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WIL-10187-E-03

 

Wilden

®

 

12 

Suggested Installation, Operation, Maintenance and Troubleshooting 

 

The P8 pump has a 51 mm (2") inlet and 51 mm (2") outlet and is designed for flows 

to 587 lpm (155 gpm). The P8 pump is manufactured with wetted parts of pure, 
unpigmented PVDF or polypropylene. A variety of diaphragms and O-rings are 
available to satisfy temperature, chemical compatibility, abrasion and flex concerns. 
The suction pipe size should be at least 51 mm (2") diameter or larger if highly 
viscous material is being pumped. The suction hose must be non-collapsible, 
reinforced type as the P8 pump is capable of pulling a high vacuum. Discharge 
piping should be at least 51 mm (2"); larger diameter can be used to reduce friction 
losses. It is critical that all fittings and connections are airtight or a reduction or loss of 

pump suction capability will result. 
For P8 plastic models, Wilden offers 68 kg (150 lb) flanges. The following details 
should be noted when mating these to pipe works: 

 

A 60

80 shore gasket that covers the entire flange face should be used 

 

The gasket should be between 1.91 mm (0.075") and 4.45 mm (0.175") 

thickness 

 

Mating flanges with flat as opposed to raised surfaces should be used for 
proper mechanical sealing 

 

The flanges should be tightened to aminimum of 6.8 N·m (5 ft-lb) but no 
more than 13.5 N·m (10 ft-lb)  

CAUTION: 

All fittings and connections must be airtight. Otherwise, pump 

suction capability will be reduced or lost.

 

Months of careful planning, study and selection efforts can result in unsatisfactory 
pump performance if installation details are left to chance. You can avoid 
premature failure and long-term dissatisfaction by exercising reasonable care 
throughout the installation process

.

 

Location

 

Noise, safety and other logistical factors usually dictate where equipment will be 
situated on the production floor. Multiple installations with conflicting 
requirements can result in congestion of utility areas, leaving few choices for 
additional pumps. 
Within the framework of these and other existing conditions, every pump should 
be located in such a way that several key factors are balanced against each 
other to maximum advantage. 

 

Access: 

First of all, the location should be accessible. If it’s easy to 

reach the pump, maintenance personnel will have an easier time 
carrying out routine inspections and adjustments. Should major repairs 
become necessary, ease of access can play a key role in speeding the 
repair process and reducing total downtime. 

 

Air Supply: 

Every pump location should have an air line large enough to 

supply the volume of air necessary to achieve the desired pumping rate. 
Use air pressure up to a maximum of 8.6 bar (125 psig) depending on 
pumping requirements. 

For best results, the pumps should use a 5μ (micron) air filter, needle 

valve and regulator. The use of an air filter before the pump will ensure 
that the majority of any pipeline contaminants will be eliminated. 

 

Solenoid Operation: 

When operation is controlled by a 

solenoid valve in the air line, three-way valves should be used. 
This valve allows trapped air between the valve and the pump 
to bleed off which improves pump performance. Pumping 
volume can be estimated by counting the number of strokes 

per minute and then multiplying the figure by the displacement 
per stroke. 

 

Muffler: 

Sound levels are reduced below OSHA specifications 

using the standard Wilden muffler. Other mufflers can be used 
to further reduce sound levels, but they usually reduce pump 

performance. 

 

Elevation: 

Selecting a site that is well within the pump’s 

dynamic-lift capability will assure that loss-of-prime issues will 
be eliminated. In addition, pump efficiency can be adversely 
affected if proper attention is not given to site location. 

 

Piping: 

Final determination of the pump site should not be 

made until the piping challenges of each possible location have 

been evaluated. The impact of current and future installations 
should be considered ahead of time to make sure that 
inadvertent restrictions are not created for any remaining sites. 

The best choice possible will be a site involving the shortest and 
straightest hook-up of suction and discharge piping. Unnecessary 

elbows, bends and fittings should be avoided. Pipe sizes should be 
selected to keep friction losses within practical limits. All piping 
should be supported independently of the pump. In addition, the 
piping should be aligned to avoid placing stress on the pump fittings. 

Flexible hose can be installed to aid in absorbing the forces created 
by the natural reciprocating action of the pump. If the pump is to be 

bolted down to a solid location, a mounting pad placed between the 
pump and the foundation will assist in minimizing pump vibration. 
Flexible connections between the pump and rigid piping will also 
assist in minimizing pump vibration. If quick-closing valves are 
installed at any point in the discharge system, or if pulsation within a 
system becomes a problem, a surge suppressor (SD Equalizer

®

should be installed to protect the pump, piping and gauges from 
surges and water hammer. 

NOTE:

 Materials of construction and elastomer material 

have an effect on suction-lift parameters. Please refer to the 
performance section for specifics. 

When pumps are installed in applications involving flooded suction or 
suction-head pressures, a gate valve should be installed in the 
suction line to permit closing of the line for pump service. 
For P8 pumps, a non-raised surfaced-flange adapter should be 

utilized when mating to the pump’s inlet and discharge manifolds for 

proper sealing. 
Pumps in service with a positive suction head are most efficient 
when inlet pressure is limited to 0.5

0.7 bar (7

10 psig). Premature 

diaphragm failure may occur if positive suction is 0.7 bar (10 psig) 
and higher. 
The P8 will pass 6.4 mm (1/4") solids. whenever the possibility exists 
that larger solid objects may be sucked into the pump, a strainer 

should be used on the suction line. 

CAUTION:

 Do not exceed 8.6 bar (125 psig) air  

supply pressure. 

CAUTION: DO NOT EXCEED 8.6 BAR (125 PSIG) AIR SUPPLY 
PRESSURE.

 

 

Section 6 

Содержание WILDEN PRO-FLO P8

Страница 1: ...EOM ENGINEERING OPERATION MAINTENANCE P8 Clamped Plastic Pump WIL 10187 E 03 Where InnovationFlows...

Страница 2: ...troke PTFE Fitted 9 P8 Plastic Full Stroke PTFE Fitted 9 P8 Plastic Ultra FlexTM Fitted 9 Suction Lift Curves 10 Section 6 Suggested Installation Operation 11 Maintenance and Troubleshooting Section 7...

Страница 3: ...ifornia LLC Wil Flex is a trademark of PSG California LLC Saniflex is a trademark of PSG California LLC All trademarks names logos and service marks collectively trademarks in this document are regist...

Страница 4: ...y be forced out air exhaust Plastic series pumps are made of virgin plastic and are not UV stabilized Direct sunlight for prolonged periods can cause deterioration of plastics WARNING Prevent static s...

Страница 5: ...POLYPROPYLENE VALVE SEAT O RING BN BUNA N Red Dot PU POLYURETHANE Brown TV PTFE ENCAP FKM WF WIL FLEX Santoprene NOTE Most Elastomeric materials use colored dots for identification NOTE Not all models...

Страница 6: ...hamber and mani fold of the pump These same hydraulic forces lift the discharge valve ball off its seat while the opposite discharge valve ball is forced onto its seat forcing fluid to flow through th...

Страница 7: ...STANDARD inch A 490 19 3 B 76 3 0 C 414 16 3 D 693 27 3 E 770 30 3 F 89 3 5 G 417 16 4 H 333 13 1 J 381 15 0 K 307 12 1 L 227 8 9 M 254 10 0 N 15 0 6 METRIC mm STANDARD inch P 122 DIA 4 8 DIA R 152 D...

Страница 8: ...mps should be specified so that daily operation parameters will fall in the center of the pump s performance curve P8 PLASTIC TPE FITTED Ship Weight Polypropylene 34 kg 75 lb PVDF 43 kg 95 lb Air Inle...

Страница 9: ...d performance pumps should be specified so that daily operation parameters will fall in the center of the pump s performance curve P8 PLASTIC FULL STROKE PTFE FITTED Ship Weight Polypropylene 34 kg 75...

Страница 10: ...was calculated at 4 8 bar 70 psig air inlet pressure against a 2 bar 30 psig head pressure Example To pump 257 lpm 68 gpm against a discharge pressure head of 2 0 bar 30 psig requires 4 1 bar 60 psig...

Страница 11: ...g at 305 m 1 000 above sea level This chart is meant to be a guide only There are many variables that can affect your pump s operating characteristics The number of intake and discharge elbows viscosi...

Страница 12: ...eration When operation is controlled by a solenoid valve in the air line three way valves should be used This valve allows trapped air between the valve and the pump to bleed off which improves pump p...

Страница 13: ...he volume and or pressure of the air supply to the pump An air regulator is used to regulate air pressure A needle valve is used to regulate volume Pump discharge rate can also be controlled by thrott...

Страница 14: ...l to be unable toshift 7 Remove plug from pilot spoolexhaust Pump runs but little or no product flows 1 Check for pump cavitation slow pump speed down to allow thick material to flow into liquid chamb...

Страница 15: ...tribution system is based on a revolutionary design which increases reliability and performance The model P8 are available in injection molded polypropylene PLEASE read all directions before starting...

Страница 16: ...able performance Step 5 Remove the two small clamp bands which fasten the intake manifold to the liquid chambers Step 6 Lift intake manifold from liquid chambers and center section to expose intake va...

Страница 17: ...uter piston diaphragm and inner piston remain attached to the shaft and the entire assembly can be removed from the center section Figure 12 2 The outer piston diaphragm and inner piston separate from...

Страница 18: ...istribution system A 13 mm 1 2 air inlet connects the air supply to the center section Proprietary composite seals reduce the coefficient of friction and allow the P4 to run lube free The Pro Flo air...

Страница 19: ...from center block Step 9 With O ring pick gently remove the o ring from the opposite side of the center hole cut on the spool Gently remove the pilot spool from sleeve and inspect for nicks or gouges...

Страница 20: ...Large Clamp Band Rubber Fitted 18 6 N m 165 in lb Large Clamp Band PTFE Fitted 18 6 N m 165 in lb Air Chamber Screws HSFHS 3 8 16 47 5 N m 35 ft lb Figure A INSTALLATION The following tools can be use...

Страница 21: ...g surfaces must be properly aligned in order to ensure positive sealing characteristics Step 1 Gently remove the adhesive covering from the back of the PTFE tape Ensure that the adhesive strip remains...

Страница 22: ...WIL 10187 E 03 Wilden 22 Exploded View and Parts Listing P8 PLASTIC FULL STROKE DIAPHRAGM FITTED EXPLODED VIEW Section 8...

Страница 23: ...n 2 08 3700 01 08 3700 01 21 Diaphragm 2 22 Outer Piston 2 08 4550 21 500 08 4550 21 500 23 Manifold Tee Section 2 08 5160 20 08 5160 20 24 Small Clamp Band Assy 4 08 7100 03 500 08 7100 05 500 25 Sma...

Страница 24: ...WIL 10187 E 03 Wilden 24 Exploded View and Parts Listing P8 PLASTIC REDUCED STROKE DIAPHRAGM FITTED EXPLODED VIEW...

Страница 25: ...Ring 2 04 3890 03 04 3890 03 20 Inner Piston 2 08 3750 01 08 3750 01 Inner Piston Ultra Flex 2 08 3761 01 08 3761 01 21 Diaphragm Back up 2 22 Diaphragm 2 23 Outer Piston 2 08 4600 21 500 08 4600 21...

Страница 26: ...N A N A EPDM 08 1010 54 08 1020 54 N A N A 08 1080 54 N A N A FKM 08 1010 53 08 1020 53 N A N A 08 1080 53 N A N A Saniflex 08 1010 56 N A N A N A 08 1080 56 08 1060 56 08 1065 56 PTFE 08 1010 55 N A...

Страница 27: ...WIL 10187 E 03 Wilden Notes...

Страница 28: ...Terrace CA 92313 5651 USA P 1 909 422 1730 F 1 909 783 3440 psgdover com Where Innovation Flows PSG reserves the right to modifythe information and illustrations contained in this document without pr...

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