Dover PSG Wilden P1 Скачать руководство пользователя страница 11

 

WIL-10140-E-08

 

Wilden

®

 

11 

Suggested Installation, Operation, Maintenance and Troubleshooting 

 

The Pro-Flo

®

 model P1 has a 13 mm (1/2") inlet and 13 mm (1/2") outlet 

and is designed for flows to 56.8 lpm (15 gpm). The P1 Plastic pump is 
manufactured with wetted parts of pure, unpigmented PVDF, PTFE PFA 
or polypropylene. The P1 Plastic is constructed with a polypropylene 
center section. 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 13 mm (1/2") diameter or larger 
if highly viscous material is being pumped. The suction hose must be 
non-collapsible, reinforced type as the P1 is capable of pulling a high 
vacuum. Discharge piping should be at least 13 mm (1/2"); 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. 

 

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 s

hould 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 P1 Plastic models, a non-raised surfaced-flange adapter should 

be utilized when mating to the pump’s inlet and 

discharge manifolds 

for proper sealing. 
The P1 can be installed in submersible applications only when both 
the wetted and non-wetted portions are compatible with the material 
being pumped. If the pump is to be used in a submersible application, 

a hose shou

ld be attached to the pump’s air and pilot spool exhaust 

ports and piped above the liquid level. The exhaust area for the pilot 
spool is designed to be tapped for a 1/8" NPT fitting. 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. 
If the pump is to be used in a self-priming application, be sure that all 

connections are airtight and that the suction lift is within the model’s 

ability. Note: Materials of construction and elastomer material have 
an effect on suction lift parameters. Please consult Wilden distributors 
for specifics. 
The model P1 plastic will pass 1.6 mm (1/16") solids. Whenever the 
possibility exists that larger solid objects may be sucked into the pump. 

CAUTION:

 Do not exceed 8.6 bar (125 psig) air  

supply pressure. 

 

Section 6 

Содержание PSG Wilden P1

Страница 1: ...EOM ENGINEERING OPERATION MAINTENANCE P1 Clamped Plastic Pump WIL 10140 E 08 Where InnovationFlows ...

Страница 2: ...Fitted 8 P1 Plastic TPE Fitted 8 P1 Plastic PTFE Fitted 9 Suction Lift Curves 10 Section 6 Suggested Installation Operation 11 Maintenance and Troubleshooting Section 7 Disassembly Reassembly 14 Pump Disassembly 14 Single Piece Manifold Disassembly Reassembly 18 Air Valve Center Section Disassembly 20 Reassembly Hints Tips 22 Section 8 Exploded View and Parts List 24 P1 Plastic Rubber Fitted 24 P1...

Страница 3: ...lifornia 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 registered and unregistered trademarks of their respective owners Nothing contained in this document should be construed as granting any license or right to use any trademark without the prior written perm...

Страница 4: ...d result Pump valves and containers must be grounded to a proper grounding point when handling flammable fluids and whenever discharge of static electricity is a hazard CAUTION Do not exceed 8 6 bar 125 psig air supply pressure CAUTION The process fluid and cleaning fluids must be chemically compatible with all wetted pump components see E4 CAUTION Pumps should be thoroughly flushed before install...

Страница 5: ...0603 PFAcoated hardware Wil Gard II 110V 0102 Wil Gard II sensor wires ONLY hardware Wil Gard II sensor wires ONLY 0608 PFAcoated hardware Wil Gard II 220V 0103 Wil Gard II 220V 0530 Ultrapure II Wil Gard II 110V female 0612 Ultrapure PFA coated hardware 0206 PFA coated hardware connections male connections Wil Gard II sensor wires ONLY 0531 Ultrapure II female connections 0618 Ultrapure PFA coate...

Страница 6: ...ber 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 the pump discharge The movement of diaphragm A toward the center block of the pump creates a vacuum within liquid chamber A Atmospheric pressure forces fluid into the inlet manifold of the pump The inlet v...

Страница 7: ... P1 Plastic DIMENSIONS ITEM METRIC mm STANDARD inch A 31 1 2 B 130 5 1 C 196 7 7 D 208 8 2 E 218 8 6 F 56 2 2 G 114 4 5 H 127 5 0 J 203 8 0 K 145 5 7 L 114 4 5 M 84 3 3 N 102 4 0 P 8 0 3 R 20 0 8 S 28 1 1 DIMENSIONAL DRAWING ...

Страница 8: ...e pumps should be specified so that daily operation parameters will fall in the center of the pump performance curve P1 PLASTIC TPE FITTED Height 218 mm 8 6 Width 208 mm 8 2 Depth 203 mm 8 0 Est ShipWeight Polypropylene 4 kg 9 lbs PVDF 5 kg 11 lbs PTFE PFA 6 kg 12 lbs Air Inlet 6 mm 1 4 Inlet 13 mm 1 2 Outlet 13 mm 1 2 Suction Lift 5 8 m Dry 19 9 8 m Wet 32 Disp Per Stroke1 0 11 l 0 030 gal Max Fl...

Страница 9: ...1 6 mm 1 16 1 Displacement per stroke was calculated at 4 8 bar 70 psig air inlet pressure against a 2 bar 30 psig head pressure Example To pump 18 9 lpm 5 gpm against a discharge pressure head of 2 8 bar 40 psig requires 3 9 bar 56 psig and 6 93 Nm3 h 4 1 scfm air consumption See dot on chart Caution Do not exceed 8 6 bar 125 psig air supply pressure Flow rates indicated on chart were determined ...

Страница 10: ...g at 305 m 1 000 above sea level This chart is meant to be a guide only There are many variables which can affect your pump s operating characteristics The number of intake and discharge elbows viscosity of pumping fluid elevation atmospheric pressure and pipe friction loss all affect the amount of suction lift your pump will attain ...

Страница 11: ...und 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 possib...

Страница 12: ...by limiting the 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 throttling the pump discharge by partially closing a valve in the discharge line of the pump This action increases friction loss which reduces flow rate See Section 5 This is useful when the ne...

Страница 13: ...ol 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 chambers 2 Verify that vacuum required to lift liquid is not greater than the vapor pressure of the material being pumped cavitation 3 Checkforstickingballcheckvalves Ifmaterialbeing pumped is not compati...

Страница 14: ...bers is molded of polypropylene or acetal All fasteners and hardware are stainless steel and the air valve is manufactured of brass or high tech engineered thermoplastic Its air distribution system is based on a revolutionary design which offers economical reliability and performance The model P1 Plastic is available in injection molded polypropylene PVDF and PTFE PFA wetted parts PLEASE read all ...

Страница 15: ... performance PTFE o rings should be replaced when reassembled Step 5 Remove and inspect the ball retainer retainer o ring and valve ball from the bottom of the liquid chamber Check for nicks gouges chemical attack or abrasive wear Replace worn parts with genuine Wilden parts for reliable performance PTFE o rings should be replaced when reassembled Step 6 Normally the inlet and discharge manifold s...

Страница 16: ...mbled Step 8 Use a 11 mm 7 16 wrench to remove one set of clamp bands that secure one liquid chamber to the one piece center section Step 9 Lift the liquid chamber away from the center section to expose the diaphragm and outer piston Step 10 Using an adjustable wrench or by rotating the diaphragm by hand remove the diaphragm assembly from the center section ...

Страница 17: ...sc spring separate from the shaft which remains connected to the opposite side diaphragm assembly PTFE fitted pumps come standard with back up diaphragms not shown NOTE Disc spring not shown on Figure 11B Step 12 To remove the diaphragm assembly from the shaft secure shaft with soft jaws a vise fitted with plywood or other suitable material to ensure shaft is not nicked scratched or gouged Using a...

Страница 18: ...onsisting of center block and air chambers is molded from glass filled acetal on conductive models All fasteners and hardware are stainless steel The primary diaphragm is constructed of PTFE All wetted sealing o rings are PTFE encapsulated FKM on the UPII The standard air distribution system is used on the UPII All o rings used in the pump are of a special material and should only be replaced with...

Страница 19: ... the seat and seat o ring from the water chamber for further inspection If swelling cracking or other damage is apparent these parts must be replaced Step 4 Loosen and remove clamp bands from around the inlet manifold Step 5 Lift center section off of the inlet mani fold It is now possible to inspect the outboard o rings on the inlet manifold Step 6 Place center section upside down on a flat surfa...

Страница 20: ...stic P1 utilizes a revolutionary Pro Flo air distribution 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 P1 to run lube free Constructed of acetal or polypropylene the Pro Flo air distribution system is designed to perform in on off non freezing non stalling tough duty applications NOTE Replace...

Страница 21: ...ing snap ring on both sides of center section with snap ring pliers Step 7 Remove pilot spool sleeve from center section Step 8 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 and other signs of wear Replace pilot sleeve assembly or outer sleeve o rings if necessary During...

Страница 22: ...a proper sealing surface This is most easily accomplished by placing them on a flat surface prior to tightening their clamp bands to the desired torque see this page for torque specs Be sure to tighten outer pistons simultaneously on PTFE fitted pumps to ensure proper torque values Ensure proper mating of liquid chambers to manifolds prior to tightening vertical bolts Overhang should be equal on b...

Страница 23: ...he adhesive strip remains attached to the PTFE tape and is not removed with the adhesive covering Step 2 Starting at any point place the PTFE tape directly on top of the diaphragm bead Press lightly on the tape to ensure that the adhesive holds it in place during assembly Do not stretch the tape during placement on the diaphragm bead Step 3 The end of the tape should overlap approximately 13 mm 1 ...

Страница 24: ...WIL 10140 E 08 Wilden 24 Exploded View and Parts Listing P1 PLASTIC RUBBER FITTED EXPLODED VIEW Section 8 ...

Страница 25: ... 01 6802 08 17 Inner Piston 2 01 3711 08 01 3711 08 18 Outer Piston 2 01 4570 20 500 01 4570 20 500 19 Liquid Chamber 2 01 5000 20 01 5000 21 20 Manifold Tee Section 2 01 5160 20 01 5160 21 21 Inlet Manifold Elbow 2 01 5220 20 01 5220 21 22 Discharge Manifold Elbow 2 01 5230 20 01 5230 21 23 Screw SHCS Chamber Bolt 4 01 6080 03 01 6080 03 24 Vertical Bolt Washer 4 01 6730 03 01 6730 03 25 Vertical...

Страница 26: ...WIL 10140 E 08 Wilden 26 Exploded View and Parts Listing P1 PLASTIC PTFE FITTED EXPLODED VIEW ...

Страница 27: ...Chamber 2 01 5000 20 01 5000 20 01 5000 21 01 5000 21 20 Manifold Tee Section 2 01 5160 20 01 5160 20 01 5160 21 01 5160 21 21 Inlet Manifold Elbow 2 01 5220 20 01 5220 20 01 5220 21 01 5220 21 22 Discharge Manifold Elbow 2 01 5230 20 01 5230 20 01 5230 21 01 5230 21 23 Screw SHCS Chamber Bolt 4 01 6080 03 01 6080 05 01 6080 03 01 6080 05 24 Vertical Bolt Washer 4 01 6730 03 01 6730 05 01 6730 03 ...

Страница 28: ... 53 Wil Flex 01 1010 58 01 1080 58 00 1260 58 00 1260 58 Saniflex 01 1010 56 01 1080 56 01 1200 56 01 1300 56 PTFE3 01 1010 55 01 1080 55 PTFE with integral piston 01 1030 55 PVDF 01 1120 21 500 PTFE Encapsulated FKM 01 1205 60 01 1300 60 500 1Must be used with part number 01 5010 21 500 PTFE diaphragms require Neoprene back up diaphragms P N 01 1060 51 P1 Ultrapure pump series require high temp B...

Страница 29: ...WIL 10140 E 08 Wilden 29 Notes ...

Страница 30: ...WIL 10140 E 08 Wilden 30 Notes ...

Страница 31: ...WIL 10140 E 08 Wilden Notes ...

Страница 32: ...d 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 prior notice This is a non contractual document 05 2018 ...

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