Flowserve PVML User Manual

®
Pump Division
Type: PVML CENTRIFUGAL PUMPS
USER INSTRUCTIONS: INSTALLATION, OPERATION, MAINTENANCE

PCN=00079591, ed. 01-05 (E)

These instructions should be read prior to installing,
operating, using and maintaining this equipment.
PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
®
CONTENTS
PAGE
1 INTRODUCTION AND SAFETY............................3
1.1 General ...........................................................3
1.2 CE marking and approvals..............................3
1.3 Disclaimer .......................................................3
1.4 Copyright.........................................................3
1.5 Duty conditions................................................3
1.6 Safety..............................................................4
1.7 Nameplate and warning labels........................7
1.8 Specific machine performance........................8
1.9 Noise level.......................................................8
2 TRANSPORT AND STORAGE..............................9
2.1 Consignment receipt and unpacking...............9
2.2 Handling..........................................................9
2.3 Lifting...............................................................9
2.4 Storage............................................................9
2.5 Recycling and end of product life.................... 9
3 PUMP DESCRIPTION......................................... 10
3.1 Configurations...............................................10
3.2 Name nomenclature......................................10
3.3 Design of major parts....................................10
3.4 Performance and operating limits.................10
4 INSTALLATION.................................................... 11
4.1 Location.........................................................11
4.2 Part assemblies.............................................11
4.3 Foundation....................................................11
4.4 Grouting ........................................................11
4.5 Initial alignment.............................................13
4.6 Piping............................................................13
4.7 Electrical connections ...................................14
4.8 Final shaft alignment check ..........................15
4.9 Protection systems........................................15
5 COMMISSIONING, START-UP, OPERATION AND
SHUTDOWN.......................................................15
5.1 Pre-commissioning procedure......................15
5.2 Pump lubricants ............................................15
5.3 Impeller clearance......................................... 15
5.4 Direction of rotation.......................................15
5.5 Guarding .......................................................15
5.6 Priming and auxiliary supplies ......................15
5.7 Starting the pump..........................................16
5.8 Running the pump.........................................16
5.9 Stopping and shutdown.................................17
5.10 Hydraulic, mechanical and electrical duty...17
6 MAINTENANCE...................................................18
6.0 General .........................................................18
6.1 Maintenance schedule..................................18
6.2 Spare parts....................................................19
6.3 Recommended spares
and consumable items ..................................19
6.4 Tools required................................................19
6.5 Fastener torques...........................................20
6.6 Setting impeller clearances...........................20
6.7 Disassembly..................................................20
6.8 Examination of parts .....................................21
6.9 Assembly.......................................................22
PAGE
7 FAULTS; CAUSES AND REMEDIES.................. 25
8 PARTS LIST AND DRAWINGS........................... 27
8.1 Sectional drawings -PVML ........................... 27
8.2 Parts list -PVML............................................ 27
8.3 General arrangement drawing...................... 28
9 CERTIFICATION................................................. 28
10 OTHER RELEVANT DOCUMENTATION AND
MANUALS.......................................................... 28
10.1 Supplementary User Instructions ............... 28
10.2 Change notes ............................................. 28
10.3 Additional sources of information................ 28
ALPHABETICAL INDEX
PAGE
CE marking and approvals (1.2) ............................... 3
Clearances (see 6.7, Renewal clearances) ............ 20
Commissioning and operation (see 5) .................... 15
Configurations (3.1)................................................. 10
Direction of rotation (5.4)......................................... 15
Dismantling (see 6.7, Disassembly)........................ 20
Duty conditions (1.5) ................................................. 3
Electrical connections (4.7)..................................... 14
Examination of parts (6.8)....................................... 21
Faults; causes and remedies (7.0).......................... 25
General assembly drawings (see 8)........................ 28
Grouting (4.4).......................................................... 12
Guarding (5.5)......................................................... 15
Handling (2.2)............................................................ 9
Hydraulic, mechanical and electrical duty (5.10) .... 17
Lifting (2.3) ................................................................ 9
Location (4.1) .......................................................... 11
Lubrication schedule (see 5.2, Pump lubricants).... 15
Maintenance schedule (6.1).................................... 18
Piping (4.6).............................................................. 13
Priming and auxiliary supplies (5.6)........................ 15
Reassembly (see 6.9, Assembly)............................ 22
Replacement parts (see 6.2 and 6.3)...................... 19
Safety, protection systems (see 1.6 and 4.9)
Sound level (see 1.9, Noise level)............................. 8
Specific machine performance (1.8) ......................... 8
Starting the pump (5.7)............................................ 16
Stopping and shutdown (5.9).................................. 17
Storage (2.4) ............................................................. 9
Supplementary manuals or information sources..... 28
Tools required (6.4)................................................. 19
Torques for fasteners (6.5)...................................... 20
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PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
®

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, utilising sophisticated quality techniques, and safety requirements.
Flowserve is committed to continuous quality improvement and being at service for any further information about the product in its installation and operation or about its support products, repair and diagnostic services.
These instructions are intended to facilitate familiarization with the product and its permitted use. Operating the product in compliance with these instructions is important to help ensure reliability in service and avoid risks. The instructions may not take into account local regulations; ensure such regulations are observed by all, including those installing the product. Always coordinate repair activity with operations personnel, and follow all plant safety requirements and applicable safety and health laws and regulations.
These instructions should 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. 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 Pump Division to provide sound and all necessary information the content of this manual may appear insufficient and is not guaranteed by Flowserve as to its completeness or accuracy.
Flowserve manufactures products to exacting International Quality Management System Standards as certified and audited by external Quality Assurance organisations. Genuine parts and accessories have been designed, tested and incorporated into the products to help ensure their continued product quality and performance in use. As Flowserve cannot test parts and accessories sourced 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 authorised 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 purchaser order. The acknowledgement of these conditions has been sent separately to the Purchaser. A copy should be kept with these instructions.
The product must not be operated beyond
the parameters specified for the application. If there is any doubt as to the suitability of the product for the application intended, contact Flowserve for advice, quoting the serial number.
If the conditions of service on your purchase order are going to be changed (for example liquid pumped, temperature or duty) it is requested that the user seeks Flowserve’s written agreement before start up.
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PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
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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 instruct ions 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 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 b e avoided.
NEVER APPLY HEAT TO REMOVE IMPELLER Trapped lubricant or 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.
HAZARDOUS LIQUIDS When the pump is handling hazardous liquids care must be taken to avoid expo sure to th e liquid by appro priate situating the pump, limiting person nel acce ss 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.
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PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
®
appropriate. Always check that the driver, seal and
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.
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, which is quite unusual for a PVML pump due to the closed coupled design, the Ex rating applies only
ENSURE CORRECT LUBRICATION (See section 5, Commissioning, start-up, operation and shutdown.)
START THE PUMP WITH OUTLET VALVE PARTLY 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. The pump outlet control valve 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
INLET VALVES TO BE FULLY OPEN WHEN PUMP IS RUNNING Running the pump at zero flow or below the recommended minimum flow continuously will cause damage to the seal.
DO NOT RUN THE PUMP AT ABNORMALLY HIGH OR LOW FLOW RATES Operating at a flow rate higher than normal or at a flow rate with no back pressure on the pump may overload the motor and cause cavitation. Low flow rates may cause a reduction in pump/bearing life, overheating of the pump, instability and cavitation/ vibration.
to the pump. The party responsible for assembling the pump set shall select the driver 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 affects in the motor and so, for pumps sets with a VFD, the ATEX Certification for the motor must state that it is covers the situation where electrical supply is from the VFD. This particular requirement still applies even if the VFD is in a safe area.
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 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 prEn13463-5)

1.6.4 Products used in potentially explosive atmospheres

Maximum surface temperature (Temperature Class) (See section 1.6.4.3.)
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
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 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.
Use equipment only in the zone for whi ch it is
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PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
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The temperature rise at the seals and bearings and due to the minimum permitted flow rate is taken into account in the temperatures stated.
Temperature
class to
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)
Temperature limit of liquid
handled (* depending on
material and construction
variant - check which is lower)
Consult Flowserve
Consult Flowserve 115 °C (239 °F) * 180 °C (356 °F) * 275 °C (527 °F) * 400 °C (752 °F) *
The responsibility for compliance with the specified maximum liquid temperature is with the plant operator.
Temperature classification “Tx” is used when the liquid temperature varies and the pump could be installed in different hazarous 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.
Where there is any risk of the pump being run against a closed valve generating high liquid and casing external surface temperatures 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 make routine vibration monitoring checks.
In dirty or dusty environments, regular checks must be made and dirt removed from areas around close clearances and motors.
1.6.4.4 Preventing the build up of explosive mixtures
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 a power monitor).
To avoid potential hazards from fugitive emissions of vapour 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 motor stool guard must be non-sparking and anti-static for Category 2.
To avoid the potential hazard from random induced current generating a spark, the earth contact on the levelling plate or base plate must be used.
Avoid electrostatic charge: do not rub non-metallic surfaces with a dry cloth; ensure cloth is damp.
1.6.4.6 Preventing leakage
The pump must only be used to handle liquids for which it has been approved to have the correct corrosion resistance.
Avoid entrapment of liquid in the pump 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 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
ENSURE THE PUMP IS PROPERLY FILLED
AND VENTED AND DOES NOT RUN DRY Ensure the pump and relevant suction and discharge
pipeline system is totally filled with liquid at all times during the pump operation, so that an explosive atmosphere is prevented. In addition it is essential to make sure that seal chambers, auxiliary shaft seal systems and any heating and cooling systems are properly filled.
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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.
PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
®
To avoid potential explosion hazards during maintenance, the tools, cleaning and painting materials used must not give rise to sparking or adversely affect the ambient conditions. Where there is a risk from such tools or materials, maintenance must be conducted in a safe area.
It is recommended that a maintenance plan and schedule is adopted. (See section 6, Maintenance.)

1.7 Nameplate and warning labels

1.7.1 Nameplate

For details of nameplate, see the Declaration of Conformity.

1.7.2 Warning labels

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PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
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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.

1.9 Noise level

When pump noise level exceeds 85 dBA attention 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 dBA. In such situations consideration must be given to the fitting of an acoustic enclosure to meet local regulations.
Pump noise level is dependent on a number of factors ­the type of motor fitted, the operati ng cap acit y, pipework design and acoustic characteri stics of the buildin g. Typical sound pressure levels measured in dB, and A-weighted are shown in the t able below (L
). The
pfA
figures are indicative only, they are subject to a +3 dB tolerance, and cannot be guaranteed.
The values are based on the noisiest electric motors that are likely to be encountered. They represent sound pressure levels at 1 m (3.3 ft) from the directly driven pump, for "free field over a reflecting plane".
If a pump unit 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 the combined calculation.
For units driven by equipment other than electric
motors or units contained within enclosures, see the accompanying information sheets and manuals.
Typical sound pressure level, dBA (LpA at 1 m reference 20µPa)
Motor size and speed
KW (hp)
2.2 (3) 78 72 71 68 71 68 68 68 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 77 83 73 76 73 72 71
7.5 (10) 90 78 83 74 77 74 73 72
11 (15) 91 80 84 76 78 76 74 73 15 (20) 92 83 85 79 80 79 76 75
18.5 (25) 92 83 85 79 80 79 76 75 22 (30) 92 83 85 79 81 79 77 75 30 (40) 100 85 93 81 84 80 80 76 37 (50) 100 86 93 82 84 80 80 76 45 (60) 100 87 93 83 84 80 80 76 55 (75) 102 88 95 84 86 81 82 77 75 (100) 100 90 95 86 88 81 83 78 90 (120) 100 90 95 86 90 81 85 78
110 (150) 100 91 95 87 91 83 86 79 150 (200) 101 92 96 88 91 83 86 79 200 (270)
300 (400) - - - -
3550 r/min 2900 r/min 1750 r/min 1450 r/min
Pump and
motor
dBA
Pump
only
dBA
Pump and
motor
dBA
Pump
only
dBA
Pump and
motor
dBA
Pump
only
dBA
83 84
Pump and
motor
dBA
← ←
Pump
only
dBA
80 81
Motors in this range are generally job specific and noise levels should be calculated based on actual equipment installed.
For 960 rpm reduce 1450 rpm values by 5 dBA.
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PVML USER INSTRUCTIONS ENGLISH 00079591 – 01/05
®

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 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.
Typical lifting of a PVML with base plate or extended levelling plate

2.2 Handling

Boxes, crates, pallets or cartons may be unloaded using fork-lift vehicles or slings dependent on their size and construction.

2.3 Lifting

To avoid distortion, the pump unit
should be lifted as shown.
A crane must be used for all pump sets in excess of 25 kg (55 lb). Fully trained personnel must carry out lifting, in accordance with local regulations. The driver and pump weights are recorded on their respective nameplates.
Unsafe lifting is never allowed!

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.
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 that are harmful to the
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