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English

18

Wilo AG 09/2005

The example (N) value is given for the preferred 
operating flow region (typically this may extend to 
70 to 120 % of the pump best efficiency point); 
outside the preferred flow region the actual vibra-
tion experienced may be multiplied by up to 2.
These standard values can vary with the rotational 
speed and the power absorbed by the pump. For 
any special case, do not hesitate to consult us.

5.5.6 Stop/start frequency

Pump sets are normally suitable for the number of 
equally spaced stop/starts per hour shown in the 
table below. Check actual capability of the driver 
and control/starting system before commissio-
ning.   

Where duty and standby pumps are installed it is 
recommended that they are run alternately every 
week.

5.6

Stopping and shutdown

5.6.1 Stopping and restarting in continuous running

According to hydraulic conditions of the installa-
tion and its automation degree, stop and restart 
procedures can have different forms. Neverthe-
less all of them must respect imperatively the fol-
lowing rules:

Stopping:

a) Avoid that the unit turns in the opposite direc-
tion to the normal running.
b) Make sure that the discharge line pressure does 
not reach the foot valve.
c) Avoid a continuous running below the authori-
zed flow rate (see § 5.4.2).

Restart:

a) Ensure that the pump is completely full of liquid.
b) Ensure a continuous supply with a sufficient 
available NPSH.
c) Ensure a backpressure so that the motor power 
is not in excess. 
  

 

Protect the pump against water hammer when 

stopping or starting

Shutdown:  

     

5.7

Hydraulic, mechanical and electrical duty

This product has been supplied to meet the per-
formance specifications of your purchase order, 
however it is understood that during the life of the 
product these may change. The following notes 
may help the user decide how to evaluate the 
implications of any change.

5.7.1 Specific gravity (SG)

Pump capacity and total head in meters (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.

5.7.2 Viscosity

For a given flow rate the total head reduces with 
increased viscosity and increases with reduced 
viscosity. Also for a given flow rate the power 
absorbed increases with increased viscosity, and 
reduces with reduced viscosity.

5.7.3 Pump speed

Changing pump speed effects flow, total head, 
power absorbed, NPSHR, noise and vibration. Flow 
varies in direct proportion to pump speed, head 
varies as speed ratio squared and power varies as 
speed ratio cubed. 
The new duty, however, will also be dependent on 
the system curve. If increasing the speed, it is 
important therefore to ensure the maximum 
pump working pressure is not exceeded, the driver 
is not overloaded, NPSHA > NPSHR, and that noise 
and vibration are within local requirements and 
regulations.

5.7.4 Pumped flow

Flow must not fall outside the minimum and maxi-
mum continuous safe flow shown on the pump 
performance curve and or data sheet.

5.8

Pumps for Food Use or Potable Water (ACS 
range)

If the pump has not been specifically ordered for a 
food or drinking water application it must not be 
used for these types of applications. If it has been 
ordered for this type of application the following 

Alarm and trip values for installed pumps 
should be based on the actual measure-
ments (N) taken on site on the bearing 
housings of the pump in the fully com-
missioned as new condition. Measuring 
vibration at regular intervals will then 
show any deterioration in pump or sys-
tem operating conditions.

Motor rating kW (hp)

Maximum stop/starts
per hour

Up to 15 (20)

15

Between 15 (20) and 90 (120)

10

90 (120) to 150 (200)

6

Above 150 (200)

Refer

Respect the starting frequency imposed 
by the motor manufacturer.

CAUTION!

CAUTION!

Close the outlet valve and stop the 
motor. Eventually close the inlet valve.

For prolonged shutdowns and especially 
when ambient temperatures are likely to 
drop below freezing point, the pump and 
any cooling and flushing arrangements 
must be drained or otherwise protected.

CAUTION!

CAUTION!

Summary of Contents for NPG 100-315

Page 1: ...GB Installation and operating instructions Wilo NPG 4095556 Ed_01_gb_0610_Wilo NL NLG NPG www promhimtech ru zakaz promhimtech ru...

Page 2: ...Quality Management System Standards as cer tified and audited by external Quality Assurance organizations Genuineparts andaccessories have been designed tested and incorporated into the products to he...

Page 3: ...us liquids 1 7 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 opera ting personnel to the noise The...

Page 4: ...e which travels through the walls and windows does not generate too high noise levels in the machine room s surroun dings 2 Transport and storage 2 1 Consignment receipt and unpacking Immediately afte...

Page 5: ...lar 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...

Page 6: ...ve when in contact with the pump motor unit and its working parts Important for other liquids consult us for preliminary advice The NPG type pump is a single stage pump with axial suction support unde...

Page 7: ...DN 250 DN 300 DN 350 DN 400 DN 500 200 4 6 250 4 4 6 6 300 4 6 315 8 8 12 12 350 4 6 355 8 8 12 12 400 8 8 8 12 12 12 450 8 12 500 16 10 10 10 6 5 4 15 15 15 10 6 650 6 5 10 NPG 200 315 37 4 12 NPG Ty...

Page 8: ...Put shims on the foundation surface approx 20 25 mm thick one on each side of the bolt hole as an alternative leveling screws can be used Lay the base plate and level in both directions with extra sh...

Page 9: ...ent observed on site is due to a wrong adjustment under the base plate disturbed during transport or because of forces exerted by the pipework It is only necessary to rectify the adjustment under base...

Page 10: ...r their sharing out on the pump flanges refer to standard NFCR 13 931 4 4 2 Suction piping 4 4 2 1 Design of a flooded suction line The suction line must be as short and direct as possible never mount...

Page 11: ...sure surge and from reverse rotation If necessary a control manometer can be connec ted on the pipework 4 4 4 Final checks a Check the tightening of anchor bolts Tighten them if necessary b Check that...

Page 12: ...See sections 5 5 4 and 5 5 5 If a defect of cooling can lead to temperature hig her than those acceptable a system of cooling surveillance must be installed Exceptwhenexplicitlyrequiredbythecustomerin...

Page 13: ...pump with the outlet valve closed for a period longer than 30 seconds If NO pressure or LOW pressure STOP the pump Refer to faultfinding chart for fault diagnosis The pump should run smoothly and wit...

Page 14: ...ne can present a danger to operators they must be shiel ded to avoid accidental contact If a 100 pro tection is not possible the machine access must be confined to the maintenance staff only If the te...

Page 15: ...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 t...

Page 16: ...rking on the pump take measures to prevent an uncontrolled start Put a warning board on the starting device with the words Machine under repair do not start With electric drive equipment lock the main...

Page 17: ...maintenance If after some time the leakage becomes too great the glandshouldbe tightened againin order to return these to a normal level If re tightening is not possible new packing must be installed...

Page 18: ...allic surfaces if necessary with preservative is recommended at 6 monthly intervals 6 4 Recommended spares and consumable items 1500 2250 3011 3012 4130 4610 Dimensions in millimeters Gland packing Pu...

Page 19: ...fer to sectional dra wings for part numbers and identifica tion CAUTION Trouble Possible Causes Solutions Insuffcient flowrate Pump or suction pipe not completely filled Check and complete filling Air...

Page 20: ...bubbles in pipes Check and desecrate the pipes Suction level too low Check the available NPSH the required NPSH Reduce geometrical suction lift Reduce head losses in pipes and in fit tings diameter in...

Page 21: ...ressure Rotation speed too low check the dri ver Check the connection in the terminal box according to the voltage Presence of air Check and de aerate Suction pressure insufficient Check the available...

Page 22: ...English Installation and maintenance instructions Wilo Horizontal pumps NPG 8 Parts list and drawings 8 1 Sectional drawings Pump NPG Bearing Size 32 42 Pump NPG Bearing Size 55...

Page 23: ...English 26 Wilo AG 09 2005 Bearing 55a and 55b Pump NPG Bearing Size 70...

Page 24: ...stem etc are provided as separate documents in their original format If further copies of these are required they should be obtained from the sup plier for retention with these User Instructions Parts...

Page 25: ...ique directive Niederspannungsrichtlinie 2006 95 EG Low voltage directive Directive basse tension und entsprechender nationaler Gesetzgebung and with the relevant national legislation et aux l gislati...

Page 26: ...EG EG EMV Elektromagnetisk kompatibilitet 2004 108 EG EG Lavspenningsdirektiv 2006 95 EG Anvendte harmoniserte standarder s rlig 1 FIN CE standardinmukaisuusseloste Ilmoitamme t ten ett t m laite vas...

Page 27: ...lint Budapest T 36 23 889500 wilo wilo hu Ireland WILO Engineering Ltd Limerick T 353 61 227566 sales wilo ie Italy WILO Italia s r l 20068 Peschiera Borromeo Milano T 39 25538351 wilo italia wilo it...

Page 28: ...00 T 01805 W I L O K D 9 4 5 6 5 3 F 0231 4102 7126 Erreichbar Mo Fr von 7 17 Uhr Wochenende und feiertags 9 14 Uhr elektronische Bereitschaft mit R ckruf Garantie Kundendienst Anforderung Werksrepara...

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