8 PARTS LIST AND DRAWINGS...........................27
8.1 Sectional Arrangement and Parts List
Drawings – MODEL 20 .................................. 27
8.2 Sectional Arrangement and Parts List
Drawings – MODEL 30 .................................. 29
8.3 Sectional Arrangement and Parts List
Drawings – MODEL 40 .................................. 31
8.4 Sectional Arrangement and Parts List
Drawings – MODEL 60 .................................. 31
8.5 Sectional Arrangement and Parts List
Drawings – MODEL 80 .................................. 35
8.6 Mechanical Seal Sectional Arrangement and
Parts List Drawing –
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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’s 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 your 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/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 within certain 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).
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 Approvals.
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
To confirm the Approvals applying and if the product is
CE marked, check the serial number plate markings
and the Certification. (See section 9, Certification.)
1.3 Disclaimer
Information in these User Instructions is believed
to be reliable. In spite of all the efforts of
Flowserve 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 organizations. Genuine parts and
accessories have been designed, tested, and
incorporated into the products to help ensure
continued product quality and performance in use.
As Flowserve cannot test parts and accessories
sourced from other vendors, 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 authorized Flowserve parts and accessories is
considered to be misuse. Damage or failure caused
by misuse is not covered by Flowserve’s 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 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 purchase 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 example liquid pumped,
temperature, or duty), it is requested that the user seeks
Flowserve’s written agreement before start-up.
Page 4 of 41
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
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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 affect personal safety and
could result in loss of life.
This symbol indicates “hazardous and toxic fluid”
safety instructions where non-compliance would affect
personal safety and 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 sign is not a safety symbol but indicates
an important instruction in the assembly process.
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, appropriate training
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
help 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
(Lock out.)
DRAIN THE PUMP AND ISOLATE PIPING
BEFORE DISMANTLING THE PUMP
The appropriate safety precautions should be taken
where the pumped liquids are hazardous.
FLUOROELASTOMERS (When fitted.)
When a pump has experienced temperatures over
250 °C (482 °F), 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
GUARDS MUST NOT BE REMOVED WHILE
THE PUMP IS OPERATIONAL
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 APPLY HEAT TO REMOVE IMPELLER
Trapped lubricant or vapor could cause an explosion.
HOT (and cold) PARTS
If hot or freezing components or auxiliary heating
equipment can present a danger to operators and
persons entering the immediate area, action must be
taken to avoid accidental contact (such as shielding).
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),
below 5 °C (20 °F) in a restricted zone, or exceeds
local regulations, action as above shall be taken.
Page 5 of 41
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HAZARDOUS LIQUIDS
When the pump is handling hazardous liquids, care
must be taken to avoid exposure to the liquid by
appropriate pump placement, limiting personnel
access, and by operator training. If the liquid is
flammable and/or explosive, strict safety procedures
must be applied.
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 6.2, Lubrication Data.)
NEVER EXCEED THE MAXIMUM
DESIGN PRESSURE (MDP) AT THE
TEMPERATURE SHOWN ON THE PUMP
NAMEPLATE
(See section 3.3, Performance and operating limits,
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.)
NEVER RUN THE PUMP DRY OR
WITHOUT PROPER PRIME (Casing flooded)
NEVER OPERATE THE PUMP WITH
THE SUCTION VALVE CLOSED
It should be fully opened when the pump is running.
NEVER OPERATE THE PUMP AT
ZERO FLOW OR FOR EXTENDED PERIODS
BELOW THE MINIMUM CONTINUOUS FLOW
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 spacer
and starting the pump. Incorrect rotation of the pump
for even a short period can unscrew the impeller,
which can cause significant damage.
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
1.6.4 Products used in potentially explosive
atmospheres
Always check that the driver, drive coupling assembly
and pump equipment are suitably rated and/or
certified for the classification of the specific
atmosphere in which they are installed.
See section 9, Certification.
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
The following instructions for pumps and pump units
when installed in potentially explosive atmospheres
must be followed to help ensure explosion protection.
Both electrical and non-electrical equipment must meet
the requirements of European Directive 94/9/EC.
1.6.4.1 Scope of compliance
Use equipment only in the zone for which it is
appropriate. Always check that the driver, drive
coupling assembly, seal and pump equipment are
suitably rated and/or certified for the classification of
the specific atmosphere in which they are to be
installed.
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, seal and any additional
equipment, with the necessary CE Certificate/
Declaration of Conformity establishing it is suitable
for the area in which it is to be installed.
The output from a variable frequency drive (VFD) can
cause additional heating effects in the motor. On
pump installations controlled by a VFD, the ATEX
Certification for the motor must state that it covers the
situation where electrical supply is from the VFD.
This particular requirement still applies even if the
VFD is in a safe area.
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Temperature
Temperature
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 temperature of 40 °C (104 °F); refe r
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.
Maximum permitted liquid temperature for pumps
class to
EN 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)
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)*
Maximum permitted liquid temperature for pumps
with self priming casing
class to
EN 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)
Temperature limit of liquid
handled (* depending on
material and construction
variant – check which is lower)
Consult Flowserve
Consult Flowserve
110 °C (230 °F)*
175 °C (347 °F)*
270 °C (518 °F)*
350 °C (662 °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 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.
Do not attempt to check the direction of rotation with the
coupling element/pins fitted due to the risk of severe
contact between rotating and stationary components.
Where there is any risk of the pump being run against a
closed valve generating high liquid and casing external
surface temperature, it 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 perform routine vibration monitoring.
In dirty or dusty environments, regular checks must
be made and dirt removed from areas around close
clearances, bearing housings, and motors.
Additional requirements for self-priming
casing pumps
Where the system operation does not ensure control of
priming, as defined in the User Instructions, and the
maximum permitted surface temperature of the T Class
could be exceeded, it is recommended that user install
an external surface temperature protection device.
1.6.4.4 Preventing the build up of explosive
mixtures
ENSURE PUMP IS PROPERLY FILLED AND
VENTED AND DOES NOT RUN DRY
Ensure that the pump and relevant suction and discharge
piping is totally filled with liquid at all times during the
pumps operation so that an explosive atmosphere is
prevented.
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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 can not avoid this
condition it is recommended that you fit an
appropriate dry run protection device (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.
1.6.4.5 Preventing sparks
To prevent a potential hazard from mechanical
contact, the coupling guard must be non-sparking for
Category 2.
To avoid the potential hazard from random induced
current generating a spark, the baseplate must be
properly grounded.
Avoid electrostatic charge. Do not rub non-metallic
surfaces with a dry cloth; ensure the cloth is damp.
The coupling must be selected to comply with
94/9/EC and correct alignment must be maintained.
Additional requirements for 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
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 with maintenance
instructions 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.)
Pumps with mechanical seal. 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 and associated
piping due to closing of suction and discharge valves,
which could cause dangerous excessive pressures to
occur if there is heat input to the liquid. This can 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 auxiliary 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.
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1.7 Safety Labels
1.7.1 Nameplates
For details of nameplate, see the Declaration of
Conformity and section 3.
1.7.2 Warning labels & tags
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1.8 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, piping 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 assumed in the “pump and
motor” noise is that typically expected from standard
and high efficiency motors when on load directly 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 Flowserve 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 LpA at 1 m
(3.3 ft) from the machine, for “free field conditions
over a reflecting plane”.
For estimating sound power level LWA (re 1pW) then
add 14 dBA to the sound pressure value.
Typical sound pressure level, dBA, LpA at 1 m (3.28 ft) reference 20 µPa (2.9x10-9 psi)
(1) Motors in this range are generally job specific and noise levels should be calculated based on actual equipment installed.
For 960 r/min reduce 1450 r/min values by 5 dBA.
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
Pump Division and must be received in writing within
ten 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 forklift 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.
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 gravity to prevent
the unit from flipping. This is especially true with
belt driven units with the motor mounted above the
pump.
2.3.1 Lifting pump components
2.3.1.1 Casing [1100]
Use either a sling or hook through each of the two
lifting lugs located on the side of the casing.
2.3.1.2 Bearing Housing [3200]
Insert an eye hook in the drilled and tapped hole at
the top of the bearing housing. Use either a sling or
hook through the eyebolt.
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
2.3.1.3 Power end
Same as bearing housing.
2.3.1.4 Bare pump
Use either a sling or hook through each of the two
lifting lugs located on the side of the casing and
around the outboard end of the 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 bearing housing is
toward the coupling end of the pump shaft. The sling
lengths should be adjusted to balance the load before
attaching the lifting hook.
2.3.2 Lifting pump, motor and baseplate
assembly
To lift the pump, driver, and baseplate as a unit, the
following procedure must be followed.
V-belt guards should be removed if fitted.
• If the baseplate has lifting holes cut in the sides
at the end, insert lifting S hooks at the four
corners and use slings or chains to connect to a
lifting eye. Do not use slings through the lifting
holes.
• For other baseplates, sling around pump
discharge nozzle, when equipped, and the
outboard end of the motor frame using choker
hitches pulled tight.
• When pump is not equipped with optional
discharge nozzle, use user supplied eyebolt
screwed and seated into discharge of pump.
Insert lifting S hook in eyebolt and use sling.
2.4 Storage
Store the pump in a clean, dry
location away from vibration. Leave flange covers in
place to keep dirt and other foreign material out of
pump casing. Turn the pump shaft at regular
intervals to prevent brinelling of the bearings and the
seal faces, if fitted, from sticking.
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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 Storage – General
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.
Bearing housings are not filled with oil
prior to shipment
•The internal surfaces of ferrous casings, covers,
seal chamber, flange faces, and the impeller
surface are sprayed with Cortec VCI-389, or
equal
• Exposed shafts are taped with Polywrap
• Flange covers are secured to both the suction
and discharge flanges or face.
•In some cases with assemblies ordered with
external piping, components may be
disassembled for shipment
•The pump must be stored in a covered, dry
location
2.4.2 Storage – Long Term
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.
Warranty for the pumps will normally be for
12 months. Extension of this period can only be
achieved with the prior agreement of Flowserve
and would necessitate inspection prior to putting
the pump into service.
After unpacking, protection will be the responsibility of
the user. Addition of oil to the bearing housing will
remove the inhibitor. If units are to be idle for extended
periods after addition of lubricants, inhibitor oils should
be used. Every three months, the pump shaft should
be rotated approximately 10 revolutions.
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 in accordance with local regulations. If the
product contains substances that are harmful to the
environment, these should be removed and disposed
of in accordance with current local 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 local regulations at all times.
3 DESCRIPTION
3.1 General
The Flowserve MPT single stage pump has a back
pull-out rotating assembly with suction and
discharge facings on the fixed casing to allow
removal of the rotating element without breaking the
pipe joints or moving the driver. Mounting feet are
rigidly connected to the casing so piping strains
allowed in section 2.3, Flange Loads, are readily
transmitted to the foundation.
No special tools are required for dismantling and
maintenance.
An example of the nameplate used on the MPT
pump, which is always mounted on the casing, is
shown below.
Serial No.
Equipment No.
Purchase
Order
Model
Size
MDP
Material
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3.2 Design of major parts
3.2.1 Pump casing
The volute type casing with integral priming
chamber is of rugged heavy duty construction for
minimum wear under the toughest operating
conditions. Removal of the casing is not required
when performing maintenance of the rotating element.
The pump is designed with radial o-ring seals allowing
the rotating element and cover plate to be easily
removed (back pull out).
3.2.2 Valve flap
The pump suction opening is fitted with a non-return
flap valve. The flap is a solid one-piece design and
is easily removed for cleaning or replacement.
3.2.3 Impeller
A fully balanced semi-open two vane impeller is
spigotted and screwed to the shaft. The back of the
impeller has integrally cast clearing vanes.
3.2.4 Wear plate
The casing is fitted with a reversible and renewable
steel front wear plate which is a close clearance
against the impeller vanes. If the wear plate
becomes excessively worn, it can be reversed to
present its unworn face to the impeller. The Model
80 wear plate is not reversible.
3.2.5 Cover Plate
A large cover plate below the suction facing retained
by two hand nuts is easily removed to access the
impeller and wear plate for fast cleanout of clogged
or tangled solids.
A PRESSURE RELIEF VALVE IS FITTED TO
THE COVER PLATE AND MUST NOT BE
REMOVED, PLUGGED OR MODIFIED.
3.2.6 Shaft
The shaft is of ample size to transmit the maximum
power required and to minimize deflection and
vibration even during intermittent stop-start
operation. Keys are used to transmit the torque. The
shaft drive end and keyway are in accordance with
ANSI B17.1.
3.2.7 Stuffing box (Seal housing)
The seal housing is positively located, sealed and
fastened to the bearing housing and forms an oil
chamber in which the seal runs fully immersed. The
oil cools and lubricates the seal faces and prevents
seal damage if the pump is run dry. The oil level is
monitored via the sight glass fitted high on the
bearing housing allowing the pump to be shut down
in the event of a seal failure – indicated by a sudden
drop in oil level or product showing in the oil. A vent
is also fitted at the top of the housing to maintain
even atmospheric pressure in the oil chamber.
The seal housing is easily replaceable if wear from
the impeller back sealing vanes becomes excessive.
3.2.8 Shaft seal
The stuffing box is fitted with a double mechanical
seal; the pump end has a hard faced balanced
rotary unit to prevent liquid and grit entering the seal
chamber. The outboard end separates the seal and
bearing oil chambers.
3.2.9 Bearing housing
The robustly designed bearing housing is rigidly
bolted and sealed to the pump casing. The housing
is fitted with oil breather/fillers and sight glasses to
indicate fill and low oil levels. The end cover is fitted
with a lip seal to exclude dirt and moisture. An
eyebolt is fitted to the housing for back pull-out
withdrawal.
3.2.10 Pump bearings and lubrication
The pump is fitted with two different types of ball
bearings. The thrust bearing is a double row angular
contact ball bearing, and the radial bearing a single
row deep groove ball bearing. The thrust bearing is
fitted at the outboard end in all pumps except the
MODEL 80, which has it fitted at the inboard end.
Both bearings run in a common oil bath and are
sized for a long service life.
3.2.11 Impeller adjustment
The bearing housing (back pull-out assembly) is
fastened to the casing with four locknuts; these
locknuts pass through four adjustable spacers in the
bearing housing flange. Accurate impeller setting is
affected by adjustment of these spacer and locking
with the locknuts.
The correct adjustment is 0.38/0.25 mm
(0.015/0.010 in.) clearance between impeller vanes
and wear plate.
Clearance between the impeller and seal housing is
fixed and does not need adjustment.
3.2.12 Driver
The driver is normally an electric motor. Different
drive configurations may be fitted such as an
internal combustion engine, turbines, hydraulic
motors, etc driving via couplings, belts, gearboxes,
drive shafts, etc.
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If the driver is an internal combustion engine which
has not been supplied by Flowserve, a torsional
analysis must be undertaken by the supplier to
select the correct type of coupling in order to avoid
shaft failure.
3.2.13 Guards
Fabricated heavy duty sheet steel or aluminum solid
or vented guards are provided to suit customer
specific needs.
3.2.14 Baseplates
Standard baseplates are steel fabrications. Long
coupled and v-belt driven arrangement are
available. Horizontal driver alignment screws and
baseplate vertical leveling screws are provided as
an option. Special baseplates can be supplied to suit
individual installation needs.
3.3.3 Flange loads
The permissible flange loading has been listed in
the table below.
Pump Size
MODEL 20
MODEL 30
MODEL 40
Suction
MODEL 60
MODEL 80
MODEL 20
MODEL 30
MODEL 40
Discharge
MODEL 60
MODEL 80
Fx Fy Fz Mx My Mz
293.7
(66 023.8)
438.9
(98 664.7)
587.4
(132 047.5)
1026.3
(230 712.2)
1613.7
(362 759.8)
234.3
(52 670.6)
353.1
(79 376.9)
468.6
(105 341.3)
234.3
(52 670.6)
1247.4
(280 415.5)
Maximum forces (kN (lbf)) and Moments (kN.m (lbf.ft))
234.3
(526 703.6)
353.1
(79 376.9)
468.6
(105 341.3)
821.7
(184 718.2)
1247.4
(280 415.5)
191.4
(43 026.7)
293.7
(66 023.8)
382.8
(86 053.4)
191.4
(43 026.7)
1026.3
(230 712.2)
(43 026.7)
(66 023.8)
(86 053.4)
(152 077.2)
(230 712.2)
(66 023.8)
(98 664.7)
(132 047.5)
(66 023.8)
(262 759.8)
3.3 Performance and operating limits
3.3.1 Performance
MPT pumps are furnished for a particular duty and
service conditions advised on your order (See
section 1.5, Duty Conditions). Changes in the
hydraulic system will affect the pump’s performance.
3.3.2 Pressure limits
The operating pressure has been selected to meet
your specific requirements. See section 1.5, Duty Conditions for details.
The pressure and temperature operating limits for
the flanges are in accordance with the relevant
National or International standards unless advised
otherwise.
191.4
293.7
382.8
676.5
1026.3
293.7
438.9
587.4
293.7
1613.7
151.8
(111 967.7)
313.5
(231 237.6)
438.9
(323 732.6)
759
(229 838.4)
1164.9
(859 230.2)
151.8
(111 967.7)
313.5
(231 237.6)
438.9
(323 732.6)
151.8
(111 967.7)
1164.9
(859 230.2)
75.9
(55 983.8)
155.1
(114 401.8)
224.4
(165 517.4)
389.4
(287 221.4)
580.8
(428 398.1)
75.9
(55 983.8)
155.1
(114 401.8)
224.4
(165 517.44)
75.9
(55 983.8)
580.8
(428 398.08)
(85 192.8)
(175 253.8)
(243 408)
(428 398.1)
(627 992.6)
(85 192.8)
(175 253.8)
(243 408)
(85 192.8)
(627 992.6)
115.5
237.6
330
580.8
851.4
115.5
237.6
330
115.5
851.4
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F = External force, tensile or compression
M = External moment, clockwise or counterclockwise
• Forces and moments may be applied
simultaneously in any direction
• Values apply to all materials
• Higher loads may be acceptable, if direction
and magnitude of individual loads are known,
but these need approval
• Pumps must be on rigid foundations and
baseplate fully grouted
• Pump/Baseplate should not be used as pipe
anchor. Expansion joints must be properly tied
• If in doubt, contact Flowserve for information
3.3.4 Pump lubricant data
Pump bearings and mechanical seals are oil
lubricated. The oil levels in their respective
chambers are monitored via fitted sight glasses.
The recommended oil is Mobil DTE Medium or
Castrol Hyspin AWH46.
The allowable pump working temperature range is
0 °C to +75 °C (32 °F to +167 °F).
3.3.6.2 Ambient temperature
These pumps are generally fitted with TEFC motors
with an ambient temperature limit of 0 °C to +40 °C
(32 °F to 104 °F). Specific pumps may be fitted wit h
motors to suit the client’s requirements with other
ambient temperature limits – see motor nameplate
for details.
4 INSTALLATION
4.1 Location
When selecting the location, be sure to install the
unit as close as practicable to the source of the
liquid to be pumped. Allow adequate space for
access, ventilation and maintenance operations
involving dismantling and inspection of parts.
Headroom is an important consideration as an
overhead lift of some type is required for installation
and maintenance of the pump-set.
4.2 Foundation
4.2.1 Install pump units
There are many methods of installing pump units to
their foundations. The correct method depends on
the size of the pump unit, its location, and noise
vibration limitations. Non-compliance with the
provision of correct foundation and installation may
lead to failure of the pump and, as such, would be
outside the terms of the warranty.
4.2.2 Mount baseplate
The baseplate should be mounted onto a firm
foundation, either an appropriate thickness of
concrete or sturdy steel framework. It should NOT
be distorted or pulled down onto the surface of the
foundation, but should be supported to maintain the
original alignment. The location of the foundation
bolts and size of bolt holes can be obtained off the
General Arrangement Drawing (See section 8.7).
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Low vibration levels and long pump life will be
obtained when the foundations have an adequate
mass. Best practice requires the mass of the
foundation block to be five times the mass of the
equipment.
4.2.3 Install baseplate
Install the baseplate onto packing pieces (approx.
25 mm (0.984 in.) to 50 mm (1.969 in.)) evenly
spaced and adjacent to foundation bolts. Level the
baseplate to within 1 mm (0.039 in.) in every 3000
mm (118.11 in.) using a machinist’s level on the
machined surfaces of the pump and driver pads,
placing shims between baseplate and packing
pieces. The pump and driver have been aligned
before dispatch. Check alignment of pump and
motor half coupling. If this is incorrect, it indicates
that the baseplate has become twisted and should
be corrected by re-shimming.
4.3 Grouting
4.3.1 Grouting foundation bolts
Where applicable, grout in the foundation bolts.
4.3.2 Grouting baseplate
After adding pipe work connections and rechecking
the coupling alignment, the baseplate should then
be grouted in accordance with good engineering
practice. Fabricated steel and cast iron base plates
should be filled with grout. If in any doubt, please
contact your nearest Flowserve service center for
advice.
4.3.3 Grouting baseplate prevents movement
Grouting provides solid contact between the pump
unit and foundation, prevents lateral movement of
vibrating equipment, and dampens resonant
vibrations.
4.4 Initial alignment
4.4.1 Thermal expansion
The pump and motor will normally have to be
aligned at ambient temperature and should be
corrected to allow for thermal expansion at
operating temperature. In pump installations
involving high liquid temperatures, the unit should
be run at the actual operating temperature, shut
down, and the alignment checked immediately.
4.4.2 Alignment methods
4.4.2.1 Ensure the pump and motor half
couplings are disconnected.
4.4.2.2 The alignment MUST be checked.
Although the pump will have been aligned at the
factory, it is most likely that this alignment will have
been disturbed during transportation or handling.
Align the motor to the pump, not the pump to the
motor. Alignment is achieved by adding or
removing shims from under the motor feet and also
moving the motor horizontally as required. In some
cases where the alignment cannot be achieved, it
will be necessary to move the pump before
recommencing the above procedure.
4.4.2.3 For couplings with narrow flanges, use a
dial indicator gauge as shown.
The alignment values are maximal for continuous
service.
FINISHED GROUT
LEAVE TOP OF
FOUNDATION ROUGH.
DO NOT FINISH
WITH TROWEL
GROUTINGTOBE
25TO50mmDEEP
CONCRETE
Page 16 of 41
4.4.2.4 Permissible misalignment limits at
working temperature:
Parallel alignment within 0.1 mm (0.004 in.) TIR
Angular alignment within 0.05 mm (0.002 in.) TIR
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
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4.4.2.5 Measure face gap
Face gaps may be measured between the
machined faces using feeler gauges, measuring
wedge, calipers, or suitable micrometer.
4.5 Piping
4.5.1 Protective covers
Protective covers are fitted to the pipe connections
to prevent foreign bodies entering during
transportation and installation. Ensure that these
covers are removed from the pump before
connecting any pipes.
4.5.2 Forces and moments on pump flanges
Maximum forces and moments allowed on the
pump flanges vary with the pump size and type and
are shown in section 3.3.3, Flange Loads. To
minimize these forces and moments that may
cause misalignment, hot bearings, worn couplings,
vibration, and the possible failure of the pump
casing, the following points should be strictly
followed:
• Prevent excessive external pipe load
• Never draw piping into place by applying force
to pump flange connections
• Do not mount expansion joints so that their
force, due to internal pressure, acts on the
pump flange
4.5.3 Inlet pipe
The inlet pipe should be one or two sizes larger
than the pump inlet bore and pipe bends should be
as large a radius as possible. On suction lift the
piping should be inclined up towards the pump inlet
with long eccentric taper pipes incorporated to
prevent air locks. On positive suction, the inlet
piping must have a constant fall towards the pump.
4.5.4 Flow and pump suction
Flow should enter the pump suction with uniform
profile to minimize noise and wear. It is preferable
to have a straight length of suction pipe (approx. 8
to 10 times the pipe diameter) immediately
upstream of the suction nozzle and a straight
length of discharge pipe (approx. 5 to 8 times the
pipe diameter) immediately downstream of the
discharge nozzle.
Do not attach a short radius 90° bend directly on
the suction branch. A long radius suction bend may
be used as long as the bend is perpendicular to the
shaft center line of the unit. Do not install elbows at
an angle other than perpendicular to the shaft axis.
Elbows parallel to the shaft axis will cause uneven
flow into the impeller eyes.
Inlet strainers, when used, should have a net ‘free
area’ of at least three times the inlet pipe area and
a differential pressure device fitted to check for
blockage. Except in unusual circumstances,
strainers are not recommended in inlet piping. If
considerable foreign matter is expected, a screen
installed at the entrance to the wet well is
preferable.
4.5.5 Fitting valves and easy maintenance
Fitting an isolator and non-return valves can allow
easier maintenance. Never throttle pump on
suction side and never place a valve directly on the
pump inlet nozzle. If butterfly valves are used in the
suction line, the spindle must be parallel to the
pump shaft.
4.5.6 Piping and fittings should be flushed
before use.
4.5.7 Corrosive liquids
Piping for corrosive liquids should be arranged to
allow pump flushing before removal of a unit.
4.5.8 Air Release Valve
When a discharge check valve is applied an Air
Release Valve should be placed between the pump
discharge and the check valve. The Air Release
Valve’s function is to vent air from the pump during
the priming cycle. Flowserve Air Release Valves
are available.
4.6 Electrical Connections
4.6.1 Qualified electrician
Electrical connections should be
made by a qualified electrician in accordance with
the relevant local, national, and international
regulations.
It is important to be aware of the EUROPEAN
DIRECTIVE on electromagnetic compatibility when
wiring up and installing equipment on site. Attention
must be paid to ensure that the techniques used
during wiring/installation do not increase
electromagnetic emissions or decrease the
electromagnetic immunity of the equipment, wiring,
or any connected devices. If in any doubt, contact
Flowserve for advice.
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all pipe work are completely
4.6.2 Wiring motor
The motor must be wired up in
accordance with the motor manufacturer's
INSTRUCTIONS (normally supplied within the
terminal box), including any temperature, earth
leakage, current, and other protective devices as
appropriate. The identification nameplate should be
checked to ensure the power supply is appropriate.
4.6.3 Emergency stopping
5 COMISSIONING STARTUP,
OPERATION, AND SHUTDOWN
5.1 Making ready for operation
5.1.1 Lubrication
5.1.1.1 Bearings and mechanical seals
Pump bearings and mechanical seals are not
A device to provide emergency stopping shall
be fitted.
4.6.4 Rotation direction
lubricated by Flowserve. See section 6.2 for oil
chamber filling instructions.
• Bearing housing requires approx.
one liter (33.81 fl. oz.) of oil
• Mechanical seal chamber requires
Check required direction of rotation
before connecting the motor to the pump. Ensure
that the motor over power protection device is set
5% above the maximum power that the pump unit
is expected to absorb.
4.7 Final shaft alignment check
After connecting piping to the pump, rotate the
shaft several times by hand to ensure there is no
binding and all parts are free. The above operation
should be repeated with piping and pump
approx. 350 ml (11.83 fl. oz.) of oil
• Check oil level at the sight glasses
provided before putting into service
5.1.1.2 Driver bearing
Driver bearing lubrication should be in accordance
with the driver manufacturer’s instruction manual.
5.1.1.3 Coupling lubrication
Coupling lubrication, if required, should be in
accordance with the coupling manufacturer’s
instruction manual.
completely filled with water.
5.1.2 Pre-operation check list
Pre-operation Check List
6.2.1 With pump uncoupled start the driver to ensure correct direction of rotation.
6.2.2 Check alignment of piping, valves, and motor pump assembly. Alignment shall be such that joints can be bolted without placing any stress on the piping or pump.
6.2.3 Check all fasteners for tightness.
6.2.4 Visually inspect footing for cracks, etc.
6.2.5 Examine motor shims to ensure that any vibration during operation will not cause them to dislodge.
Checked by Date
6.2.6
6.2.7 Check pump and motor for lubrication.
6.2.8
6.2.9 Check all valves and fittings to ensure that they are installed to allow
6.2.10
6.2.11 Ensure pump/driver-coupling alignment is within the limits specified in 5.6.2.4.
6.2.12 Check all piping, seals, joints, and fittings for leaks.
LUBRICATION SYSTEMS (AS APPLICABLE) ARE CONNECTED AND
OPERATIONAL.
flow in the intended direction.
filled with liquid. Filling plug must be replaced after priming.
CHECK THAT ALL ELECTRICAL, HYDRAULIC, SEALANT AND
ENSURE ALL TERMINAL BOXES AND GUARDS ARE IN PLACE.
Prime the pump. Ensure that the pump casing and
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5.2 Starting the pump
5.2.1 Start-up
Before initial start-up or start-up after a
prolonged period without operation, the rotating
element should be turned by hand to ensure it
rotates freely.
5.2.2 Priming plug
Remove priming plug [4610-3] from casing and
completely fill with water.
This operation is only necessary for the
initial start up. Pump will then remain primed.
5.2.3 Discharge line
When starting the pump, ensure that the discharge
line is empty. The use of valves in the discharge
line must be avoided to achieve correct priming.
If valves are to be fitted to the discharge
line, the specialized automatic air venting
equipment must be fitted to pump. Refer to
Flowserve.
5.2.4 Correct rotation
Priming accomplished, correct rotation established,
and with suction valve wide open, start the pump.
5.2.5 Check outlet pressure and flow.
5.2.6 Pressure
If NO pressure, or LOW pressure, STOP the pump.
Refer to Faults; Causes and Remedies chart
(Section 7) for fault diagnosis.
5.2.7 Outlet valve
the pump has been fully primed and vented, it will
be unnecessary to re-vent or prime the pump.
5.3.1 Mechanical seals
5.3.1.1 Mechanical seals require no adjustment
5.3.1.2 Safeguard the inboard seal face
Before pumping dirty liquids, it is advisable, if
possible, to run the pump in using clean liquid to
safeguard the inboard seal face.
5.3.2 Stop/start frequency
Consult driver manual for maximum number of
starts per hour. STANDBY PUMPS SHOULD BE
RUN ALTERNATELY.
Any slight initial leakage will appear to stop when
the seal is run in. Seals will always have a slight
leakage in operation to lubricate the seal faces.
5.4 Stopping and shutdown
5.4.1 Close the outlet valve
If fitted, close the outlet valve but ensure that the
pump runs in this condition for no more than a few
seconds.
5.4.2 Stop the pump
5.4.3 Prolonged shutdowns
For prolonged shutdowns and especially
when ambient temperatures are likely to drop
below freezing point, close the suction valve and
drain the pump.
Do not run the pump with the outlet valve (if
fitted) closed for a period longer than 30 seconds.
5.2.8 Check the pump unit for vibration or
overheating.
If the vibration and/or temperature are excessive,
STOP the pump. Refer to Faults; Causes and Remedies chart (Section 7) for fault diagnosis.
5.3 Running
Vent the pump to enable all trapped air to
escape, taking due care with hot or hazardous
liquids. Under normal operating conditions, after
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6 MAINTENANCE
6.1 Maintenance schedule
Our specialist service personnel can help with
preventative maintenance records and provide
condition monitoring for temperature and vibration
to identify the onset of potential problems if
required. This schedule is a recommendation only
and is intended to be amended by site experience
of the prevailing conditions. It outlines
recommendations for the pump only and must be
supplemented by schedules for other equipment on
the package.
6.1.1 Routine inspection (daily/weekly)
The following checks should be made and the
appropriate action taken to remedy any deviations:
• Check operating behavior. Ensure performance,
noise, vibration, and bearing temperatures are
normal
• Check that there is no abnormal fluid or
lubricant leakage
• Check running hours since last oil change.
Change if required
• Refer to the manuals of any associated
equipment for routine checks needed
• Check oil levels in seal chamber and bearing
housing
6.1.2 Periodic inspection (6 monthly)
• Check foundation bolts for security of
attachment and corrosion
• The coupling should be checked for correct
alignment and worn driving elements
• Check all paint or protective coatings
• Check all cable glands for tightness
• Refer to the manuals of any associated
equipment for periodic checks needed
6.2 Lubrication data
6.2.1 Oil lubricated bearings and
mechanical seals
Normal intervals between oil changes are 4000
operating hours or a 12-month period. The
characteristics of the installation and severity of
service will determine the frequency of lubrication
change. See Section 3.3.4, Pump lubricant data.
Any sudden change in oil level should be
investigated without delay. A rise in bearing
housing oil level, together with a drop in the seal
chamber oil level, indicates a secondary seal failure
allowing oil leakage from the seal chamber to the
bearing housing. A drop in bearing housing oil level
indicates an external leak and a check of the pump
would show the source as a failure of the bearing
cover lip seal or gasket or a loose drain plug. An
abnormal rise or fall in the seal chamber oil level
with no change in the bearing housing oil level
indicates a primary seal failure with product leaking
into seal chamber or oil leaking into the pump.
Always use the recommended Type and
grade of oil, Mobil DTE Medium or Castrol Hyspin
AWS 46. Never mix oil types.
6.3 Mechanical seals
When leakage becomes unacceptable as
determined above, the seal will need to be repaired
or replaced.
6.4 Dismantling
6.4.1 General
Cleanliness is extremely important and care
must be taken to prevent any foreign material from
entering the pump or its components.
This pump is of the back pull-out design; it is not
necessary to remove the casing, to detach the
suction and delivery piping, or to remove the driver
to dismantle pump.
6.4.2 Dismantling the pump
Refer to Safety section before dismantling
the pump.
6.4.3 Genuine Flowserve parts
Before dismantling the pump for overhaul,
ensure genuine Flowserve replacement parts
are available.
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6.4.4 Part numbers and identification
Refer to section drawing for part numbers and
identification.
6.4.5 Replacing coupling parts
• Isolate electric driver at circuit breaker
• Disassemble and remove coupling guard
• When standard Flex. Pin coupling is fitted, cut
worn rings from coupling pins, clean pins,
expand new rings onto pins, and reassemble
coupling
• When other than standard coupling is fitted,
refer to the coupling manufacturer’s instructions
6.4.6 Complete disassembly
6.4.6.1 Rotating Element (Back pull-out
assembly)
• Remove coupling guard and coupling spacer or
drive belts as applicable
• Drain pump casing by removing vent plug
[6521] and drain plug [6515-0]. Remove any
auxiliary piping and equipment if applicable
• Drain oil from seal chamber and bearing
housing by removing drain plugs [6515-1]
• Remove bearing housing fastener nuts [6580-1]
and slinging housing from the eyebolt [1020]
provided; carefully lift the back pull-out
assembly clear of the casing and remove to
clean work area. Note that bearing housing is
sealed and located into casing with O-ring
[4610-0] and will have to be bumped free
6.4.6.2 Removal of Impeller
• Remove impeller setscrew and washer [2913
and 2905-0]
• Prevent shaft from rotating and unscrew
impeller from shaft (right hand thread)
6.4.6.3 Removal of Seal Housing and
Mechanical Seal
• Remove socket setscrews [6579] and bump
seal chamber free from spigot location on
bearing housing. Take care not to damage
stationary face of inboard seal which is mounted
in housing bore
• Back off seal drive screws and withdraw seal
assembly from shaft
6.4.6.4 Removal of Shaft and Bearings
• Remove hexagon setscrews [6570-0] retaining
bearing cover [3260] and withdraw cover
complete with lip seal [4300]. Note gasket
between bearing housing and cover. Discard
gasket and lip seal and replace with new parts
on assembly
• Press or drive shaft, complete with bearings,
from bearing housing in the direction of the
coupling end of the shaft
• Remove the drive end bearing circlip [6544]
from the shaft. Note that the circlip is fitted to all
size pumps except the MODEL 80. Remove the
bearings from the shaft using a suitable bearing
puller applying pressure to the inner race only to
avoid damaging the bearings or shaft. Bearings
SHOULD NOT be refitted, but if it is intended to
reuse them, they should be wrapped in plastic
ready for washing and inspection
6.4.6.5 Removal of Wear Plate
Remove handnuts [6580-1] and withdraw
coverplate [1223-0]. Remove hexagon setscrews
[6570-1] and separate wear plate from cover. Note
on all pump sizes except the MODEL 80, the wear
plate is reversible.
6.4.6.6 Removal of Valve Flap
Remove nuts [6580-0] from suction flange studs on
all pump sizes except MODEL 80, which uses
hexagon setscrews [6570-5], and remove suction
flange complete with valve flap. Remove check
valve pin [6570-4] and withdraw flap.
6.5 Examination of parts
6.5.1 Used parts
Used parts must be inspected before assembly to
ensure the pump will subsequently run properly. In
particular, fault diagnosis is essential to enhance
pump and plant reliability.
6.5.2 Casing, impeller, wear plate, and seal
housing
Inspect for excessive wear, pitting, corrosion,
erosion, or damage and any sealing surface
irregularities. The wear plate on all pump sizes can
be re-machined to restore its wearing face and on
all sizes except the MODEL 80 can be reversed to
present an unworn face to the impeller. Replace as
necessary.
6.5.3 Shaft, keys, and impeller setscrew
Check shaft for straightness and any damage and
bearing lands for fit, the bearings should be a
maximum 0.013 mm (0.0005 in.) interference fit on
shaft. Check keys for damage and fit in keyways
and impeller setscrew for erosion damage.
6.5.4 Gaskets, O-rings, and lip seals
After dismantling, discard and replace.
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6.5.5 Bearings
Bearings generally MUST NOT BE reused after
removal from any shaft; however, due to the small
interference fit of the bearings in these pumps, if
they are removed carefully by pulling on the inner
ring only without the use of heat and if thorough
cleaning and inspection shows them fit for further
service, they may be reused. It is strongly
recommended, however, that they be replaced as a
matter of course. Thoroughly clean the inside of
the bearing housing, bearing cover, and seal
housing, removing any sign of contamination or
rust and dry out with lint-free cloths or dry air.
6.5.6 Suction flange and flap valve
Check the valve seating on the suction flange for
erosion damage and the flap valve for deterioration
of the neoprene sealing surface and replace if
necessary.
6.5.7 Mechanical seal
Carefully inspect seal faces for cracks, chips, or
scoring and O-rings for any obvious damage. If in
doubt either replace or return seal to Flowserve
service center for inspection.
6.6 Assembly
6.6.1 To assemble the pump consult the
sectional drawings.
6.6.2 Prepare
Ensure all parts are on hand; clean and fit for
further service. Pay particular attention to threads
and gasket and O-ring sealing faces. Lightly apply
anti-seize compound to all threads and close fitting
surfaces. Do not unwrap bearings and seals or
expose the bearing housing and seal chamber
inner surfaces until time to fit. Immediately prior to
assembly, wipe clean with lint-free cloth.
6.6.3 Bearings
• Carefully press the bearings onto the shaft,
applying load to inner ring only; ensure bearings
are pushed hard up against the location
shoulder on the shaft. It is not necessary to use
heat to fit MPT bearings as only light press fits
are involved. If desired, bearings can be heated
to approx. 100 °C (212 °F) with an induction
heater, but under no circumstances use a flame
on the bearings. Fit the circlip [6544] to the shaft
at the outboard bearing [3041]. Note that a
circlip is fitted on all pump sizes except the
MODEL 80
• Support shaft/bearing assembly on clean vee
blocks under the bearings and check shaft
runout at coupling end and mechanical seal
area. Runout is not to exceed 0.05 mm (0.002
in.) TIR
• Push shaft/bearing assembly into bearing
housing from drive end, ensuring that thrust
bearing bottoms against shoulder in bearing
housing and that shaft rotates freely
• Fit new lip seal [4300] into bearing cover [3260].
Note orientation of lip seal (spring loaded lip
faces toward coupling)
• Fit new gasket at bearing housing face and refit
cover; ensure that seal lip is lightly oiled and
care is taken easing it over shaft shoulder. Refit
and tighten cover fasteners. Check that shaft
rotates freely
6.6.4 Mechanical seal
• Fit mechanical stationary face holder in recess
at inboard end of bearing cover and fit
stationary face. Take extreme care to keep face
clean and prevent damage. Lightly oil seal
rotating assembly and carefully slide over shaft
to seat against stationary
• Fit inboard stationary face holder in recess in
seal chamber and carefully fit stationary face
• Fit new O-ring to recess in bearing housing
joint, fit seal chamber over end of shaft, and
locate on bearing housing spigot. Refit and
tighten fasteners
6.6.5 Impeller
• Lightly coat shaft and impeller threads with antiseize. Preventing shaft from rotating, screw
impeller onto shaft and bottom firmly against
shaft shoulder. Fit and tighten impeller setscrew
[2913] complete with washer [2905-0]
• Check impeller to seal housing axial clearance,
which should be within the range 0.05/1.35 mm
(0.002/ 0.053 in.) on a new assembly
6.6.6 Suction flange
• Refit valve flap to suction flange with check
valve pin [6570-4] and nylon washer [2905-1]
• Fit suction flange to casing with new gasket
[4510-1]
6.6.7 Coverplate/wear plate
• Refit new, re-machined, or reversed wear plate
[1915] to the cover plate [1223-0]
• Fit new O-ring [4610-2] to cover and lightly oil
• Fit cover into casing and retain with hand nuts
[6580-1]
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6.6.8 Back pull-out assembly/case
• Fit new O-ring [4610-0] to bearing housing
spigot and lightly oil
• Ensure that spacing bushes [1680] are screwed
fully home in bearing housing flange. This will
give maximum impeller clearance on assembly
• Sling from eyebolt [1020] and fit back pull-out
assembly into casing, taking care not to damage
machined casing bores and O-ring. Tighten
fasteners finger tight only
• Back off stud nuts [6580-1] and spacing bushes
in turn by equal amounts, at the same time
pushing back pull-out assembly into casing until
impeller contacts wear plate. At this stage check
the gap between the bearing housing and case
at four places to ensure that assembly is fully
seated on wear plate
• To obtain correct clearance at wear plate turn
spacing bushes each one flat in a clockwise
direction. This will give a clearance of 0.30 mm
(0.012 in.) and the nuts [6580-1] can now be
fully tightened
6.6.9 Lubrication
Ensure oil chamber drain plugs are tightly fitted,
remove air vents [3854] from bearing housing and
seal chamber, and fill both chambers to the correct
level on the sight glasses [3858] with Mobil DTE
Medium or Castrol Hyspin AWS 46 oil.
Approximately one liter (33.81 fl. oz.) of oil in seal
chamber and 350 ml (11.83 fl. oz.) in the bearing
housing are needed. Refit vents and check for
leaks. Now that seals are lubricated, check element
for free rotation.
6.6.10 Final assembly
• Refit coupling and connect driver. Check driver
alignment
• Refit guards
• Refit suction and discharge piping with new
gaskets
• Check all fasteners and plugs for tightness
6.7 Spare Parts
6.7.1 Ordering of spares
Flowserve keeps records of all pumps that have
been supplied. When ordering spares the following
information should be quoted:
(1) Pump serial and service number(s)
(2) Pump type and size
(3) Part name
(4) Part number
(5) Number of parts required
6.7.2 Pump details
The pump size and serial number are shown on the
pump nameplate.
6.7.3 Genuine parts
To ensure continued satisfactory operation,
replacement parts to the original design
specification should be obtained from Flowserve.
Any change to the original design specification,
modification or use of a non-standard part) will
invalidate the pumps safety certification.
6.7.4 Recommended spares
Start up spares:
Normal maintenance spares:
1 – complete set of O-rings, gaskets, and lip seal
1 – mechanical sea
1 – set of bearings
1 – bearing circlip (not applicable MODEL 80)
1 – check valve flap
1 – wear plate
Critical service:
1 – complete set of O-rings, gaskets and lip seal
1 – mechanical seal
1 – set of bearings
1 – bearing circlip (not applicable MODEL 80)
1 – check valve flap
1 – wear plate
1 – impeller
1 – shaft
6.7.5 Storage of spares
Spares should be stored in a clean, dry area away
from vibration. Inspection and re-treatment of
metallic surfaces (if necessary) with preservative is
recommended at six monthly intervals.
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7 FAULTS; CAUSES AND REMEDIES
FAULT SYMPTOM
Pump overheats and seizes
Bearings have short life
⇓⇓⇓⇓
⇓⇓⇓⇓
Pump vibrates or is noisy
⇓⇓⇓⇓
⇓⇓⇓⇓
Mechanical seal has short life
⇓⇓⇓⇓
⇓⇓⇓⇓
Mechanical seal leaks excessively
⇓⇓⇓⇓
B. MECHANICAL TROUBLES
⇓⇓⇓⇓
Pump requires excessive power
⇓⇓⇓⇓
⇓⇓⇓⇓
Pump loses prime after starting
⇓⇓⇓⇓
⇓⇓⇓⇓
Insufficient pressure developed
⇓⇓⇓⇓
⇓⇓⇓⇓
Insufficient capacity delivered
⇓⇓⇓⇓
⇓⇓⇓⇓
⇓⇓⇓⇓
⇓⇓⇓⇓
Pump does not deliver liquid
PROBABLE CAUSES POSSIBLE REMEDIES
⇓⇓⇓⇓
⇓⇓⇓⇓
A. SYSTEM TROUBLES
Pump not primed. Check complete filling
Pump or suction pipe not completely filled
with liquid.
Suction lift too high or level too low.
Excessive amount of air or gas in liquid. Check and purge from pipes
Air or vapour pocket in suction line. Check suction line design for pockets
Air leaks into suction line.
Air leaks into pump through mechanical seal,
sleeve joints, casing joint or pipe lugs.
Foot valve too small. Investigate replacing the foot valve
Foot valve partially clogged. Clean foot valve
Inlet of suction pipe insufficiently submerged. Check cut out system design
Total head of system higher than differential
head of pump.
Total head of system lower than pump design
head.
Specific gravity of liquid different from design. Consult Flowserve
Viscosity of liquid differs from design. Consult Flowserve
Operation at very low capacity.
Operation at high capacity.
Misalignment due to pipe strain.
Improperly designed foundation.
Shaft bent.
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
Check and complete filling
Check NPSHa>NPSHr, proper
submergence, losses at strainers and
fittings
Check airtight pipe then joints and
gaskets
Check airtight assembly then joints
and gaskets
Check discharge head and head
losses in discharge pipe at the valve
settings. Check back pressure is not
too high
Throttle at discharge valve or ask
Flowserve if the impeller can be
trimmed
Measure value and check minimum
permitted
Measure value and check maximum
permitted
Check the flange connections and
eliminate strains using elastic
couplings or a method permitted
Check setting of baseplate: tighten,
adjust, grout base as required
Check shaft runouts within acceptable
values
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FAULT SYMPTOM
Pump overheats and seizes
Bearings have short life
⇓⇓⇓⇓
⇓⇓⇓⇓
Pump vibrates or is noisy
⇓⇓⇓⇓
⇓⇓⇓⇓
Mechanical seal has short life
⇓⇓⇓⇓
⇓⇓⇓⇓
Mechanical seal leaks excessively
⇓⇓⇓⇓
C. ELECTRICAL TROUBLES
⇓⇓⇓⇓
⇓⇓⇓⇓
⇓⇓⇓⇓
Pump requires excessive power
Pump loses prime after starting
⇓⇓⇓⇓
⇓⇓⇓⇓
Insufficient pressure developed
⇓⇓⇓⇓
⇓⇓⇓⇓
Insufficient capacity delivered
⇓⇓⇓⇓
⇓⇓⇓⇓
Pump does not deliver liquid
⇓⇓⇓⇓
⇓⇓⇓⇓
PROBABLE CAUSES POSSIBLE REMEDIES
⇓⇓⇓⇓
⇓⇓⇓⇓
Rotating part rubbing on stationary part
internally.
Bearings worn Replace bearings
Wearing ring surfaces worn. Replace worn wear ring/ surfaces
Impeller damaged or eroded. Replace impeller and check reason
Leakage under sleeve due to joint failure. Replace joint and check for damage
Mechanical seal improperly installed.
Incorrect type of mechanical seal for
operating conditions.
Shaft running off centre because of worn
bearings or misalignment.
Impeller out of balance resulting in vibration. Check and consult Flowserve
Abrasive solids in liquid pumped. Check and consult Flowserve
Mechanical seal was run dry.
Internal misalignment due to improper repairs
causing impeller to rub.
Excessive thrust caused by a mechanical
failure inside the pump.
Excessive grease in ball bearings. Check method of regreasing
Lack of lubrication for bearings.
Improper installation of bearings
Damaged bearings due to contamination.
Wrong direction of rotation.
Motor running too slow, Check motor terminal box connections
Check for signs of this and consult
Flowserve if necessary
Check alignment of faces or damaged
parts and assembly method used
Consult Flowserve
Check misalignment and correct if
necessary. If alignment satisfactory
check bearings for excessive wear
Check mechanical seal condition and
source of dry running and repair
Check method of assembly, possible
damage or state of cleanliness during
assembly
Check wear condition of Impeller, its
clearances and liquid passages
Check hours run since last change of
lubricant, the schedule and its basis
Check method of assembly, possible
damage or state of cleanliness during
assembly and type of bearing used
Check contamination source and
replace damaged bearings
Reverse 2 phases on motor terminal
box
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8 PARTS LIST AND DRAWINGS
8.1 Sectional Arrangement and Parts List Drawings – MODEL 20
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143A2A39
ITEM DESCRIPTION No. OF DRG. No. MATERIAL CCN No.
7000 INSTRUCTION MANUAL 1 PAPER 85392699
6821 DRIVE SCREWS (NAMEPLATE) 4 122A2R37 SS 95330452
9322-3 WARNING TAG - ALIGNMENT 1
9323 DECAL - PRIMING 1
9322-0 NAMEPLATE 1 AY51851A SS 78800505
ABOVE ITEMS NOT SHOWN ON DRAWING
SPARES ITEM DESCRIPTION No. OF DRG. No. MATERIAL CCN No.
6700 KEY 1 11A9C85 C. STL. 95264024 6580-2 HAND NUT 2 1038A020MPTA001 C. I. 75533802 6580-1 HEX NUT – BEARING HOUSING 4 38A4S5 ST. STL. 95296992 6580-0 HEX NUT – SUCTION FLANGE 4 38A4C7 C. STL. 95084760 6579 FERRYHEAD SCREW 4
6572-3 STUD – SUCTION FLANGE 4 13A3J399 C. STL. 95150314 6572-2 STUD – BEARING HOUSING 4 12A3S254 ST. STL. 75543421 6572-1 STUD – HAND NUT 2 13A3J250 ST. STL. 95236378 6570-4 CAPSCREW (PIN) - VALVE 1 2714A020MPTA001 C. STL. 75534222 6570-3 CAPSCREW – DISCHARGE 4 35A2C325 C. STL. 95002168 6570-1 CAPSCREW – WEAR PLATE 2 35A2C108 C. STL. 95079711 6570-0 CAPSCREW – BEARING COVER 4 35A2C4 C. STL. 95211393 6569 PLUG SQ. HEAD – SUCTION FLANGE 1 30A7C3 C. STL. 95061479-
2 6544 RETAINING RING 1 162A13S118 C. STL. 95223368-
6541 LOCKWASHER – WEAR PLATE 2 14A5C76 C. STL. 95081857 6541-1 LOCKWASHER – A & B SUCTION FLG 4 14A5C120 C. STL. 95081790 6521 PLUG SQ. HEAD – CASING 2 30A7C3 C. I. 95061479 6515-1 PLUG SQ. HEAD – BEARING HOUSING 2 30A7C3 C. I. 95061479 6515-0 PLUG SQ. HEAD – CASING DRAIN 1 30A7C6 C. I. 95033544-
6511 PRIMING PLUG 1 565A10S10 C. STL. 956638032 6301 FLAPPER VALVE 1 2214A020MPTA001 NEOPRENE 755308992 4610-3 O-RING – PRIMING PLUG 1 20A11EM222 VITON 950222321 4610-2 O-RING – COVER PLATE/CASING 1 20A11CM437 Buna N 950872431 4610-1 O-RING – BEARING HSG/SEAL HSG 1 20A11CM244 Buna N 950866661 4610-0 O-RING – CASING /BEARING HSG 1 20A11CM360 Buna N 952772651 4590-2 GASKET – END COVER 1 2584A020MPTA001 NTL/SYN 755309641 4590-1 GASKET – FLANGE SUCTION 1 2586A020MPTA001 NTL/SYN 755166661 4590-0 GASKET – DISCHARGE 1 32A11X6 NTL/SYN 606698681 4300 LIP SEAL – BEARING COVER 1 2796A118DIAC001 NITRILE 755540712 4200 MECHANICAL SEAL 1 1802A112MPTA001 BX/C F X/JF
4011 SEAL HOUSING 1 2632A020MPTA001 C. I. 75531004 3858 SIGHT GLASS 3 4260A000MPTA001 POLYMIDE 75553578 3854 AIR VENT 2 - STEEL 81300261 3260 BEARING COVER 1 0573A020MPTA001 C. I. 75530931 3200 BEARING HOUSING 1 1109A020MPTA001 C. I. 75533869-
2 3043 BALL BEARING - NDE 1 26A19X206 STEEL 952006302 3041 BALL BEARING - DE 1 27A19X306 STEEL 95200762-
3 2200 IMPELLER 1 1129A020MPTA001 D. I. 755166173 2100 SHAFT 1 2807A020MPTA001 ST. STL. 755333152 1915 WEAR PLATE 1 1869A020MPTA001 C. I. 75529487-
1680 SPACER BUSHING 4 2454A020MPTA001 ST. STL. 75533232 1223-0 COVER PLATE 1 2729A020MPTA001 C. I. 75531038 1139 SUCTION FLANGE - 2” NPT 1 0850A020MPTA001 C. I. 75530113 1100 CASING 1 2469A020MPTA001 C. I. 75533893 1020 EYE BOLT 1 124A2C3X0.5 C. STL. 75536938-
RECOMMENDED SPARES INDICATED THUS :- 1 = START-UP SPARES
2 = NORMAL MAINTENANCE SPARES (INCLUDES START-UP)
3 = CRITICAL SERVICE (INCLUDES START-UP/MAINTENANCE)
RECOMMENDED OIL :- Mobil DTE Medium or Castrol Hyspin AWS 46 oil
OIL QUANTITY :- SEAL CHAMBER APPROX. 1 L (33.81 fl. oz.)
BEARING HOUSING APPROX. 350 ml (11.83 fl. oz.)
AL. STL. 95309803-
75555284-
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8.2 Sectional Arrangement and Parts List Drawings – MODEL 30
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ITEM DESCRIPTION No. OF DRG. No. MATERIAL CCN No.
7000 INSTRUCTION MANUAL 1 PAPER 85392699
6821 DRIVE SCREWS (NAMEPLATE) 4 122A2R37 SS 95330452
9322-3 WARNING TAG - ALIGNMENT 1
9323 DECAL - PRIMING 1
ABOVE ITEMS NOT SHOWN ON DRAWING
9322-0 NAMEPLATE 1 AY51851A SS 78800505
SPARES ITEM DESCRIPTION No. OF DRG. No. MATERIAL CCN No.
6700 KEY 1 11A9C137 C. STL. 95293080 6580-2 HAND NUT 2 1038A020MPTA001 C. I. 75533802 6580-1 HEX NUT - BEARING HOUSING 4 38A4S7 ST. STL. 95370581 6580-0 HEX NUT - SUCTION FLANGE 4 38A4C7 C. STL. 95084760 6579 FERRYHEAD SCREW 4 143A2A79 AL. STL. 95410577 6572-3 STUD - SUCTION FLANGE 4 13A3J398 C. STL. 95688156 6572-2 STUD - BEARING HOUSING 4 12A2S254 ST. STL. 75543439 6572-1 STUD - HAND NUT 2 13A3J389 ST. STL. 95159166 6570-4 CAPSCREW (PIN) - VALVE 1 2714A030MPTA001 C. STL. 75534230 6570-3 CAPSCREW - DISCHARGE 4 35A2C325 C. STL. 95002168 6570-2 CAPSCREW - HANDLE 2 35A2C110 C. STL. 95053146 6570-1 CAPSCREW - WEAR PLATE 4 35A2C110 C. STL. 95053146 6570-0 CAPSCREW - BEARING COVER 4 35A2C111 C. STL. 68885607-
6569 PLUG SQ. HEAD - SUCTION FLANGE 1 30A7C3 C. STL. 95061479-
2 6544 RETAINING RING 1 173A13S175 C. STL. 95391264-
6541 LOCKWASHER - WEAR PLATE 4 14A5C76 C. STL. 95081857 6521 PLUG SQ. HEAD - CASING 2 30A7C3 C. I. 95061479 6515-1 PLUG SQ. HEAD - BEARING HOUSING 2 30A7C4 C. I. 95078606 6515-0 PLUG SQ. HEAD - CASING DRAIN 1 30A7C7 C. I. 95033551-
6511 PRIMING PLUG 1 565A10S10 C. STL. 956638032 6301 FLAPPER VALVE 1 2214A030MPTA001 NEOPRENE 755185551 4610-3 O-RING - PRIMING PLUG 1 20A11EM222 VITON 950222321 4610-2 O-RING - COVER PLATE/CASING 1 20A11CM447 Buna N 950179191 4610-1 O-RING - BEARING HSG/SEAL HSG 1 20A11CM260 Buna N 950868981 4610-0 O-RING - CASING /BEARING HSG 1 20A11CM446 Buna N 950179011 4590-2 GASKET - END COVER 1 2586A030MPTA001 NTL/SYN 755303451 4590-1 GASKET - FLANGE SUCTION 1 2586A030MPTA001 NTL/SYN 755166741 4590-0 GASKET - DISCHARGE 1 32A11X8 NTL/SYN 606698761 4300 LIP SEAL - BEARING COVER 1 2796A175DIAB001 NITRILE 755540552 4200 MECHANICAL SEAL 1 1802A150MPTA001 BX/C F X/JF
4011 SEAL HOUSING 1 2632A030MPTA001 C. I. 75517375-
3260 BEARING COVER 1 0573A080MPTA001 C. I. 75516989-
3200 BEARING HOUSING 1 1109A080MPTA001 C. I. 755181672 3043 BALL BEARING - NDE 1 24A19X311 STEEL 954289422 3041 BALL BEARING - DE 1 27A19X311 STEEL 95214037-
2913 CAPSCREW - IMPELLER 1 35A2T323 ST. STL. 95251856-
2905-1 WASHER - VALVE 1 11A5X4 NYLON 97461974-
2905-0 WASHER - IMPELLER 1 2888A030MPTA001 ST. STL. 755296443 2200 IMPELLER 1 1129A080MPTA001 D. I. 755166583 2100 SHAFT 1 2807A080MPTA001 ST. STL. 755329292 1915 WEAR PLATE 1 1869A080MPTA001 C. I. 75518415-
1680 SPACER BUSHING 4 2454A030MPTA001 ST. STL. 75517524-
1223-1 HANDLE - COVER PLATE 2 1032A000MPTA001 D. I. 75516906-
1223-0 COVER PLATE 1 2729A080MPTA001 C. I. 75517987-
1139 SUCTION FLANGE - 8” 125# SPOOL 1 0850A080MPTC001 C. I. 75516732-
1100 CASING 1 2469A080MPTA001 C. I. 75525386-
1020 EYE BOLT 1 124A2C3X0.5 C. STL. 75536938-
RECOMMENDED SPARES INDICATED THUS :- 1 = START-UP SPARES
2 = NORMAL MAINTENANCE SPARES (INCLUDES START-UP)
3 = CRITICAL SERVICE (INCLUDES START-UP/MAINTENANCE)
RECOMMENDED OIL :- Mobil DTE Medium or Castrol Hyspin AWS 46 oil
OIL QUANTITY :- SEAL CHAMBER APPROX. 1 L (33.81 fl. oz.)
BEARING HOUSING APPROX. 350 ml (11.83 fl. oz.)
75555326-
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8.7 General Arrangement Drawing
The typical general arrangement drawing and any
specific drawings required by the Contract will be
sent to the Purchaser separately. If required, these
should be obtained from the Purchaser and
retained with this manual.
9 CERTIFICATION
Certificates determined from the Contract
requirements are provided with these instructions
where applicable. Examples are certificates for CE
marking, ATEX marking, etc. If required, copies of
other certificates sent separately to the Purchaser
should be obtained from the Purchaser for retention
with these User Instructions.
10 OTHER RELEVANT
DOCUMENTATION AND MANUALS
10.1 Supplementary Instruction
Manuals
See also the supplementary instruction manuals
supplied with this manual, e.g., for electric motors,
controllers, engines, gearboxes, sealant systems,
etc.
10.2 Change notes
If any changes, agreed with Flowserve Pump
Division, are made to the product after its supply, a
record of the details should be maintained with
these User Instructions.
MPT USER INSTRUCTIONS ENGLISH 85392699 06-09
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NOTES
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NOTES
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NOTES
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FLOWSERVE
REGIONAL SALES OFFICES:
USA and Canada
Flowserve Corporation (Pump Division)
5215 North O’Connor Blvd. Suite 2300
Irving, Texas 75039, USA