excess lubrication will reduce pump performance.
Pump is pre-lubed.
TEMPERATURE LIMITS:
Acetal –29°C to 82°C –20°F to 180°F
Buna-N –12°C to 82°C 10°F to 180°F
Geolast
®
–40°C to 82°C –40°F to 180°F
Neoprene –18°C to 93°C 0°F to 200°F
Nordel
®
EPDM –51°C to 138°C –60°F to 280°F
Nylon –18°C to 93°C 0°F to 200°F
PFA –7°C to 107°C 45°F to 225°F
Polypropylene 0°C to 79°C 32°F to 175°F
Polyurethane –12°C to 66°C 10°F to 150°F
PVDF –12°C to 107°C 10°F to 225°F
Saniflex™ –29°C to 104°C –20°F to 220°F
SIPD PTFE
SIPD PTFE
PTFE
Viton
with
EPDM-backed 4°C to 137°C 40°F to 280°F
with
Neoprene-backed
1
4°C to 104°C 40°F to 220°F
®
FKM –40°C to 177°C –40°F to 350°F
4°C to 93°C 40°F to 200°F
Wil-Flex™ –40°C to 107°C –40°F to 225°F
1
4°C to 149°C (40°F to 300°F) - 13 mm (1/2") and 25 mm (1") models only.
NOTE: Not all materials are available for all models.
Refer to Section 2 for material options for your
pump.
CAUTION: When choosing pump materials, be
sure to check the temperature limits for all wetted
components. Example: Viton® has a maximum limit
of 177°C (350°F) but polypropylene has a maximum
limit of only 79°C (175°F).
CAUTION:
upon mechanical stress only. Certain chemicals
will significantly reduce maximum safe operating
temperatures. Consult Chemical Resistance Guide for
chemical compatibility and temperature limits.
Maximum temperature limits are based
CAUTION: The process fluid and cleaning fluids
must be chemically compatible with all wetted
pump components. Consult Chemical Resistance
Guide.
CAUTION: Pumps should be thoroughly flushed
before installing into process lines. FDA- and
USDA-approved pumps should be cleaned and/or
sanitized before being used.
CAUTION: Always wear safety glasses when
operating pump. If diaphragm rupture occurs,
material being pumped may be forced out air
exhaust.
CAUTION: Before any maintenance or repair is
attempted, the compressed air line to the pump
should be disconnected and all air pressure
allowed to bleed from pump. Disconnect all intake,
discharge and air lines. Drain the pump by turning
it upside down and allowing any fluid to flow into a
suitable container.
CAUTION: Blow out air line for 10 to 20 seconds
before attaching to pump to make sure all pipeline
debris is clear. Use an in-line air filter. A 5μ (micron)
air filter is recommended.
NOTE: When installing PTFE diaphragms, it is
important to tighten outer pistons simultaneously
(turning in opposite directions) to ensure tight fit.
(See torque specifications in Section 7.)
NOTE: Cast Iron PTFE-fitted pumps come standard
from the factory with expanded PTFE gaskets
installed in the diaphragm bead of the liquid
chamber. PTFE gaskets cannot be re-used.
NOTE: Before starting disassembly, mark a line
from each liquid chamber to its corresponding air
chamber. This line will assist in proper alignment
during reassembly.
WARNING: Prevent static sparking. If static sparking
occurs, fire or explosion could 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.
WIL-10184-E- 01 1 WILDEN PUMP & ENGINEERING, LLC
CAUTION: Pro-Flo® pumps cannot be used in
submersible applications.
CAUTION : Tighten all hardware prior to installation.
Page 4
Section 2
WILDEN PUMP DESIGNATION SYSTEM
P8 METAL
51 mm (2") Pump
Maximum Flow Rate:
630 lpm (166 gpm)
MODEL
P8 = PRO-FLO
WETTED PARTS & OUTER PISTON
AA = ALUMINUM / ALUMINUM
SS = STAINLESS STEEL /
STAINLESS STEEL
WW = CAST IRON / CAST IRON
AIR CHAMBERS
A = ALUMINUM
C = PTF E-COATED
N = NICKEL-PLATED
S = STAINLESS STEEL
V = HAL AR®-COATED
[Santoprene® (Two Black Dots) ]
NE = NEOPRENE (Green Dot)
PU = POLYURE THANE (Clear)
TF = P TFE ( White)
VT = VITON® (Silver
or White Dot)
WF = WIL-F LEX ™
1,2,3
[Santoprene®- (Three Black
Dots)]
DIAPHRAGMS
VALVE BALLS
1,3
1,2, 3
1,2,3
1,3
O-RINGS
VALVE SE ATS
SPECIALT Y
CODE
(if applicable)
VALVE SE ATS
A = ALUMINUM
BN = BUNA-N (Red Dot)
EP = EPDM (Blue Dot)
SANIFLE X™ [Hytrel® (Cream)]
FS =
F W =
SA NITA RY W IL-F LE X ™
[Santoprene® (Two Black Dots) ]
H = A LLOY C
M = MILD S TEEL
NE = NEOPRENE (Green Dot)
PU = POLYURE THANE (Clear)
S = S TAINLESS S TEEL
VT = VITON® (Silver
or White Dot)
WF = WIL-F LEX ™
[Santoprene (Three Black
Dots)]
VALVE SEAT O-RINGS
TF = PTF E
NOTE:
1
Meets Requirements of FDA CFR21.177
2
Meets Requirements of USP Class VI
3
Meets Requirements of 1935/2004/EC
1,2,3
1,3
SPECIALTY CODES
0014 BSP
0023 Wing nuts
0030 Screen based
0036 Screen based, BSP
0039 Screen based, polyurethane screen
0044 Stallion, balls & seats ONLY
0047 Stallion externals, balls and seats
0070 Saniflo™ FDA
0075 Saniflo™ FDA, Stallion balls and seats ONLY
0079 Tri-clamp fittings, wing nuts
0080 Tri-clamp fittings ONLY
NOTE: MOST E LAS TOMERIC MATERIA LS USE COLORED DOT S FOR IDENTIFICATION.
NOTE: Not all models are available wi th all material options.
®
Viton
are registered trademarks of DuPont Dow Elastomers.
Saniflo™ FDA, Stallion balls and seats ONLY (1935/2004/EC)
0075
E
Saniflo™ FDA, Wil-Gard II™ 110V (1935/2004/EC)
0120
Page 5
Section 3
HOW IT WORKS—PUMP
The Wilden diaphragm pump is an air-operated, positive displacement, self-priming pump. These drawings show flow pattern
through the pump upon its initial stroke. It is assumed the pump has no fluid in it prior to its initial stroke.
FIGUR E 1 The air valve dire cts pre ssurized
air to the back side of diaphragm A. The
compressed air is applied directly to the
liquid column separated by elastomeric
diaphragms. The diaphragm acts as
a separation membrane between the
compressed air and liquid; a balanced
load removes mechanical stress from the
diaphragm. The compressed air moves
the diaphragm away from the center
of the pump. The opposite diaphragm
is pulled in by the shaft connected to
the pressurized diaphragm. Diaphragm
B is on its suction stroke; air behind
the diaphragm has been forced out to
atmosphere through the exhaust por t of
the pump. The movement of diaphragm
B toward the center of the pump creates
a vacuum within chamber B. Atmos pheric
pressure forces fluid into the inlet
manifold forcing the inlet valve ball off its
seat. Liquid is free to move past the inlet
valve ball and fill the liquid chamber (see
shaded area).
HOW IT WORKS—AIR DISTRIBUTION SYSTEM
FIGURE 2 When the pressurized diaphragm,
diaphra gm A, re aches t he limit of it s disc harge
stroke, the air valve redirects pressurized
air to the back side of diaphragm B. The
pressurized air forces diaphragm B away
from the center while pulling diaphragm A
to the center. Diaphragm B is now on its
discharge stroke. Diaphragm B forces the
inlet valve ball onto its seat due to the
hydraulic forces developed in the liquid
chamber and manifold 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 of the pump creates a
vacuum within liquid chamber A. Atmospheric pressure forces fluid into the inlet
manifold of the pump. The inlet valve ball
is forced off its seat allowing the fluid being
pumped to fill the liquid chamber.
FIGURE 3 At completion of the stroke,
the air valve again redirec ts air to the
back side of diaphragm A, which star ts
diaphragm B on its exhaust stroke. As
the pump reaches its original star ting
point, each diaphragm has gone through
one exhaust and one discharge stroke.
This constitutes one complete pumping
cycle. The pump may take several cycles
to completely prime depending on the
conditions of the application.
The Pro-Flo
two moving par ts: the air valve spool and the pilot spool. The
heart of the system is the air valve spool and air valve. This
valve design incorporates an unbalanced spool. The smaller
end of the spool is pressurized continuously, while the large
end is alternately pressurized then exhausted to move the
spool. The spool directs pressurized air to one air chamber
while exhausting the other. The air causes the main shaft/
diaphragm assembly to shift to one side — discharging
liquid on that side and pulling liquid in on the other side.
When the shaf t reaches the end of its stroke, the inner piston
actuates the pilot spool, which pressurizes and exhausts the
large end of the air valve spool. The repositioning of the air
valve spool routes the air to the other air chamber.
316 Stainless Steel 51 kg (112 lb)
Cast Iron 47 kg (104 lb)
Alloy C 52 kg (114 lb)
Air Inlet ...................................13 mm (1/2”)
Inlet ............................................51 mm (2”)
Outlet .........................................51 mm (2”)
Suction Lift ..................... 6.9 m Dr y (22.7’)
8.6 m Wet (28.4’)
Disp. per Stroke1 ................. 2.6 L (0.70 gal)
Max. Flow Rate ............ 623 lpm (165 gpm)
Max. Size Solids .................. 6.4 mm (1/4”)
1
Displacement per stroke was calculated
at 4.8 bar (70 psig) air inlet pressure
against a 2.1 bar (30 psig) head pressure.
Example: To pump 386 lpm (102 gpm)
against a discharge head of 2.8 bar (40
psig) requires 5.5 bar (80 psig) and 137
Nm3/h (85 scfm) air consumption.
CAUTION : Do not exceed 8.6 bar (125
psig) air supply pressure.
Flow rates indicated on chart were determined by pumping water.
For optimum life and performance, pumps should be specified so that daily operation
parameters will fall in the center of the pump's performance curve.
P8 METAL
TPE-FITTED
Ship Weight .........Aluminum 32 kg (70 lb)
316 Stainless Steel 51 kg (112 lb)
Cast Iron 47 kg (104 lb)
Alloy C 52 kg (114 lb)
Air Inlet ...................................13 mm (1/2”)
Inlet ............................................51 mm (2”)
Outlet .........................................51 mm (2”)
Suction Lift ......................6.7 m Dry (22.1’)
8.6 m Wet (28.4’)
Disp. per Stroke
Max. Flow Rate ............ 630 lpm (166 gpm)
Max. Size Solids .................. 6.4 mm (1/4”)
1
Displacement per stroke was calculated
at 4.8 bar (70 psig) air inlet pressure
against a 2.1 bar (30 psig) head pressure.
Example: To pump 227 lpm (60 gpm)
against a discharge head of 3.4 bar (50
psig) requires 4.1 bar (60 psig) and 66
Nm3/h (41 scfm) air consumption.
CAUTION : Do not exceed 8.6 bar (125
psig) air supply pressure.
1
.................2.8 L (0.75 gal)
Flow rates indicated on chart were determined by pumping water.
For optimum life and performance, pumps should be specified so that daily operation
parameters will fall in the center of the pump's performance curve.
WIL-10184-E- 015 WILDEN PUMP & ENGINEERING, LLC
Page 8
Section 5A
PERFORMANCE
P8 METAL
REDUCED-STROKE PTFE-FITTED
Ship Weight .........Aluminum 32 kg (70 lb)
316 Stainless Steel 51 kg (112 lb)
Cast Iron 47 kg (104 lb)
Alloy C 52 kg (114 lb)
Air Inlet ................................... 13 mm (1⁄ 2")
Inlet ............................................ 51 mm (2")
Outlet ......................................... 51 mm (2")
Suction Lift ......................4.6 m Dry (15.0')
9.5 m Wet (31.0')
Disp. per Stroke
Max. Flow Rate ............ 496 lpm (131 gpm)
Max. Size Solids ................... 6.4 mm (1/4")
1
Displacement per stroke was calculated
at 4.8 bar (70 psig) air inlet pressure
against a 2.1 bar (30 psig) head pressure.
Example: To pump 238 lpm (63 gpm)
against a discharge pressure head of
2.1 bar (30 psig) requires 4.1 bar (60 psig)
and 94 Nm3/h (55 scfm) air consumption.
CAUTION : Do not exceed 8.6 bar (125
psig) air supply pressure.
1
...............1.67 L (0.44 gal)
Flow rates indicated on chart were determined by pumping water.
For optimum life and performance, pumps should be specified so that daily operation
parameters will fall in the center of the pump's performance curve.
P8 METAL
FULL-STROKE PTFE-FITTED
Ship Weight ........Aluminum 32 kg (70 lb)
316 Stainless Steel 51 kg (112 lb)
Cast Iron 47 kg (104 lb)
Alloy C 52 kg (114 lb)
Air Inlet ...................................13 mm (1/2”)
Inlet ............................................51 mm (2”)
Outlet .........................................51 mm (2”)
Suction Lift ......................6.7 m Dry (22.1’)
9.0 m Wet (29.5’)
Disp. per Stroke
Max. Flow Rate ............ 618 lpm (163 gpm)
Max. Size Solids .................. 6.4 mm (1/4”)
1
Displacement per stroke was calculated
at 4.8 bar (70 psig) air inlet pressure
against a 2.1 bar (30 psig) head pressure.
Example: To pump 280 lpm (74 gpm)
against a discharge head of 2.8 bar (40
psig) requires 4.1 bar (60 psig) and 87
Nm3/h (54 scfm) air consumption.
CAUTION : Do not exceed 8.6 bar (125
psig) air supply pressure.
1
................. 2.6 L (0.70 gal)
Flow rates indicated on chart were determined by pumping water.
For optimum life and performance, pumps should be specified so that daily operation
parameters will fall in the center of the pump's performance curve.
WILDEN PUMP & ENGINEERING, LLC 6 WIL-10184-E- 01
Page 9
PERFORMANCE
P8 METAL
ULTRA-FLEX™-FITTED
Ship Weight .........Aluminum 32 kg (70 lb)
316 Stainless Steel 51 kg (112 lb)
Cast Iron 47 kg (104 lb)
Alloy C 52 kg (114 lb)
Air Inlet ................................... 13 mm (1/2")
Inlet ............................................ 51 mm (2")
Outlet ......................................... 51 mm (2")
Suction Lift ......................4.9 m Dry (16.0')
8.8 m Wet (29.0')
Disp. per Stroke
Max. Flow Rate ............ 526 lpm (139 gpm)
Max. Size Solids ................... 6.4 mm (1/4")
1
Displacement per stroke was calculated
at 4.8 bar (70 psig) air inlet pressure
against a 2.1 bar (30 psig) head pressure.
Example: To pump 201 lpm (53 gpm)
against a discharge pressure head of
2.1 bar (30 psig) requires 4.1 bar (60 psig)
and 60 Nm3/h (35 scfm) air consumption.
CAUTION : Do not exceed 8.6 bar (125
psig) air supply pressure.
1
............... 2.12 L (0.56 gal)
Flow rates indicated on chart were determined by pumping water.
For optimum life and performance, pumps should be specified so that daily operation
parameters will fall in the center of the pump's performance curve.
WIL-10184-E- 017 WILDEN PUMP & ENGINEERING, LLC
Page 10
Section 5A
SUCTION-LIFT CURVES
P8 METAL SUCTIONLIFT CAPABILITY
Suction-lift curves are calibrated for pumps operating
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, viscosity
of pumping fluid, elevation (atmospheric pressure)
and pipe friction loss all affect the amount of suction
lift your pump will attain.
WILDEN PUMP & ENGINEERING, LLC 8 WIL-10184-E- 01
Page 11
Section 6
SUGGESTED INSTALLATION
Wilden pumps are designed to meet the performance
requirements of even the most demanding pumping
applications. They have been designed and manufactured
to the highest standards and are available in a variety of
liquid path materials to meet your chemical resistance
needs. Refer to the performance section of this manual for
an in-depth analysis of the performance characteristics of
your pump. Wilden offers the widest variety of elastomer
options in the industry to satisfy temperature, chemical
compatibility, abrasion resistance and flex concerns.
The suction pipe size should be at least the equivalent or
larger than the diameter size of the suction inlet on your
Wilden pump. The suction hose must be non-collapsible,
reinforced type as these pumps are capable of pulling a high
vacuum. Discharge piping should also be the equivalent
or larger than the diameter of the pump discharge which
will help reduce friction losses. It is critical that all fittings
and connections are airtight or a reduction or loss of pump
suction capability will result.
INSTALLATION: Months of careful planning, study,
and selection efforts can result in unsatisfactory pump
performance if installation details are left to chance.
Premature failure and long-term dissatisfaction can be
avoided if reasonable care is exercised 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 the
following 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. Bleed port is to be left open unless being
used with the submersible option.
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.
If the pump is to be used in a self-priming application, make
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 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.
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.
NOTE: Pro-Flo
ALL WILDEN PUMPS ARE CAPABLE OF PASSING SOLIDS.
A STRAINER SHOULD BE USED ON THE PUMP INTAKE TO
ENSURE THAT THE PUMP'S RATED SOLIDS CAPACITY IS
NOT EXCEEDED.
CAUTION: DO NOT EXCEED 8.6 BAR (125 PSIG) AIR
SUPPLY PRESSURE.
®
and Accu-Flo™ pumps are not submersible.
®
)
WIL-10184-E- 019 WILDEN PUMP & ENGINEERING, LLC
Page 12
FOOTPAD
Section 5A
SUGGESTED INSTALLATION
This illustration is a generic
representation of an air-operated
double-diaphragm pump.
MUFFLER
FLEXIBLE
CONNECTION
SUCTION
EQUALIZER
SURGE DAMPENER
(OPTIONAL)
GAUGE
(OPTIONAL)
SHUT-OFF
VALVE
FLEXIBLE
CONNECTION
NOTE: In the event of a power failure, the shut-off valve
should be closed, if the restarting of the pump is not
desirable once power is regained.
COMBINATION
FILTER & REGULATOR
AIR SHUT-OFF VALVE
AIR-OPERATED PUMPS: To stop the pump from operating
in an emergency situation, simply close the shut-off valve
(user-supplied) installed in the air supply line. A properly
functioning valve will stop the air supply to the pump,
therefore stopping output. This shut-off valve should be
located far enough away from the pumping equipment
such that it can be reached safely in an emergency
situation.
WILDEN PUMP & ENGINEERING, LLC 10 WIL-10184-E- 01
Page 13
SUGGESTED OPERATION & MAINTENANCE
OPERATION: The P8 pumps are pre-lubricated, and do
not require in-line lubrication. Additional lubrication
will not damage the pump, however if the pump is
heavily lubricated by an external source, the pump’s
internal lubrication may be washed away. If the pump
is then moved to a non-lubricated location, it may need
to be disassembled and re-lubricated as described in
the DISASSEMBLY/REASSEMBLY INSTRUCTIONS.
Pump discharge rate can be controlled 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 need exists to control the pump
from a remote location. When the pump discharge
pressure equals or exceeds the air supply pressure,
the pump will stop; no bypass or pressure relief valve
is needed, and pump damage will not occur. The
pump has reached a “deadhead” situation and can be
TROUBLESHOOTING
restarted by reducing the fluid discharge pressure or
increasing the air inlet pressure. The Wilden P8 pumps
run solely on compressed air and do not generate
heat, therefore your process fluid temperature will not
be affected.
MAINTENANCE AND INSPECTIONS: Since each
application is unique, maintenance schedules may
be different for every pump. Frequency of use, line
pressure, viscosity and abrasiveness of process fluid
all affect the parts life of a Wilden pump. Periodic
inspections have been found to offer the best
means for preventing unscheduled pump downtime.
Personnel familiar with the pump’s construction and
service should be informed of any abnormalities that
are detected during operation.
RECORDS: When service is required, a record should
be made of all necessary repairs and replacements.
Over a period of time, such records can become a
valuable tool for predicting and preventing future
maintenance problems and unscheduled downtime. In
addition, accurate records make it possible to identify
pumps that are poorly suited to their applications.
Pump will not run or runs slowly.
1. Ensure that the air inlet pressure is at least 0.4 bar
(5 psig) above startup pressure and that the differential
pressure (the difference between air inlet and liquid
discharge pressures) is not less than 0.7 bar (10 psig).
2. Check air inlet filter for debris (see SUGGESTED
INSTALLATION).
3. Check for extreme air leakage (blow by) that would
indicate worn seals /bores in the air valve, pilot
spool and main shaft.
4. Disassemble pump and check for obstructions in
the air passageways or objects that would obstruct
the movement of internal parts.
5. Check for sticking ball check valves. If material being
pumped is not compatible with pump elastomers,
swelling may occur. Replace ball check valves and
seals with proper elastomers. Also, as the check
valve balls wear out, they become smaller and can
become stuck in the seats. In this case, replace balls
and seats.
6. Check for broken inner piston that will cause the air
valve spool to be unable to shift.
7. Remove plug from pilot spool exhaust.
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.
WIL-10184-E- 01 11 WILDEN PUMP & ENGINEERING, LLC
2. Verify that vacuum required to lif t liquid is not
greater than the vapor pressure of the material
being pumped (cavitation).
3. Check for sticking ball check valves. If material being
pumped is not compatible with pump elastomers,
swelling may occur. Replace ball check valves and
seats with proper elastomers. Also, as the check
valve balls wear out, they become smaller and can
become stuck in the seats. In this case, replace balls
and seats.
Pump air valve freezes.
1. Check for excessive moisture in compressed
air. Either install a dryer or hot air generator for
compressed air. Alternatively, a coalescing filter
may be used to remove the water from the
compressed air in some applications.
Air bubbles in pump discharge.
1. Check for ruptured diaphragm.
2. Check tightness of outer pistons (refer to Section 7).
3. Check tightness of fasteners and integrity of O-rings
and seals, especially at intake manifold.
4. Ensure pipe connections are airtight.
Product comes out air exhaust.
1. Check for diaphragm rupture.
2. Check tightness of outer pistons to shaft.
Page 14
Section 7
PUMP DISASSEMBLY
Tools Required:
• 1/2" Wrench
• 9/16" Wrench
• 11/16" Wrench
• Adjustable Wrench
• Vise equipped w/
soft jaws (such as
plywood, plastic
or other suitable
material)
CAUTION: Before any maintenance or repair is attempted, the compressed air line
to the pump should be disconnected and all air pressure allowed to bleed from the
pump. Disconnect all intake, discharge and air lines. Drain the pump by turning it
upside down and allowing any fluid to flow into a suitable container. Be aware of
any hazardous effects of contact with your process fluid.
NOTE: The model photographed for these instructions incorporates rubber
diaphragms, balls and seats. Models with PTFE diaphragms, balls and seats are
the same except where noted.
Step 1
Before starting disassembly, mark
a line from each liquid chamber to
its corresponding air chamber. This
line will assist in proper alignment
during reassembly.
WILDEN PUMP & ENGINEERING, LLC 12 WIL-10184-E- 01
Step 2
Utilizing a 1/2" wrench, remove
the two (2) small clamp bands that
fasten the discharge manifold to
the liquid chambers.
Step 3
Remove the discharge manifold to
expose the valve balls and seats.
Inspect ball cage area of manifold
for excessive wear or damage.
Page 15
PUMP DISASSEMBLY
Step 4
Remove the discharge valve balls
and seats from the liquid chambers
and inspect for nicks, chemical
attack or abrasive wear. Replace
worn parts with genuine Wilden
parts for reliable performance.
Step 5
Remove the two (2) small clamp
bands which fasten the intake
manifold to the liquid chambers.
Step 6
Lift liquid chambers and center
section from intake manifold to
expose intake valve balls and
seats. Inspect ball cage area of
liquid chamber for excessive wear
or damage.
Step 7
Remove one (1) set of large clamp
bands which secure one (1) liquid
chamber to the center section.
WIL-10184-E- 01 13 WILDEN PUMP & ENGINEERING, LLC
Step 8
Lift liquid chamber away from
center section to expose diaphragm
and outer piston.
Step 9A
Using an adjustable wrench, or by
rotating the diaphragm by hand,
remove the diaphragm assembly.
NOTE: Due to varying torque
values, one of the following two
situations may occur: 1) The outer
piston, diaphragm and inner piston
remain attached to the shaft and the
entire assembly can be removed
from the center section.
Page 16
PUMP DISASSEMBLY
Step 9B
2) The outer piston, diaphragm and
inner piston separate from the shaft
which remains connected to the
opposite side diaphragm assembly.
Repeat disassembly instructions
for the opposite liquid chamber.
Inspect diaphragm assembly and
shaft for signs of wear or chemical
attack. Replace all worn parts with
genuine Wilden parts for reliable
performance.
Step 10
To remove diaphragm assembly
from shaf t, secure shaft with sof t
jaws (a vise fitted with plywood,
plastic or other suitable material)
to ensure shaft is not nicked,
scratched or gouged. Using
an adjustable wrench, remove
diaphragm assembly from shaft.
WILDEN PUMP & ENGINEERING, LLC 14 WIL-10184-E- 01
Page 17
AIR VALVE / CENTER SECTION DISASSEMBLY
Tools Required:
• 3/16" Hex-Head Wrench
• 1/4" Hex-Head Wrench
• Snap-Ring Pliers
• O-Ring Pick
CAUTION: Before any maintenance or repair is attempted, the compressed air line
to the pump should be disconnected and all air pressure allowed to bleed from the
pump. Disconnect all intake, discharge and air lines. Drain the pump by turning it
upside down and allowing any fluid to flow into a suitable container. Be aware of
hazardous effects of contact with your process fluid.
®
The Wilden P8 metal pump utilizes a revolutionary Pro-Flo
air distribution system.
Proprietary composite seals reduce the co efficient of friction and allow lube-free
®
operation. The Pro-Flo
air distribution system is designed to perform in on/off,
Loosen the air valve bolts utilizing
a 3/16" hex-head wrench and then
remove muffler plate screws.
Step 2
Remove muffler plate and air valve
bolts from air valve assembly
exposing muffler gasket for
Step 3
Lift away air valve assembly
and remove air valve gasket for
inspection. Replace if necessary.
inspection. Replace if necessary.
WIL-10184-E- 01 15 WILDEN PUMP & ENGINEERING, LLC
Page 18
AIR VALVE / CENTER SECTION DISASSEMBLY
Step 4
Remove air valve end cap to expose
air valve spool by simply lifting up
on end cap once air valve bolts are
removed.
Step 7
Remove air chamber bolts with
1/4" hex-head wrench.
WILDEN PUMP & ENGINEERING, LLC 16 WIL-10184-E- 01
Step 5
Remove air valve spool from air
valve body by threading one air
valve bolt into the end of the spool
and gently sliding the spool out of
the air valve body. Inspect seals for
signs of wear and replace entire
assembly if necessary. Use caution
when handling air valve spool to
prevent damaging seals.
NOTE: Seals should not be
removed from assembly. Seals are
not sold separately.
Step 8
Remove pilot spool bushing from
center block.
Step 6
Remove pilot spool retaining snap
ring on both sides of center section
with snap-ring pliers.
Step 9
With O-ring pick, gently remove the
O-ring from the opposite side of the
notched end of 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 re-assembly never
insert the pilot spool into the sleeve
with the “notched" end side first, this
end incorporates the urethane O-ring
and will be damaged as it slides over
the ports cut in the sleeve.
NOTE: Seals should not be
removed from pilot spool. Seals
are not sold separately.
Page 19
AIR VALVE / CENTER SECTION DISASSEMBLY
A
Step 10A
Check center block shaf t seals for
signs of wear. If necessary, remove
shaft seals with O-ring pick and
replace.
Step 10B
NOTE: Threaded sleeves (see 10A)
are removable and can be replaced
if necessary. Sleeves can be press
fit by hand.
WIL-10184-E- 01 17 WILDEN PUMP & ENGINEERING, LLC
Page 20
REASSEMBLY HINTS & TIPS
RE A SSE M B LY:
Upon performing applicable maintenance to the air
distrib ution system, t he pump can now be re assembled .
Please refer to the disassembly instructions for photos
and parts placement. To reassemble the pump, follow
the disassembly instructions in reverse order. The air
distribution system needs to be assembled first, then
the diaphragms and finally the wetted path. Please find
the applicable torque specifications on this page. The
following tips will assist in the assembly process.
• Lubricate air valve bore, center section shaft
and pilot spool bore with NLGI grade 2 white EP
bearing grease or equivalent.
• Clean the inside of the center section shaft bore to
ensure no damage is done to new shaft seals.
• A small amount of NLGI grade 2 white EP bearing
grease can be applied to the muffler and air valve
gaskets to locate gaskets during assembly.
• Make sure that the exhaust port on the muffler plate
is centered between the two exhaust ports on the
center section.
• Stainless bolts should be lubed to reduce the
possibility of seizing during tightening.
• Use a mallet to tamp lightly on the large clamp
bands to seat the diaphragm before tightening.
PRO-FLO® MAXIMUM TORQUE SPECIFICATIONS
Description of PartTorque
Air Valve5.1 N•m (45 in-lb)
Air Chamber/Center Block47.5 N•m (35 ft-lb)
Outer Pistons, Rubber & PTFE, Excluding
Steel Inner Pistons
Outer Pistons, Ultra-Flex™74.6 N•m (55 ft-lb)
Small Clamp Bands6.6 N•m (58 in-lb)
Large Clamp Bands (Rubber-Fitted)47.5 N•m (35 ft-lb)
Large Clamp Bands (PTFE-Fitted)47.5 N•m (35 ft-lb)
106 N•m (78 ft-lb)
119 N•m (88 ft-lb)
SHAFT SEAL INSTALLATION:
PRE-INSTALLATION
• Once all of the old seals have been removed, the
inside of the bushing should be cleaned to ensure
no debris is left that may cause premature damage
to the new seals.
INSTALLATION
The following tools can be used to aid in the installation
of the new seals:
• Wrap electrical tape around each leg of the needle-nose
pliers (heat shrink tubing may also be used). This is done
to prevent damaging the inside surface of the new seal.
• With a new seal in hand, place the two legs of the
needle-nose pliers inside the seal ring. (See Figure A.)
• Open the pliers as wide as the seal diameter will allow,
then with two fingers pull down on the top portion of
the seal to form a kidney shape. (See Figure B.)
• Lightly clamp the pliers together to hold the seal into
the kidney shape. Be sure to pull the seal into as tight
of a kidney shape as possible, this will allow the seal to
travel down the bushing bore easier.
• With the seal clamped in the pliers, insert the seal into
the bushing bore and position the bottom of the seal
into the correct groove. Once the bottom of the seal is
seated in the groove, release the clamp pressure on the
pliers. This will allow the seal to partially snap back to its
original shape.
• After the pliers are removed, you will notice a slight
bump in the seal shape. Before the seal can be properly
resized, the bump in the seal should be removed as
much as possible. This can be done with either the
Phillips screwdriver or your finger. With either the side
of the screwdriver or your finger, apply light pressure
to the peak of the bump. This pressure will cause the
bump to be almost completely eliminated.
• Lubricate the edge of the shaft with
white EP bearing grease.
• Slowly insert the center shaft with a rotating motion.
This will complete the resizing of the seal.
• Perform these steps for the remaining seals.
NLGI grade 2
Figure B
Figure A
WILDEN PUMP & ENGINEERING, LLC 18 WIL-10184-E- 01
SHA FT SE AL
SHA FT SE AL
TAPE
NEEDLE-NOSE
PLIERS
TAPE
Page 21
GASKET KIT INSTALLATION
Carefully prepare sealing surfaces by removing all
debris and foreign matter from diaphragm bead
and all mating surfaces. If necessary, smooth or
Step 1
Gently remove the adhesive
covering from the back of the PTFE
tape. Ensure that the adhesive strip
remains attached to the PTFE tape.
Step 2
Starting at any point, place the PTFE
tape in the center of the diaphragm
bead groove on the liquid chamber
and pres s lightly on the tape to en sure
that the adhesive holds in place
during assembly. Do not stretch the
tape during placement in the center
of diaphragm bead groove.
deburr all sealing surfaces. Mating surfaces must
be properly aligned in order to ensure positive
sealing characteristics.
Step 3
The end of the tape should overlap
approximately 13 mm (1/2").
Proceed to install the PTFE tape on
the remaining liquid chamber.
WIL-10184-E- 01 19 WILDEN PUMP & ENGINEERING, LLC
Page 22
Section 8
EXPLODED VIEW & PARTS LISTING
P8 METAL
Full-Stroke Diaphragm-FittedEXPLODED VIEW
FULL-STROKE PTFE-FITTED
ALL CIRCLED PART IDENTIFIERS ARE INCLUDED IN REPAIR KITS (see Section 9).
Center Block includes item number 15.
BSP-fitted pumps are available. Contact your distributor for part numbers.
For optional P8 Metal Pump elastomers, see Section 9.
0070 Specialty Code = Saniflo
FDA
*See Section 9 — Elastomer Chart
All bold face items are primary wear parts.
WIL-10184-E- 0121WILDEN PUMP & ENGINEERING, LLC
Page 24
EXPLODED VIEW & PARTS LISTING
P8 METAL
Reduced-Stroke Diaphragm-FittedEXPLODED VIEW
2521222024
ULTRA-FLEX™
ALL CIRCLED PART IDENTIFIERS ARE INCLUDED IN REPAIR KITS (see Section 9).
Manifold, Footed Inlet Tri-Clamp
24Large Clamp Band Assembly208-7300-03-70
25Screw, HHC Large (3/8”-16 x 3”)408-6120-03
26Wing Nut, Large Clamp Band (3/8”-16)408-6671-10
27Washer, Brass Flat (Ø.392” x Ø.875” x .063”)408-6720-07-70
28Small Clamp Band Assembly408-7100-03-70
29RHSN Bolt, Small Clamp Band (5/16”-18 x 1-1/2”)808-6050-03
30Wing Nut, Small Clamp Band (5/16”-18)808-6661-10
31Washer, Brass Flat (Ø.340” x Ø.750” x .063”)808-6700-07-70
STATEMENT OF COMPLIANCE TO REGULATIONS (EC) NO 1935/2004
ON MATERIALSAND ARTICLES INTEDNDED TO COME INTO CONTACT WITH FOOD
(asper Article 16 of EGULATION (EC) No 1935/2004)
Wilden Pump &Engineering,LLC,22069 Van Buren Street, Grand Terrace, CA92313-5607 USA,certifies as the manufacturer thattheAir-Operated Double Diaphragm pumps listed below complywith the European CommunityRegulation 1935/2004/(EC)for Food Contact Materials.
Materialsused in equipment thatare intended to contact food belongto the groupsofmaterialslisted in Annex1 (EC) 1935/2004 (List ofgroups ofmaterialsand articles which may be covered by specificmeasures)
5) Rubbers
8) Metal and Alloy10) Plastics
Compliance is subject to material and equipment storage, handling and usage recommended byWilden in the engineering operation andmaintenance manual and supplemental technicalpublications.
This declaration is based on the following information:
Statementsof raw material suppliers
Wilden will make available to the competent authorities appropriate documentation to demonstrate compliance
Approved By:
Chris DistasoDirector of EngineeringDate:July 5,2017
Page 30
NOTES
Page 31
WARRANTY
Each and every product manufactured by Wilden Pump and Engineering, LLC is built to meet the highest
standards of quality. Every pump is functionally tested to insure integrity of operation.
Wilden Pump and Engineering, LLC warrants that pumps, accessories and parts manufactured or supplied by
it to be free from defects in material and workmanship for a period of five (5) years from date of installation or
six (6) years from date of manufacture, whichever comes first. Failure due to normal wear, misapplication, or
abuse is, of course, excluded from this warranty.
Since the use of Wilden pumps and parts is beyond our control, we cannot guarantee the suitability of any pump
or part for a particular application and Wilden Pump and Engineering, LLC shall not be liable for any consequential
damage or expense arising from the use or misuse of its products on any application. Responsibility is limited
solely to replacement or repair of defective Wilden pumps and parts.
All decisions as to the cause of failure are the sole determination of Wilden Pump and Engineering, LLC.
Prior approval must be obtained from Wilden for return of any items for warranty consideration and must be
accompanied by the appropriate MSDS for the product(s) involved. A Return Goods Tag, obtained from an
authorized Wilden distributor, must be included with the items which must be shipped freight prepaid.
The foregoing warranty is exclusive and in lieu of all other warranties expressed or implied (whether written or oral)
including all implied warranties of merchantability and fitness for any particular purpose. No distributor or other
person is authorized to assume any liability or obligation for Wilden Pump and Engineering, LLC other than expressly
provided herein.
PLEASE PRINT OR TYPE AND FAX TO WILDEN
PUMP INFORMATION
Item # Serial #
Company Where Purchased
YOUR INFORMATION
Company Name
Industry
Name Title
Street Address
City State Postal Code Country
Telephone Fax E-mail Web Address
Number of pumps in facility? Number of Wilden pumps?
Types of pumps in facility (check all that apply): Diaphragm
Media being pumped?
Other
Centrifugal
Gear
Submersible
Lobe
How did you hear of Wilden Pump?
Other
Trade Journal
Trade Show
Internet/ E-mail
Distributor
ONCE COMPLETE, FAX TO (909) 783-3440
OR GO TO PSGDOVER.COM > WILDEN > SUPPORT TO COMPLETE THE WARRANTY REGISTRATION ONLINE
NOTE: WARRANTY VOID IF PAGE IS NOT FAXED TO WILDEN OR SUBMIT TED ONLINE VIA THE PSGDOVER.COM WEBSITE
WILDEN PUMP & ENGINEERING, LLC
Page 32
PSG
22069 Van Buren St., Grand Terrace, CA 92313-5607
P: +1 (909) 422-1730
• F: +1 (909) 783-3440
wildenpump.com
Where Innovation Flows
PSG® reserves the right to modify the information and illustrations contained in this document without prior notice. This is a non-contractual document. 07-2018