Flowserve L Worthington Simpson User Manual

USER INSTRUCTIONS
WORTHINGTON SIMPSON® L and U
Installation
Operation
Horizontal, split case, volute type centrifugal pumps for water and general service
PCN=85392721 07-12 (Based on C953KH025)
These instructions must be read prior to installing,
operating, using and maintaining this equipment.
L and U USER INSTRUCTIONS ENGLISH 85392721 07-12
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 ......................................................... 10
2.5 Recycling and end of product life .................. 10
3 PUMP DESCRIPTION ...................................... 11
3.1 Configurations ............................................... 11
3.2 Name nomenclature ...................................... 11
3.3 Design of major parts .................................... 11
3.4 Performance and operating limits ................. 12
4 INSTALLATION ................................................ 12
4.1 Location ........................................................ 12
4.2 Part assemblies ............................................ 12
4.3 Foundation .................................................... 12
4.4 Grouting ........................................................ 13
4.5 Initial alignment ............................................. 13
4.6 Piping ............................................................ 14
4.7 Final shaft alignment check .......................... 16
4.8 Electrical connections ................................... 16
4.9 Protection systems ........................................ 17
6 MAINTENANCE ............................................... 21
6.1 General ......................................................... 22
6.2 Maintenance schedule.................................. 22
6.3 Spare parts ................................................... 24
6.4 Recommended spares and consumable items 24
6.5 Tools required ............................................... 25
6.6 Fastener torques .......................................... 25
6.7 Renewal clearances ..................................... 25
6.8 Disassembly ................................................. 25
6.9 Examination of parts ..................................... 26
6.10 Assembly ...................................................... 26
7 FAULTS; CAUSES AND REMEDIES ............... 28
8 PARTS LISTS AND DRAWINGS ...................... 30
8.1 Sectional drawing – L, double entry impeller,
grease lubricated, gland packed .................. 30
8.2 Sectional drawing – U Pump horizontal,
grease lubricated, cartridge seal .................. 31
8.3 Sectional drawing – U Pump vertival, grease
lubricated, cartridge seal .............................. 32
8.4 General arrangement drawing ...................... 33
9 CERTIFICATION .............................................. 33
10 OTHER RELEVANT DOCUMENTATION AND
MANUALS ........................................................ 33
10.1 Supplementary User Instructions ................. 33
10.2 Change notes ............................................... 33
10.3 Additional sources of information ................. 33
PAGE
5 COMMISSIONING, STARTUP, OPERATION
AND SHUTDOWN ........................................... 17
5.1 Pre-commissioning procedure ...................... 17
5.2 Pump lubricants ............................................ 18
5.3 Direction of rotation ....................................... 18
5.4 Guarding ....................................................... 19
5.5 Priming and auxiliary supplies ...................... 19
5.6 Starting the pump .......................................... 19
5.7 Running the pump ......................................... 19
5.8 Stopping and shutdown ................................ 21
5.9 Hydraulic, mechanical and electrical duty .... 21
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L and U USER INSTRUCTIONS ENGLISH 85392721 07-12
INDEX
PAGE
Additional sources (10.3) ......................................... 33
Alignment of shafting (4.5) ....................................... 13
ATEX marking (1.6.4.2) ............................................. 7
CE marking and approvals (1.2) ................................ 4
Certification (9) ........................................................ 33
Clearances (6.7, Renewal clearances).................... 25
Commissioning and operation (5) ............................ 17
Compliance, ATEX (1.6.4.1) ...................................... 6
Configurations (3.1) ................................................. 11
Consumable items (6.4) .......................................... 24
Copyright (1.4) ........................................................... 4
Design of major parts (3.3) ...................................... 11
Direction of rotation (5.3) ......................................... 18
Disassembly (6.8) .................................................... 25
Disclaimer (1.3) .......................................................... 4
Dismantling (6.8, Disassembly) ............................... 25
Drawings (8) ............................................................ 30
Duty conditions (1.5) .................................................. 4
Electrical connections (4.8) ..................................... 16
End of product life (2.5) ........................................... 10
Examination of parts (6.9) ....................................... 26
Fastener torques (6.6) ............................................. 25
Faults; causes and remedies (7) ............................. 28
Forces and moments (4.6.2) ................................... 14
Foundation (4.3) ...................................................... 12
General arrangement drawing (8.4) ........................ 33
General assembly drawings (8) ............................... 30
Grouting (4.4) ........................................................... 13
Guarding (5.4) .......................................................... 19
Handling (2.2) .......................................................... 10
Hydraulic; mechanical and electrical duty (5.9) ....... 21
Inspection (6.2.1 and 6.2.2) ..................................... 23
Installation (4) .......................................................... 12
Lifting (2.3) ............................................................... 10
Location (4.1) ........................................................... 12
Lubrication (5.1.1) .................................................... 17
Maintenance (6) ....................................................... 21
Maintenance schedule (6.2) .................................... 22
Name nomenclature (3.2) ........................................ 11
Nameplate (1.7.1) ...................................................... 8
Operating limits (3.4.1) ............................................ 12
Ordering spare parts (6.3.1) .................................... 24
Parts lists (8) ............................................................ 30
Performance (3.4) .................................................... 12
Piping (4.6) .............................................................. 14
PAGE
Priming and auxiliary supplies (5.5) .........................19
Protection systems (4.9) ..........................................17
Reassembly (6.10 Assembly) ..................................26
Receipt and unpacking (2.1) ....................................10
Recommended grease lubricants (5.2.2) .................18
Recommended oil lubricants (5.2.1) ........................18
Recommended spares (6.4) .....................................24
Re-lubrication (6.2.3) ................................................23
Renewal clearances (6.7) ........................................25
Replacement parts (6.3 and 6.4) ..............................24
Running the pump (5.7) ...........................................19
Safety (1.6) ................................................................. 5
Safety action (1.6.3) ................................................... 5
Safety labels (1.7.2) ................................................... 8
Safety markings (1.6.1) .............................................. 5
Safety, protection systems (4.9) ...............................17
Sectional drawings (8) ..............................................30
Sound pressure level (1.9, Noise level) ..................... 9
Sources, additional information (10.3) .....................33
Spare parts (6.3) ......................................................24
Specific machine performance (1.8) .......................... 8
Starting the pump (5.6).............................................19
Start/stop frequency (5.7.6) ......................................21
Stopping and shutdown (5.8) ...................................21
Storage, pump (2.4) .................................................10
Storage, spare parts (6.3.2) .....................................24
Supplementary manuals or info sources (10) ..........33
Supplementary User Instructions (10.1)...................33
Tools required (6.5) ..................................................25
Torques for fasteners (6.6) .......................................25
Trouble-shooting (see 7) ..........................................28
Vibration (5.7.5) ........................................................20
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L and U USER INSTRUCTIONS ENGLISH 85392721 07-12
1. INTRODUCTION AND SAFETY
1.1 General
These Instructions must always be kept
close to the product's operating location or directly with the product.
Flowserve products are designed, developed and manufactured with state-of-the-art technologies in modern facilities. The unit is produced with great care and commitment to continuous quality control, utilising sophisticated quality techniques, and safety requirements.
Flowserve is committed to continuous quality improvement and being at service for any further information about the product in its installation and operation or about its support products, repair and diagnostic services.
These instructions are intended to facilitate familiarization with the product and its permitted use. Operating the product in compliance with these instructions is important to help ensure reliability in service and avoid risks. The instructions may not take into account local regulations; ensure such regulations are observed by all, including those installing the product. Always coordinate repair activity with operations personnel, and follow all plant safety requirements and applicable safety and health laws and regulations.
These instructions must be read prior to
installing, operating, using and maintaining the equipment in any region worldwide. The equipment must not be put into service until all the conditions relating to safety noted in the instructions, have been met. Failure to follow and apply the present user instructions is considered to be misuse. Personal injury, product damage, delay or failure caused by misuse are not covered by the Flowserve warranty.
1.2 CE marking and approvals
It is a legal requirement that machinery and equipment put into service within 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 of 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 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 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 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 the written agreement of Flowserve before start up.
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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 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 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 be avoided.
APPLYING HEAT TO REMOVE IMPELLER There may be occasions when the impeller has either been shrunk fit on to the pump shaft or has become difficult to remove due to products of corrosion.
If you elect to use heat to remove the impeller, it must be applied quickly to the impeller boss. TAKE GREAT CARE!
Before applying 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 vapour. This must be carried out with the shaft in the vertical position. On some pump sizes a cavity exists in the impeller bore so on occasions a significant volume of liquid may drain out.
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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 80 °C (175 °F) o r below -5 °C (23 °F) in a restricted zone, or exceed local regulations, action as above shall be taken.
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 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 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 pump and mechanical 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.
1.6.4 Products used in potentially explosive
atmospheres
Measures are required to:
Avoid excessive surface 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. For ATEX, both electrical and non-electrical equipment must meet the requirements of 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.
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 effects in the motor and so, for pumps sets with a VFD, the ATEX Certification for the motor must state that it is covers the situation 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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s
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 temperature
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 ºC (104 ºF); refer to Flowserve for higher ambient temperatures.
The surface temperature on the pump is influenced by the temperature of the liquid handled. The maximum permissible liquid temperature depends on the ATEX temperature class and must not exceed the values in the table that follows.
Temperature clas
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
65 °C (149 °F) *
80 °C (176 °F) * 115 °C (239 °F) * 180 °C (356 °F) * 275 °C (527 °F) * 400 °C (752 °F) *
The temperature rise at the seals and bearings and due to the minimum permitted flow rate is taken into account in the temperatures stated.
The operator is responsible to ensure that the specified maximum liquid temperature is not exceeded.
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.
Avoid mechanical, hydraulic or electrical overload by using motor overload trips, temperature monitors or a power monitor and make routine vibration monitoring checks.
In dirty or dusty environments make regular checks and remove dirt from areas around close clearances, bearing housings and motors.
Where there is any risk of the pump being run against a closed valve generating high liquid and casing external surface temperatures fit an external surface temperature protection device.
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.
1.6.4.4 Preventing the build up of explosive mixtures
ENSURE THE PUMP IS PROPERLY FILLED AND VENTED AND DOES NOT RUN DRY Ensure the pump and relevant suction and discharge pipeline system is totally filled with liquid at all times during the pump operation, so that an explosive atmosphere is prevented. In addition it is essential to make sure that seal chambers, auxiliary shaft seal systems and any heating and cooling systems are properly filled.
If the operation of the system cannot avoid this condition, fit an appropriate dry run protection device is (for example 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.
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1.6.4.5 Preventing sparks
To prevent a potential hazard from mechanical
contact, the coupling guard must be non-sparking. To avoid the potential hazard from random induced
current generating a spark, the baseplate must 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. Correct coupling alignment must be maintained.
Additional requirement for metallic pumps on non-metallic baseplates
When metallic components are fitted on a non­metallic baseplate they must be individually earthed.
1.6.4.6 Preventing leakage
The pump must only be used to handle liquids for which it has been approved to have the correct corrosion resistance.
Avoid entrapment of liquid in the pump 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, install of a liquid detection device.
1.6.4.7 Maintenance to avoid the 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.)
1.7 Nameplate and safety labels
1.7.1 Nameplate
For details of nameplate, see the Declaration of Conformity, or separate documentation included with
these User Instructions.
1.7.2 Safety labels
Oil lubricated units only:
1.8 Specific machine performance
For performance parameters see section 1.5, Duty conditions. When the contract requirement specifies
these to be incorporated into User Instructions these are included here. Where performance data has been supplied separately to the purchaser these should be obtained and retained with these User Instructions if required.
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1 1 85
1.9 Noise level
Attention must be given to the exposure of personnel to the noise, and local legislation will define when guidance to personnel on noise limitation is required, and when noise exposure reduction is mandatory. This is typically 80 to 85 dBA.
The usual approach is to control the exposure time to the noise or to enclose the machine to reduce emitted sound. You may have already specified a limiting noise level when the equipment was ordered, however if no noise requirements were defined, then attention is drawn to the following table to give an indication of equipment noise level so that you can take the appropriate action in your plant.
Pump noise level is dependent on a number of operational factors, flow rate, pipework design and acoustic characteristics of the building, and so the values given are subject to a 3 dBA tolerance and cannot be guaranteed.
Similarly the motor noise 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 1 pW) then add 17 dBA to the sound pressure value.
Motor size and speed
kW (hp)
<0.55(<0.75) 72 72 64 65 62 64 62 64
0.75 (1) 72 72 64 66 62 64 62 64
1.1 (1.5) 74 74 66 67 64 64 62 63
1.5 (2) 74 74 66 71 64 64 62 63
2.2 (3) 75 76 68 72 65 66 63 64 3 (4) 75 76 70 73 65 66 63 64 4 (5) 75 76 71 73 65 66 63 64
5.5 (7.5) 76 77 72 75 66 67 64 65
7.5 (10) 76 77 72 75 66 67 64 65 11(15) 80 81 76 78 70 71 68 69
15 (20) 80 81 76 78 70 71 68 69
18.5 (25) 81 81 77 78 71 71 69 71 22 (30) 81 81 77 79 71 71 69 71 30 (40) 83 83 79 81 73 73 71 73 37 (50) 83 83 79 81 73 73 71 73 45 (60) 86 86 82 84 76 76 74 76 55 (75) 86 86 82 84 76 76 74 76
75 (100) 87 87 83 85 77 77 75 77 90 (120) 87 88 83 85 77 78 75 78
110 (150) 89 90 85 87 79 80 77 80 150 (200) 89 90 85 87 79 80 77 80 200 (270) 300 (400) 87
1
The noise level of machines in this range will most likely be of values which require noise exposure control, but typical values are inappropriate.
Note: for 1 180 and 960 r/min reduce 1 450 r/min values by 2 dBA. For 880 and 720 r/min reduce 1 450 r/min values by 3 dBA.
3 550 r/min 2 900 r/min 1 750 r/min 1 450 r/min
Pump
only
1 1
Pump and
Typical sound pressure level LpA at 1 m reference 20 µPa, dBA
motor
Pump
only
Pump and
motor
Pump
only
Pump and
motor
87 83 90 85
Pump
only
Pump and
motor
85 86
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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 and received in writing within one month of receipt of the equipment. Later claims cannot be accepted.
Check any crates, 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.
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
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.
To avoid distortion, the pump unit
should be lifted as shown:
Do not use the driver, bare-shaft pump or component lifting points to lift the complete machine. Before lifting the driver alone, refer to the manufacturer’s instructions.
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 environment, these should be removed and disposed of in accordance with current regulations. This also includes the liquids and or gases that may be used in the "seal system" or other utilities.
Make sure that hazardous substances are disposed of safely and that the correct personal protective equipment is used. The safety specifications must be in accordance with the current regulations at all times.
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3 PUMP DESCRIPTION
3.1 Configurations
The L and U range of pumps are horizontal split casing volute type centrifugal pumps designed for water works, drainage, general service and circulating applications. They can be used with motor, steam turbine and gasoline or diesel engine drives.
The range can have the following configurations:
L single-stage horizontal suction and discharge nozzles. U two-stage horizontal suction and discharge nozzles.
LV single-stage horizontal suction/discharge, vertical shaft. UV two-stage horizontal suction/discharge, vertical shaft.
3.2 Name nomenclature
The pump size will be engraved on the nameplate typically as below:
6 L-13
Nominal discharge branch size (inch) Configuration – see 3.1 above Nominal maximum impeller diameter (inch) The typical nomenclature above is the general guide
to the configuration description. Identify the actual pump size and serial number from the pump nameplate. Check that this agrees with the applicable certification provided.
3.3 Design of major parts
3.3.1 Pump casing
The pump has its main casing gasket axial to the shaft allowing maintenance to the rotating element by removing the top half casing. Suction and discharge branches are in the bottom half and therefore remain undisturbed.
3.3.2 Impeller
The impeller is fully shrouded and may be fitted with optional hub rings.
3.3.3 Shaft
The large diameter stiff shaft, mounted on bearings, has a keyed drive end.
3.3.4 Pump bearings and lubrication
Ball bearings are fitted and are grease lubricated as standard. There is an option of oil lubrication when the pump is intended for horizontal mounting.
Bearing isolators or stationary labyrinths may be fitted as an option in the bearing covers to protect the bearings.
Vertically built pumps have as standard has a liquid lubricated journal bearing fitted at the non-drive end. This bearing is lubricated by pumped product or from an external clean source.
3.3.5 Bearing housing
Two grease nipples enable grease lubricated bearings to be replenished between major service intervals.
3.3.6 Seal housing
The design enables one of a number of sealing options to be fitted.
3.3.7 Shaft seal
The mechanical seal(s), attached to the pump shaft, seals the pumped liquid from the environment. Gland packing may be fitted as an option on the L and U.
3.3.8 Driver
The driver is normally an electric motor. Different drive configurations may be fitted such as internal combustion engines, turbines, hydraulic motors etc driving via couplings, belts, gearboxes, drive shafts etc.
3.3.9 Accessories
Accessories may be fitted when specified by the customer.
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