Flowserve FM Centrifugal Pump PCN=71576526, 71576526 User Instructions

USER INSTRUCTIONS
FM centrifugal pump
Multi-stage, centrifugal close-coupled pump with an axial suction and a vertical axis discharge
PCN=71576526 – 03/07 (E)
Installation
Operation
These instructions must be read prior to installing,
operating, using and maintaining this equipment.
FM USER INSTRUCTIONS ENGLISH 71576526 - 03/07
Page 2of 32 flowserve.com
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......................................................... 11
2.4 Storage...................................................... 11
2.5 Recyclingand endof product life ............... 11
3 PUMP DESCRIPTION ...................................... 11
3.1 Descriptionand restrictions of use ............. 11
3.2 Nomenclature............................................ 12
3.3 Coveragecharts........................................ 13
4 INSTALLATION................................................. 15
4.1 Location..................................................... 15
4.2 Foundation ................................................ 15
4.3 Piping........................................................ 15
4.4 Electrical connections ................................ 17
4.5 Protection systems.................................... 18
5 COMMISSIONING START-UP, OPERATION AND
SHUTDOWN....................................................... 18
5.1 Direction of rotation.................................... 18
5.2 Guarding.................................................... 18
5.3 Priming and auxiliary supplies.................... 18
5.4 Starting the pump....................................... 19
5.5 Running the pump ..................................... 19
5.6 Stopping and shutdown ............................. 21
5.7 Hydraulic, mechanical andelectrical duty... 22
5.8 Pumps for Food Use or Potable Water....... 22
Page
6 MAINTENANCE................................................ 22
6.1 General..................................................... 22
6.2 Maintenance schedule............................... 23
6.3 Spare parts................................................ 25
6.4 Recommended spares............................... 25
6.5 Disassembly.............................................. 25
7 FAULTS; CAUSES AND REMEDIES................. 27
8 PARTS LIST AND DRAWINGS......................... 28
8.1 Sectional drawing ...................................... 28
8.2 Sectional drawing parts list........................ 29
8.3 General arrangement drawing.................... 29
9 CERTIFICATION.............................................. 29
10 OTHER RELEVANTDOCUMENTATION AND
MANUALS ........................................................... 29
10.1 Supplementary User Instructions manuals29
10.2 Change notes .......................................... 29
10.3 Additional sources of information.............. 29
FM USER INSTRUCTIONS ENGLISH 71576526 - 03/07
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INDEX
Page
Additional sources (10.3) .....................................29
ATEX marking (1.6.4.2)..........................................7
CE marking andapprovals (1.2).............................4
Certification (9)....................................................29
Change notes (10.2)............................................29
Cleaning prior to operation (5.8.1)........................22
Commissioning, start-up, operation (5).................18
Compliance, ATEX (1.6.4.1)...................................6
Configurations (3.1) .............................................11
Copyright (1.4).......................................................4
Coverage charts (3.3)..........................................13
Direction of rotation (5.1)......................................18
Disassembly (6.5)................................................25
Discharge piping(4.3.3) ......................................16
Disclaimer (1.3)......................................................4
Dismantling (see 6.5, Disassembly) .....................25
Drawings (8.1).....................................................28
Duty conditions (1.5)..............................................4
Electrical connections (4.4)..................................17
Electrical supply (4.4.2)........................................17
End of product life (2.5)........................................11
Faults; causes and remedies (7)..........................27
Final checks (4.3.4)..............................................17
First pump start up (5.4.2) ...................................19
Foundation (4.2)..................................................15
Forces andmoments (see 4.3.1)..........................16
General arrangement drawing (8.3)......................29
Gland packing (6.2.5)...........................................24
Guarding (5.2)......................................................18
Handling (2.2)......................................................10
Hydraulic, mechanical and electrical duty (5.7).....22
Inspection (6.2.2and 6.2.3)..................................24
Installation (4)......................................................15
Internal coating (6.2.6).........................................25
Lifting (2.3)...........................................................11
Location (4.1).......................................................15
Maintenance (6)...................................................22
Maintenance schedule (6.2).................................23
Mechanical seal (6.2.4)........................................24
Nomenclature (3.2) ..............................................12
Nameplate (1.7.1)..................................................8
Operating limits (see3.1) .....................................12
Orderingspare parts (6.3.1).................................25
Parts lists (8.2).....................................................29
Piping (4.3)..........................................................15
Protection systems (4.5)......................................18
Pump masses (2.2.2)...........................................10
Receipt and unpacking (2.1) ................................10
Recommended spares (6.4).................................25
Recycling (2.5).....................................................11
Replacement parts (see 6.3 and 6.4)....................25
Running the pump (5.5) .......................................19
Safety action (1.6.3)...............................................5
Safety labels (1.7.2)...............................................8
Safety markings (1.6.1)..........................................5
Safety, protectionsystems (see 1.6 and4.8)
Page
Sectional drawings (8.1) ......................................28
Sound level (see 1.9, Noise level)..........................9
Sources, additional information (10.3)..................29
Spare parts (6.3)..................................................25
Specific machine performance (1.8).......................8
Standard maintenance (6.2.1) .............................23
Starting the pump (5.4)........................................19
Stop/start frequency (5.5.6)..................................21
Stoppingand shutdown (5.6) ............................... 21
Storage, pump (2.4).............................................11
Storage, spare parts (6.3.2) .................................25
Suction piping (4.3.2)...........................................16
Supplementary manuals or information sources...29
Transport and storage (2) ...................................10
Trouble-shooting (see 7)...................................... 27
Vibration (5.5.5)...................................................21
FM USER INSTRUCTIONS ENGLISH 71576526 - 03/07
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1 INTRODUCTION AND SAFETY
1.1 General
These instructions must always be kept close to the product's operating location or directly with the product.
Flowserve 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 installationand operation or about its support products, repair and diagnostic services.
These instructionsare intendedto facilitate familiarization with the product andits permitted use. Operating the product in compliance with these instructions is important to help ensure reliability in service andavoid risks. The instructions may not take into account local regulations; ensure such regulations are observed by all, including those installingthe product. Always coordinate repair activity with operations personnel, and follow all plant safety requirements andapplicable safety and health laws and regulations.
These instructions must be read prior to installing, operating,using and maintaining the equipment in any region worldwide. The equipment must not be put into service until all the conditions relating to safety noted in the instructions, have been met.
1.2 CE marking and approvals
It is a legal requirement that machinery and equipment put into service withincertain regionsof the worldshall conformwith the applicable CE MarkingDirectives coveringMachinery and, where applicable, Low Voltage Equipment, Electromagnetic Compatibility (EMC), Pressure Equipment Directive (PED) andEquipment for Potentially Explosive Atmospheres (ATEX).
Where applicabletheDirectives andany additional Approvals cover importantsafety aspectsrelating to machinery andequipment and the satisfactory provision oftechnicaldocuments andsafety instructions. Where applicablethis document incorporatesinformationrelevanttotheseDirectives and Approvals.
To confirm the Approvalsapplyingandifthe productis CE marked,checktheserial number plate markings andthe Certification. (Seesection 9, Certification.)
1.3 Disclaimer
Information in these UserInstructions is believed to be reliable.In spiteof all the efforts of Flowserve Corporation to provide soundandall necessary information the content of thismanualmayappear insufficientandis not guaranteed by Flowserveas to its completenessor accuracy.
Flowserve manufactures productstoexacting InternationalQualityManagementSystem Standards as certifiedandaudited by externalQuality Assurance organizations. Genuine partsand accessories have beendesigned,tested andincorporated into the productsto helpensure theircontinuedproduct quality and performancein use. As Flowservecannot test parts andaccessoriessourced fromothervendorsthe incorrect incorporationofsuch partsandaccessories may adverselyaffect the performanceandsafety featuresof the products. Thefailureto properlyselect, installor use authorized Flowserve partsand accessoriesisconsideredto be misuse. Damage or failurecausedby misuse is notcovered by the Flowserve warranty. In addition,any modificationof Flowserve productsor removal of originalcomponents may impairthesafety of these products intheir 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 shouldbe kept with these instructions.
The productmust not be operatedbeyond the parameters specified for the application. If there is anydoubt 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.
FM USER INSTRUCTIONS ENGLISH 71576526 - 03/07
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1.6 Safety
1.6.1 Summary of safety markings
These UserInstructions containspecific safety markings where non-observance of aninstruction wouldcause hazards. Thespecific safety markings are:
This symbol indicates electricalsafety instructions where non-compliance will involve a highrisk to personal safety or the loss of life.
This symbol indicates safety instructions where non-compliance would affect personal safety and could result in loss of life.
This symbol indicates “hazardous substances and toxicfluid”safety instructions where non­compliance would affect personalsafety andcould result in loss of life.
This symbol indicates safety instructions where non-compliance willinvolve some risk to safe operationand personalsafety andwould damage the equipment or property.
This symbol indicates explosive atmosphere zone marking according to ATEX. It is used in safety instructions where non-compliance in the hazardous area would cause the risk of an explosion.
This symbol is used in safety instructions to remind not to rub non-metallic surfaces with a dry cloth; ensure cloth is damp. It is usedwhere non­compliance in the hazardous area would cause the risk of an explosion.
Thissign is not a safetysymbol butindicates
an importantinstructionin 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 andskill, 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 PUMPAND 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 (482ºF), 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 havesharp corners and the wearing of appropriate safety gloves andequipment is required when handling these components. To lift heavy pieces above 25 kg (55 lb) use a crane appropriate for the mass andin accordance with current local regulations.
THERMAL SHOCK Rapid changes in the temperature of the liquid within the pumpcan cause thermal shock, which can result in damage or breakage ofcomponents and should be avoided.
NEVERAPPLY HEATTO REMOVE IMPELLER Trapped lubricant or vapor could causean explosion.
HOT (and cold) PARTS If hot or freezing components or auxiliary heating supplies can present adanger to operators and persons enteringthe 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 enteringthe immediate area. Note: bearing housings must not be insulated and drive motors and bearings may be hot.
If the temperature is greater than 68 °C (175 °F) or below 5 °C (20 °F) in a restricted zone, or exceeds local regulations, action as above shall be taken.
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HAZARDOUS LIQUIDS Whenthepump is handlinghazardous liquidscare must be takento avoidexposure to the liquid by appropriatesittingof the pump, limitingpersonnel access and byoperatortraining.Ifthe liquid is flammable and/orexplosive, strictsafety procedures must be applied.
Gland packingmust not be used when pumping hazardous liquids.
PREVENTEXCESSIVE EXTERNAL PIPE LOAD Do not use pumpas a support for piping. Do not mount expansion joints, unless allowed by Flowserve in writing, so that their force, due to internal pressure, actson the pump flange.
ENSURE CORRECTLUBRICATION (See section 5, Commissioning, startup, operation and shutdown.)
STARTTHE PUMP WITHOUTLET VALVE PARTOPENED (Unless otherwise instructed at a specificpoint 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 wherethis situation cannot occur. Pumpoutlet valve shall may need to be adjusted to comply with the duty followingthe run-up process. (Seesection 5, Commissioning start-up, operation and shutdown.)
NEVER RUN THE PUMP DRY
INLET VALVES TO BE FULLY OPEN WHEN PUMP IS RUNNING Running the pumpat zeroflow or below the recommended minimumflow continuously willcause damage to theseal.
DO NOT RUN THE PUMP AT ABNORMALLY HIGH OR LOW FLOW RATES Operating at a flow rate higher than normalor 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.
1.6.4 Productsused in potentially explosive atmospheres
The following instructionsfor pumps andpump units when installedin potentiallyexplosive atmospheres must be followed to help ensure explosionprotection.
The terminology and procedures ensure that the installed pump is in compliance with the European Directive 94/9/EC, knownasthe ATEXDirective, which is mandatory in Europe andmay also be specified in other countries.Where applicable, bothelectricaland non-electrical equipment must meet the requirements 94/9/EC.
Evenif theinstallationis ina region where ATEXis not theapplicable regulation, the generalmeasures described shall be followedtoensure safeoperation.
The measures are explained under the headings of:
Avoiding excessive surface temperaturePreventing build up of explosive mixturesPreventing the generation of sparksPreventing leakagesMaintaining the pump to avoid hazard
1.6.4.1 Scope of compliance
Use equipmentonly inthezone for whichitis appropriate. Alwayscheckthat the driver,drive couplingassembly, seal and pump equipmentare suitably ratedand/orcertifiedfor theclassification of thespecificatmospherein which they areto be installed.
WhereFlowserve hassupplied only the bareshaft pump, the Ex rating applies only to the pump. The partyresponsible for assembling the pump setshall selectthe coupling, driver andany additional equipment, with the necessary CE Declaration of Conformity establishing it issuitablefor the area in whichit is to be installed.
The output froma variable frequency drive (VFD)can cause additional heatingaffectsin the motor andso, for pumps sets with a VFD, the ATEXCertificationforthe motor muststatethatit is coversthesituationwhere electricalsupply isfromthe VFD. This particular requirementstillapplies evenif the VFD is ina safe area.
FM USER INSTRUCTIONS ENGLISH 71576526 - 03/07
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1.6.4.2 Marking
Anexample 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 levelof protection
Gas and/or Dust G = Gas; D=Dust
c = Constructionalsafety
(in accordance withEN 13463-5)
Gas Group (Equipment Category 2 only) IIA –Propane (typical) IIB –Ethylene (typical) IIC – Hydrogen(typical)
Maximum surface temperature(TemperatureClass) (seesection 1.6.4.3)
1.6.4.3 Avoiding excessive surface temperatures
ENSURE THE EQUIPMENT TEMPERATURE
CLASS IS SUITABLE FOR THE HAZARD ZONE Pumps have a temperature class as stated in the
ATEX Ex rating on the nameplate. These are based on a maximumambient of 40 °C (104 °F); refer to Flowserve for higher ambient temperatures.
The surface temperature on the pump is influenced by the temperature of the liquid handled. The maximum permissible liquid temperature depends on the temperature class and must not exceed the values in the table that follows.
The temperature rise at the seals, bearings and due to the minimum permitted flow rate is taken into account in the temperatures stated.
Temperature
classto
EN13463-1
Maximum
surface
temperature
permitted
Temperature limit of liquid
handled (* depending on
material and construction
variant- check which is
lower)
T6 T5 T4 T3 T2 T1
85 °C (185°F) 100 °C (212°F) 135 °C (275°F) 200 °C (392°F) 300 °C (572°F) 450 °C (842°F)
Consult Flowserve Consult Flowserve
115°C (239 °F) * 180°C (356 °F) * 275°C (527 °F) * 400°C (752 °F) *
The responsibility for compliance with the specified maximum liquid temperature is with the plant operator.
Temperature classification “Tx” is used when the liquid temperature varies and the pumpcould be installed in different hazardous atmospheres. In this case the user is responsible for ensuring that the pump surface temperature does not exceed that permitted in the particular hazardous atmosphere.
If an explosive atmosphere exists during the installation, do not attempt to check the direction of rotation by starting the pump unfilled. Even a short run time may give a hightemperature resulting from contact between rotating and stationary components. Furthermore, confinement of liquid in the pumpand pipes must be avoided (valve closed). If the liquid heats up this may cause excessive pressure andlead to bursting of pump components.
Wherethere is anyrisk of the pump being runagainst a closed valve generating high liquid and casing externalsurface temperatures it is recommended that users fit anexternalsurface temperature protection device.
Avoid mechanical, hydraulic or electrical overload by using motor overload trips, temperature monitor or a power monitor and make routine vibration monitoring checks.
In dirty or dusty environments, regular checks must be made and dirt removed fromareas around close clearances, bearinghousings and motors.
1.6.4.4 Preventing the build up of explosive mixtures
ENSURE PUMP IS PROPERLY FILLED AND
VENTED AND DOES NOT RUN DRY. Ensure pump and relevant suction and discharge
pipeline systemis totally filledwith 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 thesystem cannot avoid this condition the fitting of an appropriate dry run protection device is recommended (eg liquid detection or power monitor).
To avoid potential hazards fromfugitive emissions of vapor 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 ground contact on the baseplate must be used.
Avoid electrostatic charge: do not rub non­metallic surfaces with a dry cloth, ensure cloth is damp. Where applicable the coupling must be selected to comply with 94/9/EC and correct alignment must be maintained.
Additional requirements for metallic pumps on non-metallic baseplates
When metallic components are fitted on a non­metallic baseplate they must be individually earthed (grounded).
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.
Avoidentrapmentof liquid in the pump andassociated pipingdue toclosingofsuction anddischargevalves, which couldcause dangerous excessive pressuresto occurif thereis heatinputto the liquid. Thiscanoccur if the pump is stationary or running.
Bursting of liquid containing parts due to freezing must be avoided by draining or protectingthe pump and ancillary systems.
Where there is the potential hazard of a loss ofa seal barrier fluid or external flush, the fluid must be monitored.
If leakage of liquid to atmosphere can result in a hazard, the installation of a liquid detection device is recommended.
1.6.4.7 Maintenance to avoid the hazard
CORRECTMAINTENANCE IS REQUIRED TO AVOID POTENTIAL HAZARDS WHICHGIVE 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, cleaningand painting materials used must not give rise tosparking or adversely affect the ambient conditions.
Where there is a risk fromsuch tools or materials; maintenance must be conducted in a safe area. It is recommended that a maintenance planand 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, orseparate 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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1.9 Noise level
Attention must be given to theexposure 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 cantake 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 dBAtolerance and cannot be guaranteed.
Similarly the motor noise assumed in the “pump and motor” noise is that typically expected fromstandard 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 “pumponly” noise levels in the table should be combined with the level for the driver obtained from the supplier. Consult Flowserve or anoise specialist if assistance is required in combining the values.
It is recommended that where exposure approaches the prescribedlimit, thensite noise measurements should be made.
The values are in sound pressure level LpAat 1 m (3.3 ft) from the machine, for “free field conditions over a reflecting plane”.
For estimating sound power level LWA (re1 pW) then add 17 dBA to the soundpressure value.
TypicalsoundpressurelevelLpAat1 m reference 20 μPa, dBA
3 550 r/min 2 900 r/min 1 750 r/min 1 450 r/min
Motor size and speed
kW (hp)
Pump
only
Pump and
motor
Pump
only
Pump and
motor
Pump
only
Pump and
motor
Pump
only
Pump and
motor
< 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) 85 87 83 85 300 (400) 87 90 85 86
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/minreduce 1 450 r/min values by 2dBA. For 880 and 720 r/min reduce 1 450 r/min values by 3 dBA.
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In areas where the staff has to intervene, remember that whenthe level of thesound pressure is: below 70 dBA: it is not necessary to take special
precautions.
above 70 dBA: people working continuously in
the machine room must be supplied with protective devicesagainst noise.
below 85 dBA: no particular measures need to
be taken for casual visitors stayingin the room during a limited period.
above 85 dBA: the room must be considered as
a dangerous area because of the noise and a warning sign must be fixed at each entry warning the people cominginto the room, even for a short period, thatthey must wear hearing protection.
above 105 dBA: special hearing protection
adapted to this noise level and to the spectral noise components must be installed and a warning sign to this effect erected at each entry. The staff in the room must wear ear protection.
Make sure that the noise, which travels through the walls andwindows, does not generate too high noise levels in the machine room's surroundings.
2 TRANSPORT AND STORAGE
2.1 Consignment receipt and unpacking
Immediately after receipt of theequipment it must be checked against the delivery and shipping documents forits completeness and that there has been no damage in transportation.
Any shortage and or damage must be reported immediately to the Flowserve and received in writing within one month of receiptof the equipment. Later claims cannot be accepted. Check any crates, boxes andwrappings for any accessories or spare parts which may be packed separately withthe equipment or attached to side walls of the box orequipment.
Each product has a unique serial number. Check that this number corresponds with that advisedand always quote this number in correspondence as well as when ordering spare parts or further accessories.
2.2 Handling
2.2.1 General instructions concerning handling
Boxes, crates, pallets or cartons may be unloaded using fork lift vehicles or slings dependent on their size andconstruction. See 2.3.1 for positioningof slings.
To lift heavy pieces above 25 kg (55 lb), use a winch adapted to the mass and in accordance with the current local regulations.
To lift machines or pieces with oneor several suspension rings, only use hooks and chains in compliance with the local regulations concerning safety.
Never put cables, chains orropes directly on orin the suspension rings. Cables, chains or liftingropes must never present excessive bending.
Never bendthe lifting hooks, suspension rings, chains, etc... which should only be made to endure stresses within calculated limits. Remember that the capacity of a lifting device decreases when the direction of thelifting force direction makes an angle with the device axis.
To increase the safety andthe efficiency of the lifting device, allthe lifting elements must be as perpendicular as possible. If necessary a lifting beam can be placed between the winch and the load.
When heavy pieces are lifted up, never stay or work under the load or in the area which could be in the path of the load if it were to swingor fall away.
Never leave aload hanging froma winch. The acceleration or the slowing-down of lifting equipment must stay in the safety limits for the staff.
A winch must be positioned in such a way that the load will be raised perpendicularly. Where possible necessary precautionsmust be taken to avoid the swing of the load, usingfor example two winches making approximately the same angle, below 30°, with the vertical.
2.2.2 Pump masses
Unit Mass
FM
Motor Mass
Pump type
kg lb kg lb
50 FM 2E 51 112 16 35 50 FM 3E 61 134 21 46 50 FM 2L 57 126 21 46 50 FM 3L 63 139 26 57 50 FM 4L 77 170 36 79 50 FM 5L 107 236 43 95 65 FM 2aE 77 170 36 79 65 FM 2cE 85 187 43 95 65FM 3bE 120 265 63 139 65 FM 3cE 120 265 63 139 65 FM 4cE 155 342 72 159 65 FM 1cL 60 132 26 57 65 FM 2aL 77 170 36 79 65 FM 2cL 85 187 43 95 65 FM 3bL 120 265 63 139 65 FM 3cL 120 265 63 139 65 FM 4cL 155 342 72 159
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