Flowserve QLQ User Manual

USER INSTRUCTIONS
®
Worthington centrifugal pumps
Vertical QLQ and QLQC
Installation
multiple stage, double suction, vertical wet pit and canned centrifugal pumps
PCN=87900027 – 06/14 (E ) Original instructions
Maintenance
These instructions must be read prior to installing,
operating, using and maintaining this equipment.
QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
CONTENTS:
PAGE
1 INTRODUCTION AND SAFETY ........................... 4
1.1 General ........................................... ................ 4
1.2 CE marking and approvals .............................. 4
1.3 Disclaimer ....................................................... 4
1.4 Copyright ........................................................ . 4
1.5 Duty conditions............................ .................... 4
1.6 Safety .............................................................. 5
1.7 Nameplate and safety labels ........................... 8
1.8 Specific machine performance .................... .... 8
1.9 Noise level ........................ ............................... 9
2 TRANSPORT AND STORAGE ........................... 10
2.1 Consignment receipt and unpacking ............ 10
2.2 Handling ........................................................ 10
2.3 Lifting ............................................................. 10
2.4 Storage ................................................ .......... 12
2.5 Recycling and end of product life .................. 14
3 PUMP DESCRIPTION ......................................... 15
3.1 Configurations ............................................... 15
3.2 Nomenclature ................................................ 15
3.3 Design of major parts .................................... 16
3.4 Performance and operating limits ................. 18
6 MAINTENANCE ................................................... 42
6.1 Maintenance schedule ...................................42
6.2 Spare parts ....................................................44
6.4 Tools required ................................................44
6.5 Fastener torque .............................................44
6.6 Setting impeller clearance .............................45
6.7 Disassembly ..................................................45
6.8 Examination of parts .......................... ... .... .... .46
6.9 Reassemble procedure .................................50
7 FAULTS; CAUSES AND REMEDIES ................... 52
8 PARTS LIST AND DRAWINGS ............................ 54
PAGE
4 INSTALLATION .................................................... 19
4.1 Location ......... ................................................ 19
4.2 Part assemblies............................................. 23
4.3 Foundation .................................................... 23
4.4 Grouting ........................................................ 25
4.5 Initial alignment ............................................. 26
4.6 Piping ............................................................ 28
4.7 Electrical connections ................................. .. 30
4.8 Protection systems ........................................ 30
5 COMMISSIONING, STARTUP, OPERATION AND
SHUTDOWN ................................... ......................... 32
5.1 Pre-commissioning procedure ...................... 32
5.2 Pump Lubricants ........................................... 32
5.3 Lubrication of thrust bearing ......................... 33
5.4 Impeller adjustment ....................................... 34
5.5 Direction of rotation ....................................... 36
5.6 Guarding ....................................................... 36
5.7 Priming and auxiliary supplies ............ .... .... .. 36
5.8 Starting the pump .......................................... 36
5.9 Running or operation .................................... 39
5.10 Stopping and shutdown .............................. 40
5.11 Hydraulic, mechanical and electrical duty ... 40
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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
INDEX:
PAGE
Alignment (4.5) .................................................. ...... 25
Assembly (6.9) ......................................................... 49
ATEX marking (1.6.4.2) ............................................. 7
CE marking and approvals (1.2) ................................ 4
Clearances (6.6) ................................................ ...... 44
Commissioning and operation (5) ............................ 31
Compliance, ATEX (1.6.4.1) ...................................... 6
Configurations (3.1) ........................................... ...... 15
Copyright (1.4) ........................................................... 4
Design of major parts (3.3) ...................................... 16
Direction of rotation (5.5) ......................................... 35
Disassembly (6.7) ............................... ..................... 44
Disclaimer (1.3) .......................................................... 4
Dismantling (see 6.7, Disassembly) ........................ 44
Drawings (8) .................... .... .... ... .... .... .... ....... .... .... .. 55
Duty conditions (1.5) .................................................. 4
Electrical connections (4.7) ....................... .............. 29
End of product life (2.5) ........................................... 14
Examination of parts (6.8) ....................................... 45
Fastener torques (6.5) ............................................. 43
Faults; causes and remedies (7) ............................. 51
General assembly drawings (8.1) ............................ 53
Grouting (4.4) ............................................. .............. 25
Guarding (5.6) .................................................... ...... 35
Handling (2.2) .......................................................... 10
Hydraulic, mechanical and electrical duty (5.10) ..... 39
Impeller clearance (6.6) ........................................... 44
Inspection (see 6.1, Maintenance schedule) ........... 41
Installation (4) .......................................................... 19
Lifting (2.3) ............................................................... 10
Location (4.1) ........................................................... 19
Lubrication, thrust bearings (5.3) ............................. 33
Lubrication, pump (see 5.2, Pump lubricants) ......... 31
Maintenance (6) ....................................................... 41
Maintenance schedule (6.1) .................................... 41
Name nomenclature (3.2) ........................................ 15
Nameplate (1.7.1) ................................... ... .... .... .... ... . 8
Operating limits (3.4) ....... .... .... ... .... .... ....... .... .... .... .. 18
Ordering spare parts (6.2.1) .................................... 43
Part assemblies (4.2) ............................................... 23
Parts lists (8) ............................................................ 53
Performance (3.4) .................................................... 18
Piping (4.6) .............. ................................................ 27
Pre-commissioning (5.1) .......................................... 31
Protection systems (4.8) .......................................... 30
Priming and auxiliary supplies (5.7) ......................... 35
Reassembly (see 6.9, Assembly) ............................ 49
Receipt and unpacking (2.1) .................................... 10
Recommended oil lubricants (5.2.2) ........................ 31
Recommended spares (6.3) .................................... 43
Recycling (2.5) ......................................................... 14
Replacement parts (see 6.2 and 6.3) ...................... 43
Running and operation (5.9) .................................... 38
PAGE
Safety action (1.6.3) ................................................... 5
Safety labels (1.7.2) ... ................................................ 8
Safety markings (1.6.1) .............................................. 5
Safety, protection systems ....................................... 30
Sectional drawings (8) .............................................. 53
Sound level (see 1.9, Noise level) .............................. 8
Spare parts (6.2) ................... .... ....... .... .... .... ... .... .... . 43
Specific machine performance (1.8) .......................... 8
Starting the pump (5.8) ............................................ 35
Stop/start frequency (5.8.8) ...................................... 38
Stopping and shutdown (5.10) ................................. 39
Storage, pump (2.4) ................................................. 12
Storage, spare parts (6.2.2) ..................................... 43
Supplementary manuals or info, contacts ................ 60
Tools required (6.4) .................................................. 43
Torques for fasteners (6.5) ....................................... 43
Trouble-shooting (see 7) .......................................... 51
Vibration (5.8.7) ........................................................ 38
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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
1 INTRODUCTION AND SAFETY
1.1 General
These instructions must always be kept
close to the product's operating location or directly with the product.
Flowserve products are designed, developed and manufactured with state-of-the-art technologies in modern facilities. The unit is produced with great care and commitment to continuous quality control, utilizing sophisticated quality techniques and safety requirements.
Flowserve is committed to continuous quality improvement and being at service for any further information about the product in its installation and operation or about its support products, repair and diagnostic services.
These instructions are intended to facilitate familiarization with the product and its permitted use. Operating the product in compliance with these instructions is important to help ensure reliability in service and avoid risks. The instructions may not take into account local regulations; ensure such regulations are observed by all, including those installing the product. Always coordinate repair activity with operations personnel, and follow all plant safety requirements and applicable safety and health laws and regulations.
These instructions must be read prior to
installing, operating, using and maintaining the equipment in any region worldwide. The equipment must not be put into service until all the conditions relating to safety noted in the instructions, have been met. Failure to follow and apply the present user instructions is considered to be misuse. Personal injury, product damage, delay or failure caused by misuse are not covered by the Flowserve warranty.
1.2 CE marking and approvals
It is a legal requirement that machinery and equipment put into service within 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 complete and reliable. However, in spite of all the efforts of Flowserve Corporation to provide comprehensive instructions, good engineering and safety practice should always be used..
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 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 authorized Flowserve parts and accessories is considered to be misuse. Damage or failure caused by misuse is not covered by the Flowserve warranty. In addition, any modification of Flowserve products or removal of original components may impair the safety of these products in their use.
1.4 Copyright
All rights reserved. No part of these instructions may be reproduced, stored in a retrieval system or transmitted in any form or by any means without prior permission of Flowserve.
1.5 Duty conditions
This product has been selected to meet the specifications of your purchaser order. The acknowledgement of these conditions has been sent separately to the Purchaser. A copy should be kept with these instructions.
The product must not be operated beyond
the parameters specified for the application. If there is any doubt as to the suitability of the product for the application intended, contact Flowserve for advice, quoting the serial number.
If the conditions of service on your purchase order are going to be changed (for example liquid pumped, temperature or duty) it is requested that the user
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seeks the written agreement of Flowserve before start up.
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 spec ific safety m arkings 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 indica te s “ha zar do us an d to xic fluid ” safety instructions where non-compliance would affect personal safe ty 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 symbol is used in safety instructions to remind not to rub non-metallic surfaces with a dry cloth; ensure the cloth is damp. It is used in safety instructions where non-compliance in the hazardous area would cause the risk of an explosion.
This sign is not a safety symbol but indicates
an important ins t ructi on i n t he as sem bly pr oce ss.
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 operatio ns 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.
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, d ue to in tern al pressure, acts on the pump flange.
ENSURE CORRECT LUBRICATION (See section 5, Commissioning, startup, operation and shutdown.)
START THE PUMP WITH OUTLET V ALVE PARTL Y 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 startup, 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 backpressure 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.
NEVER DO MAINTENANCE WORK
WHEN THE UNIT IS CONNECTED TO POWER
HAZARDOUS LIQUIDS When the pump is handling hazardous liquids care must be taken to avoid exposure to the liquid by appropriate siting of the pump, limiting personnel
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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 pump ing hazardous liquids.
DRAIN THE PUMP AND ISOLATE PIPEWORK BEFORE DISMANTLING THE PUMP The appropriate safety precautions should be taken where the pumped liquids are hazardo u s .
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.
GUARDS MUST NOT BE REMOVED WHILE THE PUMP IS OPERATI ONAL The unit must not be operated unless coupling guard is in place. Failure to observe this warning could result in injury to operating personnel.
THERMAL SHOCK Rapid changes in the temperature of the liquid within the pump can cause thermal shock that can result in damage or breakage of components and should be avoided.
APPL YING HEAT TO REMOVE IMPELLER There may be occasions when the impeller has become difficult to remove due to products that are corrosive in nature. If you elect to use heat to remove the impeller, it must be applied with great care and before app lying heat, ensure any residual hazardous liquid trapped between the impeller and pump shaft is thoroughly drained out through the impeller keyway to prevent an explosion or emission of toxic vapor. Impeller design varies and so are the heat, applying location and the duration of heat application. Contact nearest Flowserve Service Center for help.
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 m ust 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 80 °C (175 °F) or below -5 °C (20 °F) in a restricted zone, or exceeds local regulations, action as above shall be taken.
1.6.4 Products used in potentially explosive atmospheres
The following instructions for pumps and pump units when installed in potentially explosive atmospheres must be followed to help ensure explosion protection. For ATEX both electrical and non-electrical equipment must meet the requirements of European Directive 94/9/EC. Always observe the regional legal Ex requirements eg Ex electrical items outside the EU may be required certified to other than ATEX eg IECEx, UL.
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
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 ATEX pump set shall select the coupling , 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 the ATEX Certification for the motor shall 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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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
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 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 Pumps have a temperature class as stated in the 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 liquid handled. The maximum permissible liquid temperature depends on the ATEX temperature class and must not exceed the values in the table that follows.
Temperature
class to
EN13463-1
T6
T5 T4 T3 T2 T1
*The table only takes the ATEX temperature class into consideration. Pump design or material, as well as component design or material, may further limit the maximum working temperature of the liquid.
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
Consult Flowserve
Consult Flowserve
115 °C (239 °F) * 180 °C (356 °F) * 275 °C (527 °F) * 400 °C (752 °F) *
The temperature rise at the seals and bearings due to the minimum permitted flow rate is taken into account in the temperatures stated.
The responsibility for compliance with the specified maximum liqu id temperature is with the plant operator.
Temperature classification “Tx” is used when the liquid temperature varies and when the pump is required to be used in differently classified potentially explosive atmospheres. In this case the user is responsible for ensuring that the pump surface temperature does not exceed that permitted in its actual installed location.
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, users shall fit an external surface temperature protection device.
Avoid mechanical, hydraulic or electrical overload by using motor overload trips, temperature monitor or a power monitor. Make routine vibration measurements. In dirty or dusty environments, regular checks shall be made and dirt removed from areas around close clearances, bearing housings and motors.
1.6.4.4 Preventing the build up of explosive mixtures
ENSURE THE PUMP IS PROPERLY FILLED AND VENTED AND DOES NOT RUN DRY Ensure the pump and relevant suction and discharge pipeline system is completely filled with liquid at all times during the pump operation, so that an explosive atmosphere is prevented. In addition, it is essential to make sure that seal chambers, auxiliary shaft seal systems and any heating and cooling systems are properly filled.
If the operation of the system cannot avoid this condition, user shall fit an appropriate dry run protection device (eg. liquid detection or a power monitor).
To avoid potential hazards from fugitive emissions of vapor or gas to the atm osphere the surr ounding area shall be well ventilated.
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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
1.6.4.5 Preventing sparks
To prevent a potential hazard from mechanical contact, the coupling guard must be non-sparking and anti-static for Category 2.
To avoid the potential hazard from random induced current generating a spark, the baseplate shall be properly grounded.
Avoid electrostatic charge: do not rub non-metallic surfaces with a dry cloth; ensure cloth is damp.
For ATEX the coupling must be selected to comply with 94/9/EC and correct alignment must be maintained.
1.6.4.6 Preventing leakage
The pump shall only be used to h andle 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 shall be monitored.
If leakage of liquid to atmosphere can result in a hazard, users shall install a liquid detection device.
1.6.4.7 Maintenance to avoid the hazard
It is recommended that a maintenance plan and schedule is adopted. See section 6.
1.7 Nameplate and safety labels
1.7.1 Nameplate
For details of nameplate, see the Declaration of Conformity.
1.7.2 Safety labels
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.
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1.8 Specific machine performance
For performance parameters see section 1.5, Duty conditions. Pump performance data are summarized
on pump data sheet which is included in proper section of “Job User’s Instruct ion”.
QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
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 80 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 operating conditions, pipework design and acoustic characteristics of the building.
Typical sound pressure levels measured in dB and A-weighted are shown in the table in section 1.9.1. The figures are indicative only; they are subjected to a +3 dB tolerance and cannot be guaranteed.
The dBA values are based on the noisiest ungeared electric motors that are likely to be encountered. The third column table shows 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 should be combined with the level for the driver obtained from the supplier. Consult a Noise Specialist for the combined calculation.
If the motor is driven by an inverter, it may show an increase in noise level at some speeds.
1.9.1 Typical vertical motor noise data (Hollow and solid shafts)
Motor
Frame
Size.
NEMA
180
210
250
280
320
360
400
440
449
5000
5800
6800
8000
RPM
3600 70.0 78.0 1800 60.0 68.0
1200 & slower 55.0 63.0
3600 70.0 78.2 1800 60.0 68.2
1200 & slower 55.0 63.2
3600 75.0 83.4 1800 70.0 78.4
1200 & slower 60.0 68.4
3600 75.0 83.8 1800 70.0 78.8
1200 & slower 60.0 68.8
3600 75.0 84.0 1800 65.0 74.0
1200 & slower 65.0 74.0
3600 75.0 84.2 1800 65.0 74.2
1200 & slower 65.0 74.2
3600 80.0 89.5 1800 70.0 79.5
1200 & slower 65.0 74.5
3600 80.0 90.0 1800 70.0 80.0
1200 & slower 70.0 80.0
1800 85.0 97.8
1200 & slower 80.0 92.8
3600 90.0 102.8 1800 85.0 97.8
1200 & slower 80.0 92.8
3600 90.0 103.7 1800 90.0 103.7
1200 & slower 80.0 93.7
1800 90.0 103.9
1200 & slower 85.0 98.8
1800 90.0 104.7
1200 & slower 85.0 99.7
Sound
Pressure
(dBA )
Sound Power (dBA )
For units driven by equipment other than
electric motors or units contained within enclosures, see the accompanying information sheets and manuals.
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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
2 TRANSPORT AND STORAGE
2.1 Consignment receipt and unpacking
Immediately after receipt of the equipment, it must be checked against the delivery and shipping documents for its completeness and that there has been no damage in transportation.
Any shortage and or damage must be reported immediately to Flowserve Pump Division and received in writing within one month of receipt of the equipment. Later claims cannot be accepted.
Check any crate, boxes and wrappings for any accessories or spare parts that may be packed separately with the equipment or attached to sidewalls of the box or equipment.
Each product has a unique serial number. Check that this number corresponds with that advised and always quote this number in correspondence as well as when ordering spare parts or further accessories.
2.2 Handling
Boxes, crates, pallets or cartons may be unloaded using forklift vehicles or slings dependent on their size and construction.
2.3 Lifting
For pumps supplied with two piece head shaft or solid shaft drivers, proceed with the lifting as explained in
2.3.1. Flowserve will not supply eyebolts neither fixed nor
separately with the pump. It is the responsibility of the installer to arrange appropriate hardware that can handle the weights and results in safe and successfu l installation.
2.3.1 Lifting of fabricated discharge heads with or without the pump
If the pump is supplied with a fabricated discharge head use the 4 points method of lifting as shown in the details provided below or 2 points method using a lifting beam. This method is applicable to the lifting of the discharge head with or without the pump assembled.
For pump supplied with motor stand already assembled on the discharge head, the motor stand lifting points shall not be used for lifting. Lift the pump using a lifting beam and two of the four discharge head lifting points.
Example: Lifting of discharge head
To avoid distortion, the pump unit should be lifted by using lifting equipment certified to local standards.
The pumps are generally very heavy therefore, size/shape factors will have to be considered before attempting to lift them. It is strongly recommended to attempt lifting from a safe distance to prevent any injury or loss of life. Consulting with experts is recommended.
A crane must be used for all pump sets and components in excess of 25 kg (55 lb.). Fully trained personnel must carry out lifting, in accordance with local regulations. If you are not sure about the driver and pump weights contact Flowserve for information.
Pump heads may be shipped with the seal housing installed. For ease of assembly and to prevent damage, we recommend removing the housing before putting the head on the pump.
For pumps supplied with hollow shaft drivers and one-piece head shaft, attach head shaft to the lineshaft with a coupling and tighten first.
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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
2.3.2 Lifting of bowl assembly only
Clamp the bowl assembly and center the lifting hook for lifting and lowering the assembly into the sump/suction barrel.
a) Lower the bowl assembly until the clamp
extensions rest on the foundation (use appropriate supports).
b) Build the very first section of the column piping,
and lower the entire assembly to assemble the next column section.
c) Continue to build until it is ready for discharge
head assembly. d) Install the discharge head. e) Assemble the motor.
Example: Lifting of bowl assembly
2.3.3 Lifting of the motor stand only
Motor stand shall be lifted using the four lifting points foreseen on the motor stand itself.
The four motor stand lifting points shall not be
used for the lift of the assembled pump. Example: Lifting of motor stand
2.3.4 Lifting of suction barrel
Suction barrel (also referred as ‘Can’) is always supplied separately and has to be installed into the sump first. Install eyebolts on the flange of the suction barrel and attach slings and straps to bring the suction barrel to a vertical position. Move the barrel for installation. Provide hand support to prevent the suction barrel from swaying during movement.
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QLQ, QLQC USER INSTRUCTIONS ENGLISH 87900027 – 06/14
Example: Lifting of suction barrel
SUCTION BARREL (CAN)
2.3.5 Lifting of fully assembled pumps
If the pump is fully assembled, it has to be adequately strapped and supported at least two places before it can be lifted from the shipping crate and moved to the installation site. See details shown. Same rules are applicable when the pump is pulled out from the sump and moved to another locatio n.
Examples shown here are for illustration only. See section 2.3 1~2.3.4 for specific lifting instructions based on design variations. The pumps vary in weight, length and physical appearances from the types shown here. Therefore, before lifting is attempted, exercise caution to pr event any injuries or loss of life.
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 the pump at frequent intervals (refer to section 2.4.1.2) to prevent brinelling of the bearings and the seal faces, if fitted, from sticking. Electric Motors (Pump Driver) should not be stored in damp places without special protection (Refer to Motor manufacturers instructions).
The pump may be stored as above for up to 6 months.
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2.4.1 Long term storage
During extended periods of storage prior to installation, precautions must be taken to protect the pump from deterioration. The various parts of the pump are protected prior to shipment by applying varying grades of preservative to the parts. However, during shipment and handling the preservatives are subjected to conditions that can cause their removal. Also, during extended periods of time the preservatives may deteriorate. The listed procedures (2.4.1.1 to 2.4.1.5) should be followed to prevent deterioration of the pump during the extended storage period. These procedures may also be supplemented by the experience of the person(s) performing the tasks.
2.4.1.1 Inspection upon arrival
When the pump is received it should be inspected for damage or other signs of rough handling. If any damage is found it should be reported to the carrier immediately. Inspect the preservative coating on various parts. If necessary, renew preservative in areas where it has been rubbed or scraped. Inspect all painted surfaces. If necessary, touch up the areas where paint has been chipped or scraped. Inspect all covers over pump openings and piping connections. If covers or seals for the covers are damaged or loose, they are to be removed, and a visual inspection made of the accessible interior areas for accumulation of foreign materials or water. If necessary, clean and preserve the interior parts as noted above to restore the parts to the "as shipped" condition. Install or replace covers and fasten securely.
2.4.1.2 Storage
component parts should be stored indoors where they will be protected from the elements. In no case should any pump element be subjected to exte nded periods of submergence or wetting prior to start up. If it is not possible to store the pump and its components indoors, precautions must be taken to protect them from the elements. Regardless of whether storage is indoors or outside, the storage area should be vibration free. All boxes marked for indoor storage should be stored indoors. When stored outdoors the pump and its components should be protected from dirt, dust, rain, snow, or other unfavorable conditions by heavy plastic sheets, canvas, waterproof burlap or other suitable coverings. All equipment must be placed upon skids or blocks to prevent contact with the ground and surface contaminants. Equipment must be adequately supported to prevent distortion and bending.
If at all possible, the pump and its
The pump shaft should be rotated, in the direction of rotation, at least 1 and 1/4 turn monthly during the storage period and any other period s of s tandby. When selecting a storage area the following should be taken into consideration.
a) The deterioration of the equipment will be
proportionate to the class of stor age provided.
b) The expenses involved in restoring the
equipment at time of installation will be proportionate to the class of stor age provided.
2.4.1.3 Inspection and maintenance
The stored equipment has to be placed on a periodic inspection schedule by the purchaser. The responsibility for setting up an inspection schedule rests with the purchaser and will be dependent upon the class of storage provided. It would be expected initially, inspection would occur weekly, then depending upon the inspection reports being favorable or unfavorable, inspection would continue weekly, monthly, or quarterly, as may be determined. Each inspection should consist of a general surface inspection to assure that:
a) Pump supports are firmly in place. b) Pump covers over openings are firmly in place. c) Pump coverings, plastic or tarps are firmly in
place. Any holes or tears must be repaired to prevent entrance of dirt or water.
d) Pump covers are periodically removed from
openings and interior accessible areas inspected. If surface rusting has occurred, clean or coat with preservative.
e) If rusting occurs on exterior surfaces clean and
repaint or coat with preservative.
f) Check individually wrapped parts for signs of
deterioration. If necessary, renew preservative and wrapping.
Six months prior to the scheduled installation date, a FLOWSERVE representative is to be employed to conduct an inspection. This inspection may include, not necessarily in its entirety and not limited to the following:
a) An inspection of all periodic inspection records as
kept on file by the purchaser, and all inspection reports that have been compiled during the storage period.
b) An inspection of the storage area to determine
the "as stored" condition of the equipment prior to any protection covers being removed.
c) An inspection of the equipment with protective
covers and flange covers removed.
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d) Depending upon the length of time the equipment
was stored, the type of storage provided (i.e. Indoor: heated, unheated, ground floor, concrete floor. Outdoors: under roof, no roof, waterproof coverings, on concrete, on ground) and as a result of the inspection of (a),( b) & (c) above the FLOWSERVE representative may require a partial or complete dismantling of the equip m ent.
e) Dismantling may necessitate restoration of
painted or preserved surfaces, and, or replacement of gaskets, "O" rings, packing and bearings.
f) All costs involved during inspection, dismantling,
restoration, replacement of parts and reassembly will have to the accounted to the purchaser. All necessary labour, tools and cranes will be supplied by the purchaser.
Upon completion of the inspection the FLOWSERVE representative shall submit a report to the purchaser, and to the Manager of Customer Service, stating in detail the results of the inspection. One month prior to installation of the equipment, a FLOWSERVE representative is to be employed to conduct a final inspection. This inspection will be made to assure that the requirements of the six months inspection report were satisfactorily completed and that the equipment is ready for installation. Upon completion of this inspection the FLOWSERVE representative shall submit a final report to the purchaser, and to the Manager of Customer Service, advising the results of the final inspection. All costs involved in conducting the final inspection will have to the accounted to the purchaser. Prior to and during start up, any requireme nts for the services of an FLOWSERVE representative will revert back to the original contract agreement for equipment purchased, with revised costing.
2.4.1.4 Delay in th e startup
Startup of the pumps, after installation on the plant, should be executed within two months as a maximum. In case, for any reason, the period between installation and startup should exceed the two months, the following precautions must be taken:
a) If acid descaling are foreseen on the plant, the
pump must be by-passed during these operations, or, otherwise, shall be fully disassembled, washed with basic solution, dried and reassembled. All these operations shall be executed by Flowserve personnel or under Flowserve supervision.
b) It is advisable, for a long term permanence on the
plant before startup, that blind flanges are interposed between the pump nozzles and the relevant pipe, to avoid the possibility that foreign material can be introduced into the pump. In case such flange s not installed, it is advisable that the inner parts of the pumps is carefully inspected (by disassembling, if necessary) to verify the absence of foreign material before the startup.
c) During the period between installation and
startup the same maintenance checks described in point 2.4.1.3 shall be carried out.
2.4.1.5 Painting and preservation
Paints and preservatives used are either FLOWSERVE standard or 'special' as required by the contract specification. Refer to FLOWSERVE for the description of paints and preservatives used on this order if needed.
2.4.1.6 Associated equipment
Motors, Turbines, Gears, etc., being supplied by FLOWSERVE. Generally rotors of associated equipment should be blocked to relieve bearing loads. Storage should be indoors and dry. See the specific manufacturers storage requirements.
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 using an environmentally acceptable method and in accordance with local regulations. If the product contains substances which are harmful to the environment, these should be removed and disposed 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.
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3 PUMP DESCRIPTION
Should questions arise concerning the pump, Flowserve pump division will require the complete serial number to be of assistance. The serial number is stamped on a metal nameplate affixed to the discharge head assembly. The driver will have a separate nameplate attached to it. If you are requesting information on the driver, please provide both the driver serial number and the pump serial number to Flowserve representative.
3.1 Configurations
QLQs, are engineered pumps as: (a) Wet pit (sump) type (b) Double casing (can) type pumps. Most pumps are built with customer specific features and for applications such as water pumpin g stations, storm water service, industrial, O & G, power applications. The pumps vary in size, impeller types and length, whether it is an open shaft or enclosed shaft designs and type of discharge head used.
3.1.1 Wet Pit (sump) Type QLQ
3.1.2 Suction barrel (Can) QLQC
3.2 Nomenclature
The pump size/ serial number will be engraved on the nameplate typically as below: The nameplate is attached to the discharge head assembly.
3.2.1 Bowl assembly nomenclature
12 QLQ 18 / 45 / 4
Nominal Bowl Discharge flange inches
Bowl Model QLQ First Stage Impeller
Nominal Dia. – inches Additional Stages Model Total Number of Stages
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The typical nomenclature above is the general guide to the QLQ configuration description. Identify the actual pump size and serial number from the pump nameplate. The driver will have a separate nameplate attached it.
3.3 Design of major parts
3.3.1 Case assembly
Case assembly is designed to operate completely submerged in the liquid. It consists of suction bells, first and additional stages bowls, impellers and pump shaft. The suction bells serve as the input- ports to the first stage impeller. Internal vanes support the housing of the suction bell bearing. The first stage casing is made of lower and upper bell-mouth with bearing, double volute and discharge branches with bearing. Twin volute is made efficiently to convert to pressure the velocity added to the liquid by the impeller. Additional stage casings are diffuser type.
3.3.2 Impellers
QLQs are supplied with enclosed, double suction fist stage impeller types, while additional stages impellers are single suction. Impellers are low, medium and high capacity type designed for maximum coverage of all QLQ applications. Impellers are cast and machined to match each order and to provide required surface finish to achieve hydraulic characteristics. Impellers are dynamically balanced and held in position on the shaft by key and locking nut.
3.3.3 Column assembly
The column assembly con sists of column pipe, which connects the bowl assembly to the discharge head and carries the pumped fluid to the discharge head. Houses and supports the shaft and may contain bearings. Typical column assemblies are flanged, with integrated bearing support.
The column supports shaft assembly, that is either a) Open lineshaft construction utilizing the fluid being
pumped to lubricate the lineshaft bearings. or b) Enclosed lineshaft construction has an enclosing
tube around the lineshaft and utilizes oil or other
clean fluid to lubricate the lineshaft bearings. The shafts are key coupled with thrust stud design or
clamp ring design.
The column shaft is usually divided in more sections to facilitate the assembly during installation and maintenance. See sectional drawings supplied with the pump for exact column assembly details as per the order. The size and configuration vary depending upon the specific order requirements and application criteria
3.3.4 Suction strainers
Wet Pit (sump) QLQs can also be fitted with strainers to prevent foreign particles from entering the pump. The type of strainers and the mesh size depends on the application. An example is shown below. Strainers are usually fastened directly to the suction bells .
3.3.5 Suction Can
Suction can is designed to allow the impeller to have the proper level of NPSH to run properly, when the available NPSH is insufficient at ground level. It's connected with the Suction Head, and can be directly installed on the foundations or through a separate foundation plate, According to the specification, it can be designed to withstand the maximum Suction Pressure or to withstand the Maximum Allowable Working Pressure. Consult the dedicated pump document for more details on it.
3.3.6 Discharge Head Assembly
The discharge head supports the driver and bowl assembly as well as supplying a discharge connection in most cases. A shaft sealing arrangement is located in the discharge head to seal the shaft at its exit from the liquid chamber. The shaft seal will usually be either a mechanical seal assembly or packing seal with an open lineshaft or a tube-packing box with an enclosed lineshaft.
If the pump is required to have its own thrust bearing , it is installed in the discharge head has the pump thrust bearing integrated. The different types of discharge heads can be summarized in two types.
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3.3.6.1 Head for Wet pit (sump) pumps
The head has the suction nozzle and the thrust bearing (if installed in the pump) integrated. The head is fixed to the ground by means of a foundation plate or by fou ndation beams on which the head is placed.
3.3.6.2 Head for double casing (can) pumps
The head has the suction nozzle, the discharge nozzle, the thrust bearing (if installed on the pump) integrated. The head is connected to the suction barrel (can) through a flange; the head can have provisions to be fixed directly to the ground or to be fixed on a separate foundation plate. For special layouts the suction nozzle can be placed below the mounting level (refer to the dedicated General Arrangement drawing for reference).
3.3.7 Motor Stool
The motor stool is a fabricated steel structure designed to maintain the proper alignment between pump and electric motor. It can be integrated with the pump head or it can be a separate piece fixed upon the suction head.
3.3.8 Drivers
A variety of drivers may be used, however, electric motors are most common. For the purposes of this manual, all types of drivers can be grouped into two categories.
a) Hollo w shaft drivers: where the head shaft extends through a tube in the center of the rotor and is connected to the driver by a clutch assembly at the top of the driver.
b) Solid shaft drivers: where the rotor shaft is solid and projects below the driver-mounting base. This type driver requires an adjustable coupling for connecting to the pump.
3.3.9 Stuffing box
QLQs are fitted with stuffing boxes which are adequate for the pump working pressure. Stuffing boxes may fit a mechanical or packing seal.
3.3.10 Mechanical shaft seal
QLQs can be fitted with single or double mechanical seal. Depending on the services specified, the mechanical seal has different plan to provide the proper flushing to the faces trough appropriate piping either installed on the pump or to be provided and mounted when the pump is installed.
3.3.11 Thrust Bearing (if installed)
The pump shall be equipped with a thrust bearing installed in the suction head (alternatively, the thrust bearing of the driver can be designed to withstand the thrusts of the pump). The thrust bearing is designed to withstand the axial loads (static weights of rotors and hydraulic loads) occurring throughout the pump operating range. The thrust bearings can be ball type, roller type or tilting pad. The bearings are housed in a fabricated steel support directly mounted on the upper side of the discharge head. Lubrication of the thrust bearings is provided by oil bath. As standard option, an oil sight glass in installed outside the bearing house to check oil level and refilling.
3.3.12 Flexible coupling with spacer (if installed)
If the pump is equipped with thrust bearing, the pump shaft is joined to the driver shaft with a flexible coupling with spacer. The flexible coupling allow the transmission of the torque to the pump, but not the axial loads.
3.3.13 Rigid Coupling with spacer between mechanical seal and bearing support (if installed)
If the pump is equipped with mechanical seal and thrust bearing, a rigid coupling with spacer is placed between the thrust bearing and the mechanical seal. By the removal of the coupling hub and the spacer only the removal of the mechanical seal is without the
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need to dismantle the thrust bearing, simplifying the maintenance operations.
3.3.14 Rigid coupling between motor and pump (if installed)
If the pump is not equipped with the thrust bearing, a rigid coupling provides the torque and the axial load transmission between pum p and driver.
3.3.15 Accessories
Accessories (instrumentation, special flushing plans) may be fitted when specified by the customer.
3.4 Performance and operating limits
This product has been selected to meet the specifications of your purchase order, see section
1.5. These pumps are furnished for a particular service
condition. Changes in the hydraulic system may affect the pump's performance adversely. This is especially true if the changes reduce the pressur e at the suction flange or if the liquid temperature is increased. In case of doubt, contact the nearest FLOWSERVE office.
3.4.1 Operating limits
Pumped liquid temperature limits*
Maximum ambient temperature*
Maximum pump speed refer to the nameplate
-45 ºC (-50 ºF) to +205 ºC (400 ºF)
Up to +55 ºC (130 ºF)
*Subject to written agreement from Flowserve. Special designs and materials may be available for pumps operating above and below these specified limits. Contact Flowserve for upgrade options available for your specific application.
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4 INSTALLATION
Equipment operated in hazardous locations must comply with the relevant explosion protection regulations. See section 1.6.4, products used in potentially explosive atmospheres.
Six months prior to the scheduled installation date, a Flowserve Pump Division representative is to be employed to conduct an inspection of the equipment and the facility. If any deterioration of equipment is noticed, the Flowserve Pump Division representative may require a partial or complete dismantling of the equipment including restoration and replacement of some components.
4.1 Location
The pump should be located to allow room for access, ventilation, maintenance and inspection with ample headroom for lifting and should be as close as practicable to the supply of liquid to be pumped.
4.1.1 General installation check-list
The following checks should be made before starting actual installation.
a) Make sure that motor nameplate ratings and the
power supply system match correctly.
b) Check the sump depth and pump length match-
up. c) Check the liquid level in the sump. d) Check the installation equipment to be sure that
it will safely handle the pump weight and size. e) Check all pump connections (bolts, nuts etc.) for
any shipping and handling related problems.
Apply thread lubricant sparingly to male shaft threads only at the time of making up shaft connection. Excess lubricant should be avoided.
4.1.2 General installation instructions
As standard option the pumps are shipped with the suction bowl, column and suction head fully assembled and the suction barrel (if is supplied) shipped separately.
4.1.2.1 Lifting
See lifting methods in section 2.3.
4.1.2.2 Equipment and tools required for installation of a fully assembled pump
a) Mobile crane capable of hoisting and lowering the
entire weight of the pump and motor.
b)
Cable sling for attaching to the pump and motor lifting eyes.
c)
Ordinary hand tools: Pipe wrenches, end wrenches, socket set, screwdrivers, Allen wrenches, wire brush, scraper and fine emery cloth.
d)
Thread sealing compound designed for type of connection and light machinery oil.
The single most common cause of pump vibration is from a bent shaft. Shafting is straightened to stringent tolerances prior to shipping and great care must be exercised in its handling.
Always support shafting in at least three places when lifting or installing.
Always support shafting in at least three places when lifting or installing. No installation should be attempted without adequate equipment necessary for a successful installation.
On hollow shaft drivers, check the clutch size
against the shaft size, which must go through the clutch
On solid shaft drivers, check the motor shaft size
against the coupling bore size
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Parts and accessories may be placed inside shipping containers, or attached to skids in individual packages.
Inspect all containers, crates and skids for attached parts before discarding.
Lifting heavy objects is dangerous. Use of appropriate tools and procedures is must.
4.1.2.3 Uncrating and cleaning of a fully assembled pump
a) Clean the parts of all dirt, packing material and
other foreign matter.
b) Clean all machined surfaces. Remove any rust
spots found on the machined surfaces with fine emery cloth.
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