USER INSTRUCTIONS
FP centrifugal pump
Multi-stage, single suction and radial joint plan pump type
centrifugal pump
PCN=71576286 – 07/06 (E)
Installation
Operation
Maintenance
CONTENTS
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
PAGE
PAGE
1 INTRODUCTION AND SAFETY ...........................4
1.1 General...........................................................4
1.2 CE marking and approvals.............................4
1.3 Disclaimer.......................................................4
1.4 Copyright........................................................4
1.5 Duty conditions...............................................4
1.6 Safety.............................................................5
1.7 Safety labels summary...................................8
1.8 Specificmachine performance .......................8
1.9 Noise level......................................................9
2 TRANSPORT AND STORAGE...........................10
2.1 Consignment receipt and unpacking............10
2.2 Handling.......................................................10
2.3 Lifting............................................................11
2.4 Storage.........................................................11
2.5 Recycling and end of product life.................11
3 PUMP DESCRIPTION.........................................11
3.1 Configurations..............................................11
3.2 Nomenclature...............................................12
4 INSTALLATION....................................................13
4.1 Location........................................................13
4.2 Foundation ...................................................13
4.3 Grouting........................................................14
4.4 Initialalignment ............................................14
4.5 Piping ...........................................................15
4.6 Electrical connections...................................16
4.7 Final shaft alignment check..........................17
4.8 Protection systems.......................................17
6 MAINTENANCE...................................................21
6.1 General.........................................................21
6.2 Maintenance schedule .................................22
6.3 Spare parts ...................................................24
6.4 Recommended spares and consumable..........
items ...................................................................25
6.5 Disassembly.................................................25
7 FAULTS; CAUSESAND REMEDIES ..................26
8 PARTS LIST AND DRAWINGS ...........................27
8.1 Sectional drawings .......................................27
8.2 Sectional drawings part list...........................32
8.3 General arrangement drawing......................34
9 CERTIFICATION .................................................34
10 OTHER RELEVANT DOCUMENTATION AND
MANUALS...............................................................34
10.1 Supplementary User Instructions ...............34
10.2 Change notes.............................................34
10.3 Additional sources of information ...............34
5 COMMISSIONING, START-UP, OPERATION AND
SHUTDOWN...........................................................17
5.1 Direction of rotation......................................17
5.2 Guarding.......................................................17
5.3 Priming and auxiliary supplies......................18
5.4 Starting the pump.........................................18
5.5 Running the pump........................................19
5.6 Stopping andshutdown................................20
5.7 Hydraulic, mechanical and electrical duty....21
5.8 Pumps for Food Use or Potable Water........21
Page 2 of 35
INDEX
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
PAGE
PAGE
Additional sources (10.3).......................................34
Alignment of shafting (see 4.2, 4.4 and 4.7)
ATEX marking (1.6.4.2)...........................................7
CE marking and approvals (1.2)..............................4
Certification (9) ......................................................34
Change notes (10.2)..............................................34
Cleaning prior to operation (5.8.1) ........................21
Commissioning, start-up, operation (5) .................17
Compliance, ATEX (1.6.4.1)....................................6
Configurations (3.1)...............................................11
Copyright (1.4).........................................................4
Direction of rotation (5.1).......................................17
Disassembly (6.5)..................................................25
Discharge piping (4.5.3) .......................................16
Disclaimer (1.3)........................................................4
Dismantling (see 6.5, Disassembly)......................25
Drawings (8.1).......................................................27
Duty conditions (1.5)................................................4
Electrical connections (4.6) ...................................16
End of product life (2.5).........................................11
Faults; causes and remedies (7)...........................26
Final checks (4.5.4) ..............................................16
First pump start up (5.4.2) ....................................18
Foundation (4.2)....................................................13
Forces and moments (see 4.5.1)...........................15
General arrangement drawing (8.3) ......................34
Gland packing (6.2.5)............................................23
Grouting (4.3).........................................................14
Guarding (5.2)........................................................17
Handling (2.2)........................................................10
Hydraulic, mechanical and electrical duty (5.7) .....21
Inspection (6.2.2 and 6.2.3)...................................23
Installation (4)........................................................13
Internal coating (6.2.6)...........................................24
Lifting (2.3).............................................................11
Location (4.1).........................................................13
Maintenance (6).....................................................21
Maintenance schedule (6.2) ..................................22
Mechanical seal (6.2.4) .........................................23
Nomenclature (3.2)................................................12
Nameplate (1.7.1)....................................................8
Operating limits (see 3.1) ......................................12
Ordering spare parts (6.3.1)..................................24
Parts lists (8.2).......................................................32
Piping (4.5) ............................................................15
Protection systems (4.8)........................................17
Pump masses (2.2.2) ............................................10
Receipt and unpacking (2.1)..................................10
Recommended fill quantities (see 6.2.1)...............23
Recommended grease lubricants (see 6.2.1) ....... 23
Recommended spares (6.4)..................................25
Recycling (2.5).......................................................11
Replacement parts (see 6.3 and 6.4) ....................24
Running the pump (5.5).........................................19
Safety action (1.6.3).................................................5
Safety markings (1.6.1)............................................5
Safety, protection systems (see 1.6 and 4.8)
Sectional drawings (8.1) ........................................27
Sound level (see 1.9, Noise level) ...........................9
Sources, additional information (10.3)...................34
Spare parts (6.3)....................................................24
Specific machine performance (1.8)........................8
Standard maintenance (6.2.1) ..............................22
Starting the pump (5.4)..........................................18
Stop/start frequency (5.5.6) ...................................20
Stopping and shutdown (5.6).................................20
Storage, pump (2.4)...............................................11
Storage, spare parts (6.3.2)...................................25
Suction piping (4.5.2) ............................................16
Supplementary manuals or information sources...34
Thermal expansion (4.4.1) ....................................14
Transport and storage (2) .....................................10
Trouble-shooting (see 7)........................................26
Vibration (5.5.5).....................................................20
Warning labels (1.7.2)..............................................8
Page 3 of 35
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
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,
utilizing 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.
1.2 CE marking and approvals
It is a legal requirement that machinery and
equipment put into service withincertain regions of
the world shall conform with the applicable CE
Marking Directives covering Machinery and, where
applicable, Low Voltage Equipment, Electromagnetic
Compatibility (EMC), Pressure Equipment Directive
(PED) and Equipment for Potentially Explosive
Atmospheres (ATEX).
To confirmtheApprovalsapplying and iftheproduct is
CE marked,check theserialnumberplate markings
andtheCertification.(Seesection9,Certification.)
1.3 Disclaimer
Informationinthese UserInstructions is believed
to be reliable. In spite of all the effortsof Flowserve
PumpDivision to providesound andall necessary
informationthe content of thismanualmayappear
insufficient and is not guaranteedby Flowserve as
to itscompleteness or accuracy.
Flowserve manufacturesproducts to exacting
International QualityManagement System Standards
ascertified and auditedbyexternal QualityAssurance
organizations.Genuineparts andaccessorieshave
beendesigned,tested andincorporated intothe
products to help ensure their continuedproduct quality
andperformanceinuse. As Flowserve cannot test
parts and accessoriessourcedfrom other vendors the
incorrect incorporationof such parts and accessories
mayadversely affectthe performance andsafety
featuresof the products.The failuretoproperlyselect,
installoruseauthorized Flowserveparts and
accessoriesisconsideredtobemisuse.Damageor
failurecausedbymisuseisnotcovered by the
Flowserve warranty. In addition, anymodification of
Flowserve productsorremovaloforiginal components
mayimpairthesafetyof theseproducts in their use.
1.4 Copyright
All rights reserved. No part of these instructions may
be reproduced, stored in a retrieval system or
transmitted in any form or by any means without
prior permission of Flowserve Pump Division.
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.Acopy 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.
Whereapplicable the Directives andanyadditional
Approvals coverimportantsafetyaspects relating to
machinery and equipment and thesatisfactory
provision of technicaldocumentsandsafety
instructions.Whereapplicablethisdocument
incorporatesinformation relevanttothese Directives
andApprovals.
If the conditions of service on your purchase order
are going to be changed (for example liquid
pumped, temperature or duty) it is requested that the
user seeks the written agreement of Flowserve
before start up.
Page 4 of 35
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
1.6 Safety
1.6.1 Summary of safety markings
These UserInstructions containspecific safety
markingswherenon-observanceof an instruction
would causehazards.Thespecific safetymarkings
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 affect personal safety and
could result in loss of life.
This symbol indicates “hazardous substances
and toxic fluid” safety instructions where noncompliance would affect personalsafetyand could
result in loss of life.
This symbol indicates safety
instructions where non-compliance will involve some
risk to safe operation and personal safety and would
damage 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 explosion.
This symbol is used in safety instructions to
remind not to rub non-metallic surfaces with a dry
cloth; ensure cloth is damp. It is used where non-
compliance in the hazardous area would cause the
risk of an explosion.
Thissign is notasafetysymbol butindicates
an important instruction intheassemblyprocess.
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 involved. If the
personnel in question do not already possess the
necessary knowledge and skill, appropriatetraining
and instruction must be provided. If required the
operator may commission the manufacturer/supplier
to 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.
1.6.3 Safety action
This is a summary of conditions and actions to
prevent injury to personnel and damage to the
environment and to equipment. For products
used in potentially explosive atmospheres
section 1.6.4 also applies.
NEVER DO MAINTENANCE WORK
WHEN THE UNIT IS CONNECTED TO POWER
GUARDS MUST NOT BE REMOVED WHILE
THE PUMP IS OPERATIONAL
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.
THERMAL SHOCK
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.
NEVER APPLYHEAT TO REMOVE
IMPELLER
Trapped lubricantor vapour could cause an
explosion.
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 °C (175 °F)
or below 5 °C (20 °F) in a restricted zone, or
exceeds local regulations, action as above shall
be taken.
Page 5 of 35
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
HAZARDOUS LIQUIDS
Whenthe pumpishandling hazardousliquids care
mustbetakentoavoidexposure to the liquid by
appropriatesittingof the pump,limiting personnel
access andbyoperator training.If the liquid is
flammable and/or explosive, strict safetyprocedures
mustbeapplied.
Gland packing must not be used when pumping
hazardous liquids.
PREVENT EXCESSIVE EXTERNAL
PIPE LOAD
Do not use pump as a support for piping. Do not
mount expansion joints, unless allowed by
Flowserve in writing, so that their force, due to
internal pressure, acts on the pump flange.
ENSURE CORRECT LUBRICATION
(See section 5, Commissioning, startup, operation
and shutdown.)
START THE PUMP WITH OUTLET
VALVE PART OPENED
(Unless otherwise instructed at a specific point in the
User Instructions.)
This is recommended to minimize the risk of
overloading and damaging the pump motor at full or
zero flow. Pumps may be started with the valve
further open only on installations where this situation
cannot occur. Pump outlet valve shall may need to
be adjusted to comply with the duty following the
run-up process. (See section 5, Commissioning
start-up, operation and shutdown.)
NEVER RUN THE PUMP DRY
1.6.4 Products used in potentially explosive
atmospheres
Measures are required to:
Avoid excess temperature.
Prevent build up of explosive mixtures.
Prevent the generation of sparks.
Prevent leakages.
Maintain the pump to avoid hazard.
Thefollowing instructions for pumpsand pumpunits
wheninstalledinpotentiallyexplosiveatmospheres
mustbefollowed to helpensureexplosionprotection.
Bothelectricaland non-electricalequipmentmustmeet
therequirements of EuropeanDirective 94/9/EC.
1.6.4.1 Scope of compliance
Useequipment onlyinthe zoneforwhichitis
appropriate.Alwayscheckthat the driver, drive
couplingassembly, seal and pumpequipment are
suitablyratedand/orcertifiedfor the classification of
thespecific atmosphere in whichthey aretobe
installed.
Where Flowservehassuppliedonlythe bare shaft
pump, the Ex rating applies only to the pump. The
partyresponsible for assemblingthepump set shall
selectthe coupling,driverand any additional
equipment, with the necessary CE Declaration of
Conformity establishing it is suitable for the area in
which it is to be installed.
Theoutputfrom a variablefrequency drive(VFD)can
causeadditionalheatingaffects in themotor and so,for
pumps setswith a VFD,theATEX Certificationfor the
motor muststate thatitis covers the situation where
electrical supply isfrom the VFD.This particular
requirementstill applieseven if the VFDis in a safe
area.
INLET VALVES TO BE FULLY OPEN
WHEN PUMP IS RUNNING
Runningthe pump at zero flow or below the
recommended minimum flow continuouslywillcause
damage to the seal.
DO NOT RUN THE PUMP AT
ABNORMALLYHIGH OR LOW FLOW RATES
Operating at a flow rate higher than normal or at a
flow rate with no backpressure on the pump may
overload the motor and cause cavitations. Low flow
rates may cause a reduction in pump/bearing life,
overheating of the pump, instability and
cavitations/vibration.
Page 6 of 35
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
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 = normallevelof protection
Gas and/or Dust
G = Gas; D= Dust
c = Constructionalsafety
(in accordance with prEn13463-5)
Gas Group (EquipmentCategory2 only)
IIA–Propane (typical)
IIB–Ethylene (typical)
IIC – Hydrogen (typical)
Maximum surfacetemperature (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
Pumps have a temperature class as stated in the
ATEX Ex rating on the nameplate. These are based
on a maximum ambient of 40 °C (104 °F); refer to
Flowserve for higher ambient temperatures.
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 the pump could be
installed in different hazardous atmospheres. In this
case the user is responsible for ensuring that the
pump surface temperature does not exceed that
permitted in the particular hazardous atmosphere.
If an explosive atmosphere exists during the
installation, do not attempt to check the direction of
rotation by starting the pump unfilled. Even a short
run time may give a high temperature resulting from
contact between rotating and stationary
components. Furthermore, confinement of liquid in
the pump and pipes must be avoided (valve closed).
If the liquid heats up this may cause excessive
pressure and lead to bursting of pump components.
Where there is any risk of the pump being run against
a closed valve generating high liquid and casing
externalsurface temperaturesit is recommended that
users fit an external surface temperature protection
device.
Avoid mechanical, hydraulic or electrical overload by
using motor overload trips, temperature monitor or a
power monitor and make routine vibration monitoring
checks.
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
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 that follows.
The temperature rise at the seals, bearings and due
to the minimum permitted flow rate is taken into
account in the temperatures stated.
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) *
Temperature
class to
prEN 13463-1
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)
Page 7 of 35
ENSURE PUMP IS PROPERLY FILLED AND
VENTED AND DOES NOT RUN DRY.
Ensure 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 (eg liquid
detection or power monitor).
To avoid potential hazards from fugitive emissions of
vapour or gas to atmosphere the surrounding area
must be well ventilated.
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
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 ground contact on the
baseplate must be used.
Avoid electrostatic charge: do not rub non-
metallic surfaces with a dry cloth, ensure cloth is
damp.
The coupling must be selected to comply with
94/9/EC and correct alignment must be maintained.
Additional requirements 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.
It is recommended that a maintenance plan and
schedule is adopted. (See section 6, Maintenance.)
1.7 Safety labels summary
1.7.1 Nameplate
For details of nameplate, see the Declaration of
Conformity, or separate documentation included with
these User Instructions.
1.7.2 Warning labels
Avoid entrapment of liquid in the pumpand associated
piping duetoclosingof suction anddischarge valves,
which couldcause dangerous excessive pressures to
occur if there is heat input to theliquid.This canoccur
ifthepump 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 loss of a
seal barrier fluid or external flush, the fluid must be
monitored.
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 to avoid the hazard
CORRECT MAINTENANCE IS REQUIRED
TO AVOID POTENTIAL HAZARDS WHICH GIVE A
RISK OF EXPLOSION
Theresponsibilityforcompliancewith
maintenance instructions is withtheplant
operator.
Oil lubricated units only:
1.8 Specific machine performance
For performance parameters see section 1.5, Duty
conditions. When the contract requirement specifies
these to be incorporated into User Instructions these
are included here. Where performance data has
been supplied separately to the purchaser these
should be obtained and retained with these User
Instructions if required.
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.
Page 8 of 35
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
1.9 Noise level
When pump noise level exceeds 85dBAattention
must be given to prevailing Health and Safety
Legislation, to limit the exposure of plant operating
personnel to the noise.The usual approach is to
control 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 machines above a
certain power level will exceed 85 dB(A). In such
situations consideration must be given to the fitting
of an acoustic enclosure to meetlocal regulations.
Pump noise level is dependent on a number of
factors- the type of motor fitted, the operating
capacity, pipework design and acoustic
characteristics of the building. Typical sound
pressure levels measured in dB and A-weighted are
shown in the table below.
The figures are indicative only, they are subject to a
+3 dB tolerance, and cannot be guaranteed.
The values are based on the noisiest ungeared
electric motors which are likely to be encountered.
They are LpAsound pressure levels at 1m (3.3ft)
from the directly driven pump, for "free field over a
reflecting plane". For estimating LwAsound power
level (re 1 pW) add 14 dB(A) to the sound pressure
value.
If a pump only has been purchased, for fitting with
your own driver, then the "pump only" noise levels
from the table should be combined with the level for
the driver obtained from the supplier. If the motor is
driven by an inverter, it may show an increase in
noise level at some speeds. Consult a Noise
Specialist for this calculation
For units driven by equipment other than
electric motors or units contained within enclosures,
see the accompanying information sheets and
manuals.
Typicalsound pressurelevel,dBA, LpAat 1 m reference 20 μPa(LwAsound power1 pW whereLpA>85 dBA)
and speed
kW (hp)
<0.55 (<0.75)
0.75 (1) 74 66 67 62 67 62 63 62
1.1 (1.5) 74 68 67 64 67 64 65 64
1.5 (2) 77 70 70 66 70 66 66 66
2.2 (3)
3 (4) 81 74 74 70 74 70 70 70
4 (5) 82 75 75 71 75 71 71 71
5.5 (7.5) 90 (99) 77 83 73 76 73 72 71
7.5 (10)
11(15) 91 (100) 80 84 76 78 76 74 73
15 (20) 92 (101) 83 85 (94) 79 80 79 76 75
18.5 (25) 92 (101) 83 85 (94) 79 80 79 76 75
22 (30)
30 (40) 100 (109) 85 (94) 93 (102) 81 84 80 80 76
37 (50) 100 (109) 86 (95) 93 (102) 82 84 80 80 76
45 (60) 100 (109) 87 (96) 93 (102) 83 84 80 80 76
55 (75)
75 (100) 100 (109) 90 (99) 95 (104) 86 (95) 88 (97) 81 83 78
90 (120) 100 (109) 90 (99) 95 (104) 86 (95) 90 (99) 81 85 (94) 78
110(150) 100 (109) 91 (100) 95 (104) 87 (96) 91 (100) 83 86 (95) 79
150 (200)
3550 r/min 2900 r/min 1750 r/min 1450 r/minMotor size
Pump and
motor
dBA
71 66 64 62 64 62 63 62
78 72 71 68 71 68 68 68
90 (99) 78 83 74 77 74 73 72
92 (101) 83 85 (94) 79 81 79 77 75
100 (109) 88 (97) 95 (104) 84 86 (95) 81 82 77
101 (110) 92 (101) 96 (105) 88 (97) 91 (100) 83 86 (95) 79
Pump
only
dBA
Pump and
motor
dBA
Pump
only
dBA
Pump and
motor
dBA
Pump
only
dBA
Pump and
motor
dBA
Pump
only
dBA
Page 9 of 35
FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
In areas where the staff has to intervene, remember
that when the level of the sound pressure is:
Below 70 dBA :It is not necessary to take
special precautions.
Above 70 dBA :People working continuously in
the machine room must be
supplied with protective devices
against noise.
Below 85 dBA :No particular measures need to
be taken for casual visitors
staying in the room during a
limited period.
Above 85 dBA :The room must be considered as a
dangerous area because of the
noise and a warning sign must be
fixed at each entry warning the
people coming into the room, even
for a short period, that they must
wear hearing protection.
Above 105 dBA:Special hearing protection adapted
to this noise level and to the
spectral noise components must
be installed and a warning sign to
this effect erected at each entry.
The staff in the room must wear
ear protection.
Make sure that the noise, which travels through the
walls and windows, does not generate too high
noise levels in the machine room's surroundings.
2 TRANSPORT AND STORAGE
2.1 Consignment receipt and unpacking
Immediately after receipt of the equipment it must be
checked against the delivery and 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 Pump Division and
received in writing within one month of receipt of the
equipment. Later claims cannot be accepted.
Check any crate, boxes and wrappings for any
accessories or spare parts that may be packed
separately with the equipment or attached to
sidewalls 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
2.2.1 General instructions concerning handling
Boxes, crates, pallets or cartons may be unloaded
using forklift vehicles or slings dependent on their
size and construction. See 2.3.1 for positioning of
slings.
To lift heavy pieces above 25 kg (55 lb), use a winch
adapted to the mass and in accordance with the
current local regulations.
To lift machines or pieces with one or several
suspension rings, only use hooks and chains in
compliance with the local regulations concerning
safety. Never put cables, chains or ropes directly on
or in the suspension rings. Cables, chains or lifting
ropes must never present excessive bending.
Never bend the lifting hooks, suspension rings,
chains, etc., which should only be made to endure
stresses within, calculated limits. Remember that the
capacity of a lifting device decreases when the
direction of the lifting force direction makes an angle
with the device axis.
To increase the safety and the efficiency of the lifting
device, all the lifting elements must be as
perpendicular as possible. If necessary a lifting
beam can be placed between the winch and the
load.
When heavy pieces are lifted up, never stay or work
under the load or in the area, which could be in the
path of the load if it were to swing or fall away.
Never leave a load hanging from a winch. The
acceleration or the slowing-down of lifting equipment
must stay in the safety limits for the staff. A winch
must be positioned in such a way that the load will
be raised perpendicularly. Where possible
necessary precautions must be taken to avoid the
swing of the load, using for example two winches
making approximately the same angle, below 30°,
with the vertical.
2.2.2 Pump masses
All masses are in kg:
Mass of
bareshaft
pump
1 stage 37 54 78 80 204 205 530 600
2 stages 37 54 92 94 243 240 605 720
3 stages 42 61 106 108 282 275 680 840
4 stages 47 68 120 122 321 310 755 960
5 stages 52 75 134 136 360 345
6 stages 57 82 148
50FP65FP80FP100FP122FP125FP152FP202
FP
7 stages 62 89
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FP USER INSTRUCTIONS ENGLISH 71576286 - 07/06
All motors (for masses see the motor
description plate) must be handled with a winch.
For masses above 25 kg (55lb), manual
handling is forbidden.
2.3 Lifting
2.3.1 Slinging of motor pumps units
Use handling means in accordance with motor
pump unit mass mentioned on the CE plate. For the
masses of the pumps bare end of shaft see table §
2.2.2 and nameplate.
To avoid distortion, the pump unit
should be lifted as shown.
Motor pump unit
2.4 Storage
Store the pump in a clean, dry
location away from vibration. Leave piping
connection covers in place to keep dirt and other
foreign material out of pump casing. Turn pump at
intervals to prevent brinelling of the bearings and the
seal faces, if fitted, from sticking.
Do not store pumps starting on the fan guard.
The pump may be stored as above for up to 6
months. Consult Flowserve for preservative actions
when a longer storage period is needed.
2.5 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 regulations. If the
product contains substances which 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 in the
"seal system" or other utilities.
Bareshaft pump
When handling always wear gloves, safety
boots and an industrial safety helmet.
Make sure that hazardous substances or toxic
fluid 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.
3 PUMP DESCRIPTION
3.1 Configurations
The multi-stagecentrifugal pump is designed for the
pumping of cold water or all clear liquids which are
not solid and liquid mixtures, non-corrosive, nonabrasive or non-explosive when in contact with the
pump motor unit and its working parts (Important: for
other liquids consult FLOWSERVE for beforehand
advice).
The FP type pump is a centrifugal, multi-stage,
single suction and radial joint plan pump.
The modular design (2 hydraulics by pump type,
number of stages variation) enables an accurate
pump adjustment to the required operating
conditions.
It can be driven by electric motor, steam turbine, or
petrol or diesel motor.
For masses above 25 kg (55lb), manual
handling is forbidden.
The pump must be stored in a non-explosive,
ventilated location, sheltered from bad weather, dust
and vibrations.
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