N/A
D2044 Quenched and Tempered Steel CK45 NoneEN 10083-1 N/A
D3013 1018 Carbon Steel Z None N/A
D3058 304 Stainless Steel 304 NoneA276, Type 304 N/A
D3277 Carbon Steel BB 1144 UNS G11440 N/A
E2008 Ductile Iron Casting7040 None EN1563, Gr. JS 1030 N/A
E3006 Cast Iron Casting CI None A48, Gr. 25A N/A
E3035 Ductile Iron CastingDCI2 None A536, Gr. 65-45-12 N/A
E4034 Ductile Iron CastingDCI4 None Note 2 N/A
®Hastelloy is a registered trademark of Haynes International, Inc.
Note 1. The casting used for ISO pumps is E2025 and for ANSI pumps is E3020
Note 2. Dual Spec. EN1563 Gr. JS1030 & A536 Gr. 65-45-12
Designation
Durco
legacy
codes
Equivalent
wrought
designation
EN/ASTM
specifications
Nozzle load
material group
Page 13 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
Figure 3-3A: Pressure-temperature rating
(ISO pump with PN 16 flanges – Material Group No. 1.0)
Temperature
°C ( °F)
Bar
(psi)
-29
(-20)
16
(232)
-18
(0)
16
(232)
38
(100)
16
(232)
93
(200)
16
(232)
121
(250)
16
(232)
149
(300)
15.5
(225)
Figure 3-3B: Pressure–temperature rating
(ANSI pump with Class 150 flanges – Material Group
No. 1.0)
Temperature
°C ( °F)
Bar
(psi)
-29
(-20)
17.2
(250)
-18
(0)
17.2
(250)
38
(100)
17.2
(250)
93
(200)
16.2
(235)
149
(300)
14.8
(215)
3.4.4 Minimum continuous flow
The minimum continuous flow (MCF) is based on a
percentage of the best efficiency point (BEP). Figure
3-4 identifies the MCF for all PolyChe m S-serie s pump s.
Figure 3-4: Minimum continuous flow
n/a
n/a
n/a
n/a
MCF % of BEP
1 750/1 450
r/min
10 % 10 %
10 % 10 %
20 % 10 %
40 % 10 %
1 180/960
r/min
Pump size
PS3x2-6 20 % 10 % 10 %
PS3x2-10
PS50-250
PS4x3-10
PS65-250
PS3x2-13
PS50-315
PS4x3-13
PS65-315
PS6x4-13HD
PS100-315
All other sizes
3 500/2 900
r/min
30 % 10 % 10 %
10 % 10 % 10 %
4 INSTALLATION
Equipment operated in hazardous locations
must comply with the relevant explosion protection
regulatiuons. See section 1.6.4, Products used in potentially explosive atmospheres.
4.1 Location
The pump should be located to allow room for acce ss,
ventilation, maintenance, and inspe ction with ample
headroom for lifting and should be as close as
practicable to the supply of liquid to be pumped.
Refer to the general arrangement drawing for the
pump set.
4.2 Part assemblies
The supply of motors and baseplates are optional.
As a result, it is the responsibility of the installer to
ensure that the motor is assembled to the pump and
aligned as detailed in section 4.5 and 4.8.
4.3 Foundation
4.3.1 Protection of openings and threads
When the pump is shipped, all threads and all
openings are covered. This protection/covering
should not be removed until installation. If, for any
reason, the pump is removed from service, this
protection should be reinstalled.
4.3.2 Rigid baseplates - overview
The function of a baseplate is to provide a rigid
foundation under a pump and its driver that maintains
alignment between the two. Baseplates may be
generally classified into two types:
• Foundation-mounted, grouted de sign. (Figure 4-1. )
• Stilt mounted, or free standing. (Figure 4-2.)
Figure 4-1
Figure 4-2
Baseplates intended for grouted installation are
designed to use the grout as a stiffening member.
Stilt mounted baseplates, on the other hand, are
designed to provide their own rigidity. Therefore the
designs of the two baseplates are usually different.
Regardless of the type of baseplate used, it must
provide certain functions that ensure a reliable
installation. Three of these requirements are:
•The baseplate must provide sufficient rigidity to
assure the assembly can be transported and
installed, given reasonable care in handling,
without damage. It must also be rigid enough
when properly installed to resist operating loads.
•The baseplate must provide a reasonably flat
mounting surface for the pump and driver.
Uneven surfaces will result in a soft-foot condition
that may make alignment difficult or impossible.
Page 14 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
Experience indicates that a baseplate with a top
surface flatness of 1.25 mm/m (0.015 in./ft) across
the diagonal corners of the baseplate provides
such a mounting surface. Therefore, this is the
tolerance to which we supply our standard
baseplate. Some users may desire an even flatter
surface, which can facilitate installation and
alignment. Flowserve will supply flatter baseplates
upon request at extra cost. For example,
mounting surface flatness of 0.17 mm/m
(0.002 in./ft) is offered on the Flowserve Type E
“Ten Point” baseplate shown in Figure 4-1.
•The baseplate must be designed to allow the user
to final field align the pump a nd drive r to within th eir
own particular standards and to compensate for
any pump or driver movement that occurred during
handling. Normal industry practice is to achieve
final alignment by moving the motor to match the
pump. Flowserve practice is to confir m in our shop
that the pump assembly can be accurately aligned.
Before shipment, the factory verifies that there is
enough horizontal movement capability at the motor
to obtain a “perfect” final alig nment wh en the
installer puts the baseplate assembly into its
original, top levelled, unstressed conditi on.
4.3.3 Stilt and spring mounted baseplates
Flowserve offers stilt and spring mounted baseplates.
(See Figure 4-2 for stilt mounted option.) The low
vibration levels of PolyChem pumps allow the use of
these baseplates - provided they are of a rigid design.
The baseplate is set on a flat surface with no tie down
bolts or other means of anchoring it to the floor.
General instructions for assembling these baseplates
are given below. For dimensional information, please
refer to the appropriate Flowserve “Sales print”.
4.3.3.1 Stilt mounted baseplate assembly
instructions
Refer to Figure 4-3.
a) Raise or block up baseplate/pump above the floor
to allow for the assembly of the stilts.
b) Predetermine or measure the approximate
desired height for the baseplate above the floor.
c) Set the bottom nuts [2] above the stilt bolt head
[1] to the desired height.
d) Assemble lock washer [3] down over the stilt bolt.
e) Assemble the stilt bolt up through hole in the
bottom plate and hold in place.
f) Assemble the lock washer [3] and nut [2] on the stilt
bolt. Tighten the nut down on the lock washer.
g) After all four stilts have been assembled, position
the baseplate in place, over the floor cups [4]
under each stilt location, and lower the baseplate
to the floor.
h) Level and make final height adjustments to the
suction and discharge pipe by first loosening the
top nuts and turning the bottom nuts to raise or
lower the baseplate.
i) Tighten the top and bottom nuts at the lock
washer [3] first then tighten the other nuts.
j) It should be noted that the connecting pipelines
must be individually supported, and that the stilt
mounted baseplate is not intended to support
total static pipe load.
Refer to Figure 4-4.
a) Raise or block up baseplate/pump above the floor
to allow for the assembly of the stilts.
b) Set the bottom nuts [4] above the stilt bolt head [1].
This allows for 51 mm (2 in.) upwa rd movement f or
the final height adjustment o f the suctio n/discha rge
flange.
c) Assemble the lock washer [6] flat washer [5] and
bottom spring/cup assembly [2] down over the
stilt bolt [1].
d) Assemble the stilt bolt/bottom spring up through
hole in the bottom plate and hold in place.
e) Assemble top spring/cup assembly [3] down over
stilt bolt.
f) Assemble flat washer [5], lock washer [6] and
nuts [4] on the stilt bolt.
g) Tighten down top nuts, compressing the top
spring approximately 13 mm (0.5 in.). Additional
compression may be required to stabilize the
baseplate.
h) After all four stilts have been assembled, position
the baseplate in place, over the floor cups [7]
under each stilt location, and lower the baseplate
down to the floor.
i) Level and make final height adjustments to the
suction and discharge pipe by first loosening the
top nuts, and turning the bottom nuts to raise or
lower the baseplate.
j) Recompress the top spring to the compression
established in step g) and lock the nuts.
Page 15 of 52 flowserve.com
USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
t
k) It should be noted that the connecting pipelines
must be individually supported, and that the
spring mounted baseplate is not intended to
support total static pipe loads.
Figure 4-4
1 in. (25 mm) approx. i nitial heigh
1 . Sti l t bo l t
2. Bott om spring [ 3¼ in.
(83 mm ) O/D x 4 in.
(102 mm) floor cups]
3. Top spring [2 in.
(51 m m) O/D x 4 in.
(102 mm) floor cups]
4. Nuts
5. Flat washer
6. Loc k was her
7. Floor cup
4.3.3.3 Stilt/spring mounted baseplates - motor
alignment
The procedure for motor alignment on stilt or spring
mounted baseplates is similar to grouted baseplates.
The difference is primarily in the way the baseplate is
levelled.
a) Level the baseplate by using the stilt adjusters.
(Shims are not needed as with grouted baseplates.)
b) After the base is level, it is locked in place by
locking the stilt adjusters.
c) Next the initial pump alignment must be checked.
The vertical height adjustment provided by the
stilts allows the possibility of slightly twisting the
baseplate. If there has been no transit damage
or twisting of the baseplate during stilt height
adjustment, the pump and driver should be within
0.38 mm (0.015 in.) parallel, and 0.0025 mm/mm
(0.0025 in./in.) angular alignment. If this is not
the case, check to see if the driver mounting
fasteners are centered in the driver feet holes.
d) If the fasteners are not centered there was likely
shipping damage. Re-center the fasteners and
perform a preliminary alignment to the above
tolerances by shimming under the motor for
vertical alignment, and by moving the pump for
horizontal alignment.
e) If the fasteners are centered, then the baseplate
may be twisted. Slightly adjust (one turn of the
adjusting nut) the stilts at the driver end of the
baseplate and check for alignment to the above
tolerances. Repeat as necessary while
maintaining a level condition as measured from
the pump discharge flange.
f) Lock the stilt adjusters.
The remaining steps are as listed for new grouted
baseplates.
4.4 Grouting
a) The pump foundation should be located as close to
the source of the fluid to be pumped as practical.
b) There should be adequate space for workers to
install, operate, and maintain the pump. The
foundation should be sufficient to absorb any
vibration and should provide a rigid support for
the pump and motor.
c) Recommended mass of a concrete foundation
should be three times that of the pump, motor
and base. Refer to Figure 4-5.
Foundation bolts are imbedded in the
concrete inside a sleeve to allow some
movement of the bolt.
Figure 4-5
d) Level the pump baseplate assembly. If the
baseplate has machined coplanar mounti ng
surfaces, these machined surfaces are to be
referenced when leveling the baseplate. This may
require that the pump and motor b e remove d from
the baseplate in order to reference the machined
faces. If the baseplate is without machined
coplanar mounting surfaces, the pump and motor
are to be left on the baseplate. The p roper surfa ces
to reference when leveling the pump baseplate
assembly are the pump suction and discharge
flanges. DO NOT stress the baseplate.
e) Do not bolt the suction or discharge flanges of the
pump to the piping until the ba seplate f oundati on is
completely installed. If equipped, use leveling
jackscrews to level the baseplate. If jackscrews are
not provided, shims and wedges should be used.
(See Figure 4-5.) Check for levelne ss in both the
longitudinal and lateral directions. Shims should be
placed at all base anchor bolt locations, and in the
middle edge of the base if the base i s more than
1.5 m (5 ft.) long. Do not rely on th e bottom of t he
baseplate to be flat. Standard baseplate bottoms
are not machined, and it is not likely that the field
mounting surface is flat.
Page 16 of 52 flowserve.com
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