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PVML USER INSTRUCTIONS ENGLISH 00079591  – 01/05 

®

 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 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 excess temperature 

•�

Prevent build up of explosive mixtures 

•�

Prevent the generation of sparks 

•�

Prevent leakages 

•�

Maintain the pump to avoid hazard 

 
The following instructions for pumps and pump units 
when installed in potentially explosive atmospheres 
must be followed to help ensure explosion protection.  
Both electrical and non-electrical equipment must 
meet the requirements of European Directive 
94/9/EC. 
 

1.6.4.1  Scope of compliance 

 Use equipment only in the zone for which it is  

appropriate.  Always check that the driver, 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, which is quite unusual for a PVML pump due to 
the closed coupled design, the Ex rating applies only 
to the pump.  The party responsible for assembling the 
pump set shall select the driver and any additional 
equipment, with the necessary CE Certificate/ 
Declaration of Conformity establishing it is suitable for 
the area in which it is to be installed. 
 
The output from a variable frequency drive (VFD) can 
cause additional heating affects in the motor and so, 
for pumps sets with a VFD, the ATEX Certification for 
the motor must state that it is covers the situation 
where electrical supply is from the VFD.  This 
particular requirement still applies even if the VFD is 
in a safe area. 

 

1.6.4.2  Marking 

An example of ATEX equipment marking is shown 
below.  The actual classification of the pump will be 
engraved on the nameplate. 

                                   

   II 2 GD c 135 ºC (T4)

 

 
Equipment Group 
I  = Mining 
II = Non-mining 

Category 
2 or M2 = High level protection 
3 = normal level of protection 

Gas and/or Dust 
G = Gas; D= Dust 

c = Constructional safety 
      (in accordance with prEn13463-5) 

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 
ATEX Ex rating on the nameplate.  These are based 
on a maximum ambient of 40 °C (104 °F); refer to 
Flowserve for higher ambient temperatures. 
 
The surface temperature on the pump is influenced 
by the temperature of the liquid handled.  The 
maximum permissible liquid temperature depends on 
the temperature class and must not exceed the 
values in the table that follows. 

Page 5 of 29 

Summary of Contents for PVML 25.04.04

Page 1: ...OPERATION MAINTENANCE PCN 00079591 ed 01 05 E These instructions should be read prior to installing operating using and maintaining this equipment Компания ПромХимТех официальный дистрибьютор насосов Flowserve www promhimtech ru Тел 8 800 250 01 54 e mail zakaz promhimtech ru ...

Page 2: ...e items 19 6 4 Tools required 19 6 5 Fastener torques 20 6 6 Setting impeller clearances 20 6 7 Disassembly 20 6 8 Examination of parts 21 6 9 Assembly 22 PAGE 7 FAULTS CAUSES AND REMEDIES 25 8 PARTS LIST AND DRAWINGS 27 8 1 Sectional drawings PVML 27 8 2 Parts list PVML 27 8 3 General arrangement drawing 28 9 CERTIFICATION 28 10 OTHER RELEVANT DOCUMENTATION AND MANUALS 28 10 1 Supplementary User ...

Page 3: ...ment incorporates information relevant to these Directives and Approvals To confirm the Approvals applying and if the product is CE marked check the serial number plate markings and the Certification See section 9 Certification 1 3 Disclaimer Information in these User Instructions is believed to be reliable In spite of all the efforts of Flowserve Pump Division to provide sound and all necessary i...

Page 4: ...xplosive 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...

Page 5: ... the requirements of European Directive 94 9 EC 1 6 4 1 Scope of compliance Use equipment only in the zone for which it is appropriate Always check that the driver 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 which is quite unusual for a PVML pump...

Page 6: ... 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 the fitting of...

Page 7: ...king or adversely affect the ambient conditions Where there is a risk from such tools or materials maintenance must be conducted in a safe area It is recommended that a maintenance plan and schedule is adopted See section 6 Maintenance 1 7 Nameplate and warning labels 1 7 1 Nameplate For details of nameplate see the Declaration of Conformity 1 7 2 Warning labels Page 7 of 29 ...

Page 8: ...o be encountered They represent sound pressure levels at 1 m 3 3 ft from the directly driven pump for free field over a reflecting plane If a pump unit only has been purchased for fitting with your own driver then the pump only noise levels from the table should be combined with the level for the driver obtained from the supplier If the motor is driven by an inverter it may show an increase in noi...

Page 9: ...pendent on their size and construction 2 3 Lifting To avoid distortion the pump unit should be lifted as shown Typical lifting of a PVML with base plate or extended levelling plate Unsafe lifting is never allowed A crane must be used for all pump sets in excess of 25 kg 55 lb Fully trained personnel must carry out lifting in accordance with local regulations The driver and pump weights are recorde...

Page 10: ...t design and has a keyed drive end 3 3 6 Stuffing box The stuffing box has a spigot rabbet fit between the pump casing and seal plate for optimum concentricity The design enables 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 for non hazardous service on...

Page 11: ...al alignment Concrete is the most suitable material for the base The base should contain recesses for the grouting of the foundation bolts Figure 3 shows a number of variations on the design of the foundation bolts Make these recesses in the base in accordance with the above figure referring to the dimensional drawing of the pump unit If a concrete base is used observe the following points do not ...

Page 12: ...his is not possible along the seal plate If the mechanical seal is fitted with a guard this should be removed level the levelling plate in the direction P Q with an accuracy of 0 15 µm m 0 002 in ft using the adjusting bolts see Figure 5 Fill the space between the filler blocks and the levelling plate with thin filler plates level the levelling plate in the directions R S with an accuracy of 0 15 ...

Page 13: ...wo sizes larger than the pump suction and discharge Typically main pipework velocities should not exceed 2 m s 6 ft sec suction and 3 m s 9 ft sec on the discharge Take into account the available NPSH which must be higher than the required NPSH of the pump Never use the pump as a support for piping Maximum forces and moments allowed on the pump flanges vary with the pump size and type To minimize ...

Page 14: ...mpatible liquid supply to the gland at 1 5 2 0 bar 20 30 psi above suction pressure is recommended 4 6 5 3 Pumps fitted with mechanical seals Single seals requiring re circulation will normally be provided with the auxiliary piping from pump casing already fitted If the seal requires an auxiliary quench then a connection must be made to a suitable source of liquid flow low pressure steam or static...

Page 15: ...is installed To prevent excessive surface temperatures at bearings it is recommended that temperature or vibration monitoring are carried out See sections 5 7 4 and 5 7 5 5 COMMISSIONING START UP OPERATION AND SHUTDOWN These operations must be carried out by fully qualified personnel 5 1 Pre commissioning procedure BEFORE START UP REMOVE TEMPORARY RUBBER GASKET ABOVE SEAL DRIVE COLLAR GASKET CAN B...

Page 16: ...iquids are being pumped it may be necessary to slacken the gland nuts to achieve leakage The pump should be run for 30 minutes with steady leakage and the gland nuts tightened by 10 degrees at a time until leakage is reduced to an acceptable level normally a minimum of 120 drops per minute is required Bedding in of the packing may take another 30 minutes Care must be taken when adjusting the gland...

Page 17: ...doubt contact your nearest Flowserve office 5 10 1 Specific gravity SG Pump capacity and total head in metres feet do not change with SG however pressure displayed on a pressure gauge is directly proportional to SG Power absorbed is also directly proportional to SG It is therefore important to check that any change in SG will not overload the pump driver or over pressurize the pump 5 10 2 Viscosit...

Page 18: ...rbon tetrachloride Protect yourself against toxic fumes when using cleaning agents 6 1 Maintenance schedule It is recommended that a maintenance plan and schedule is adopted in line with these User Instructions It should include the following a Any auxiliary systems installed must be monitored if necessary to ensure they function correctly b Gland packings if applied instead of a mechanical seal m...

Page 19: ...are shown on the pump nameplate To ensure continued satisfactory operation replacement parts to the original design specification should be obtained from Flowserve Any change to the original design specification modification or use of a non standard part will invalidate the pump s safety certification 6 2 2 Storage of spares Spares should be stored in a clean dry area away from vibration Inspectio...

Page 20: ... between the diffuser and the pump casing remove the packing ring 4590 2 from the pump casing and dispose of this in the proper way This type of packing may only be used once 6 7 2 Removing the diffuser This procedure describes removal of the diffuser from the casing cover Bend open the lock washers 6541 and remove the hexagon head bolts 6577 1 from the diffuser Remove the diffuser 6 7 2 Removing ...

Page 21: ...se wearing ring Take a drill with a slightly smaller diameter than the width of the case wearing ring Drill two holes along the centre line of the upright edge of the case wearing ring see Figure Drill both holes not deeper than the measured height of the case wearing ring Chip off the remaining edges of the drilled holes using a hammer and chisel see Figure Make sure that the centring rim is not ...

Page 22: ...ng the impeller wearing rings The procedure specified below is to be followed with regard to the impeller wearing rings 2300 1 2 on one or both sides of the impeller Clean the mounting surfaces of the impeller wearing ring and the impeller Use the appropriate personal protection equipment when heating and positio ning the impeller wearing ring Heat the impeller wearing ring to a temperature of 120...

Page 23: ... the thrower and the electric motor 6 9 6 Fitting the motor stool This procedure describes assembly of the motor stool to the casing cover Clean the mounting surfaces of the motor stool and the casing cover Carefully place the shaft of the electric motor in the shaft sleeve so that the motor stool is resting Tighten the bolts 6577 2 6 9 7 Fitting the impeller This procedure describes assembly of t...

Page 24: ...propriate lifting points Observe the lifting instructions described in section 2 3 The lifting lugs fixed to the motor are sufficient to lift the motor but are not suitable to lift the total unit Lift the casing cover above the pump casing and make sure that the casing cover is in the correct position in relation to the pump casing There is only one way for the casing cover to fit onto the pump ca...

Page 25: ...d replace faulty parts CONSULT FLOWSERVE Foot valve too small Investigate replacing the foot valve Foot valve partially clogged Clean foot valve Inlet of suction pipe insufficiently submerged Check out system design Speed too low CONSULT FLOWSERVE Speed too high CONSULT FLOWSERVE Total head of system higher than differential head of pump Total head of system lower than pump design head Check syste...

Page 26: ... solids in liquid pumped Internal misalignment of parts preventing seal ring and seat from mating properly Check and CONSULT FLOWSERVE Mechanical seal was run dry Check mechanical seal condition and source of dry running and repair Internal misalignment due to improper repairs causing impeller to rub Check method of assembly possible damage or state of cleanliness during assembly Remedy or CONSULT...

Page 27: ...ng 2300 2 Impeller wearing ring 2430 Throttling sleeve Stub sleeve 2540 Thrower 2913 Impeller screw 3160 Motor stool 4132 Neck bush 4590 2 Gasket 4590 3 Gasket 4590 4 Gasket Ref no Description 4610 O ring 6130 Sole plate 6541 Lock washer 6562 Protective guard 6570 1 Screw 6570 2 Screw 6570 3 Screw 6572 1 Stud continuous 6572 2 Stud continuous 6577 1 Hexagon head bolt 6577 2 Hexagon head bolt 6577 ...

Page 28: ...mentary instructions such as for a driver instrumentation controller seals sealant system etc are provided as separate documents in their original format If further copies of these are required they should be obtained from the supplier for retention with these User Instructions 10 2 Change notes If any changes agreed with Flowserve Pump Division are made to the product after its supply a record of...

Page 29: ... 6800 Latin America Flowserve S A de C V Avenida Paseo de la Reforma 30 2nd Floor Colonia Juarez Centro Mexico D F Z C 06040 Tel 52 5705 5526 Fax 52 5705 1125 Asia Pacific Flowserve Pte Ltd Pump Division 200 Pandan Loop 06 03 04 Pantech 21 Singapore 128388 Tel 65 775 3003 Fax 65 779 4607 Visit our web site at www flowserve com Your Flowserve factory contact Flowserve B V P O Box 55 Lansinkesweg 30...

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