CAUTION: Do not apply compressed air to the exhaust
port — pump will not function.
CAUTION: Do not, under any circumstance loosen the set
screw located at the adjuster dial of the Pro-Flo X ™ pump.
If the set screw is loose when the pump is pressurized, it
could eject and cause injury to anyone in the area.
CAUTION : Do not over-lubricate air supply — excess
lubrication will reduce pump performance. Pump is pre-
.
lubed.
TEMPERATURE LIMITS:
Polypropylene 0°C to 79°C 32°F to 175°F
PVDF –12°C to 107°C 10°F to 225°F
PFA 7°C to 107°C 20°F to 225°F
Neoprene –18°C to 93°C 0°F to 200°F
Buna-N –12°C to 82°C 10°F to 180°F
EPDM –51°C to 138°C –60°F to 280°F
Viton
®
FKM –40°C to 177°C –40°F to 350°F
Wil-Flex™ –40°C to 107°C –40°F to 225°F
Saniflex™ –29°C to 104°C –20°F to 220°F
Polyurethane –12°C to 66°C 10°F to 150°F
Polytetrafluoroethylene (PTFE)1 4°C to 104°C 40°F to 220°F
Nylon –18°C to 93°C 0°F to 200°F
Acetal –29°C to 82°C –20°F to 180°F
SIPD PTFE
SIPD PTFE
with
Neoprene-backed
with
EPDM-backed –10°C to 137°C 14°F to 280°F
4°C to 104°C 40°F to 220°F
Polyethylene 0°C to 70°C 32°F to 158°F
Geolast
1
®
–40°C to 82°C –40°F to 180°F
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 (3 50°F) but
polypropylene has a maximum limit of only 79°C (175°F).
CAUTION: Maximum temperature limits are based upon
mechanical stress only. Certain chemicals will significantly
reduce maximum safe operating temperatures. Consult
Chemical Resistance Guide (E4) for chemical compatibilit y
and temperature limits.
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.
CAUTION: The process fluid and cleaning fluids must be
chemically compatible with all wet ted pump components.
Consult Chemical Resistance Guide (E4).
CAUTION: Do not exceed 82°C (180°F) air inlet
temperature for Pro-Flo X™ models.
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: Bef ore any maintenance or repair i s attemp ted,
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. Consult PS-TG for installation instructions
during reassembly.
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.
CAUTION: Pro-Flo® pumps cannot be used in
submersible applications. Pro-Flo X ™ is available in both
single-point exhaust (submersible) and standard (nonsubmersible) options. Do not use standard Pro-Flo X™
models in submersible applications. Turbo-Flo
®
pumps
are also available in a single-point exhaust (submersible)
configuration.
CAUTION: Tighten all hardware prior to installation.
WIL-11540-E-01 1 WILDEN PUMP & ENGINEERING, LLC
Page 4
Section 2
WILDEN PUMP DESIGNATION SYSTEM
PX820/PX830 METAL
51 mm (2") Pump
Maximum Flow Rate:
674 lpm (178 gpm)
MATERIAL CODES
MODEL
PX8 20 = PRO-FLO X™
XPX820 = PRO-FLO X™ ATE X
PX8 30 = PRO-FLO X™
XPX83 0 = PRO-FLO X™ ATE X
WETTED PARTS & OUTER PISTON
AA = ALUMINUM / ALUMINUM
SS = STAINLESS STEEL
AIR CHAMBERS
A = ALUMINUM
C = PTF E-COAT ED
N = NICKEL-PL ATED
S = STAINLESS S TEEL
t
CENTER BLOCK
A = ALUMINUM
N = NICKEL-PL ATED
P = POLYPROPYLENE
S = STAINLESS S TEEL
AIR VALVE
A = ALUMINUM
N = NICKEL-PL ATED
P = POLYPROPYLENE
S = STAINLESS S TEEL
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, balancing the
load and removing 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
port of the pump. The movement of
diaphragm B toward the center of the
pump creates a vacuum within chamber B.
Atmospheric 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
(diaphragm A), reaches the limit of its
discharge stroke, the air valve redirec ts
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
forc es the inlet valve b all onto its se at 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 redirects air to the
back side of diaphragm A, which starts
diaphragm B on its exhaust stroke. As
the pump reaches its original starting
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.
WIL-11540-E-013 WILDEN PUMP & ENGINEERING, LLC
The Pro-Flo
moving parts: 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 direc ts
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 shaft 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.
Each dial setting
represents an
entirely different
flow curve.
Pro-Flo X™ pumps
are shipped from
the factory on
setting 4, which
is the highest
flow rate setting
possible.
Moving the dial
from setting 4
causes a decrease
in flow and an even
greater decrease in
air consumption.
AIR CONSUMPTION
$
$
$
When the air
consumption
decreases more
than the flow
rate, efficiency
is improved and
operating costs
are reduced.
Page 11
Example 1
HOW TO USE THIS EMS CURVE
SETTING 4 PERFORMANCE CURVE
Figure 1Figure 2
Example data point = Example data point =
This is an example showing how to determine flow rate and
air consumption for your Pro-Flo X™ pump using the Efficien
cy Management System (EMS) curve and the performance
curve. For this example we will be using 4.1 bar (60 psig) inlet
air pressure and 2.8 bar (40 psig) discharge pressure and EMS
setting 2.
Step 1:
Identifying performance at setting 4. Locate
the curve that represents the flow rate of the
pump with 4.1 bar (60 psig) air inlet pressure.
Mark the point where this curve crosses the
horizontal line representing 2.8 bar (40 psig)
discharge pressure (Figure 1). After locating
your performance point on the flow curve,
draw a vertical line downward until reaching
the bottom scale on the chart. Identify the flow
rate (in this case, 8.2 gpm). Observe location
of performance point relative to air consumption curves and approximate air consumption
value (in this case, 9.8 scfm).
8.2
GPM
-
curve, draw vertical lines downward until
reaching the bottom scale on the chart. This
identifies the flow X Factor (in this case, 0.58)
and air X Factor (in this case, 0.48).
Step 3:
Calculating performance for specific EMS
setting. Multiply the flow rate (8.2 gpm)
obtained in Step 1 by the flow X Factor multiplier (0.58) in Step 2 to determine the flow rate
at EMS setting 2. Multiply the air consumption (9.8 scfm) obtained in Step 1 by the air
X Factor multiplier (0.48) in Step 2 to determine the air consumption at EMS setting 2
(Figure 3).
8.2
gpm
.58
4.8
gpm
0.58
0.48
(flow rate for setting 4)
(flow X Factor setting 2)
(flow rate for setting 2)
EMS CURVE
flow multiplier
air multiplier
Step 2:
Determining flow and air X Factors. Locate
your discharge pressure (40 psig) on the vertical axis of the EMS curve (Figure 2). Follow
along the 2.8 bar (40 psig) horizontal line until
intersecting both flow and air curves for your
desired EMS setting (in this case, setting 2).
Mark the points where the EMS curves intersect the horizontal discharge pressure line.
After locating your EMS points on the EMS
The flow rate and air consumption at setting
2 are found to be 18.2 lpm (4.8 gpm) and 7.9
Nm3/h (4.7 scfm) respectively.
(air X Factor setting 2)
scfm
(air consumption for setting 2)
Page 12
HOW TO USE THIS EMS CURVE
Example 2.1
SETTING 4 PERFORMANCE CURVE
Figure 4
Example data point =
This is an example showing how to determine the inlet air
pressure and the EMS setting for your Pro-Flo X™ pump to
optimize the pump for a specific application. For this exam
ple we will be using an application requirement of 18.9 lpm
(5 gpm) flow rate against 2.8 bar (40 psig) discharge pressure.
This example will illustrate how to calculate the air consump
tion that could be expected at this operational point.
10.2
gpm
-
-
DETERMINE EMS SETTING
Step 1
: Establish inlet air pressure. Higher air pres-
sures will typically allow the pump to run
more efficiently, however, available plant air
pressure can vary greatly. If an operating
pressure of 6.9 bar (100 psig) is chosen when
EMS Flow
Settings 1 & 2
0.49
In our example it is 38.6 lpm (10.2 gpm). This
is the setting 4 flow rate. Observe the location of the performance point relative to air
consumption curves and approximate air
consumption value. In our example setting
4 air consumption is 24 Nm3/h (14 scfm).
(See figure 4.)
Step 3
: Determine flow X Factor. Divide the required
flow rate 18.9 lpm (5 gpm) by the setting 4 flow
rate 38.6 lpm (10.2 gpm) to determine the flow
X Factor for the application.
5
gpm / 10.2 gpm = 0.49 (flow X Factor)
EMS CURVE
Figure 5
flow multiplier
plant air frequently dips to 6.2 bar (90 psig)
Step 4
pump performance will vary. Choose an operating pressure that is within your compressed
air system's capabilities. For this example we
will choose 4.1 bar (60 psig).
: Determine EMS setting from the flow
X Factor. Plot the point representing the flow
X Factor (0.49) and the application discharge
pressure 2.8 bar (40 psig) on the EMS curve.
This is done by following the horizontal 2.8
Step 2
: Determine performance point at setting 4. For
this example an inlet air pressure of 4.1 bar
(60 psig) inlet air pressure has been chosen.
Locate the curve that represents the performance of the pump with 4.1 bar (60 psig) inlet
air pressure. Mark the point where this curve
crosses the horizontal line representing 2.8
bar (40 psig) discharge pressure. After locating this point on the flow curve, draw a vertical line downward until reaching the bottom
scale on the chart and identify the flow rate.
bar (40 psig) discharge pressure line until it
crosses the vertical 0.49 X Factor line. Typically, this point lies between two flow EMS setting curves (in this case, the point lies between
the flow curves for EMS setting 1 and 2). Observe the location of the point relative to the
two curves it lies between and approximate
the EMS setting (Figure 5). For more precise
results you can mathematically interpolate between the two curves to determine the optimal EMS setting.
Determine air consumption at a specific
EMS setting.
Step 1
: Determine air X Factor. In order to determine
the air X Factor, identify the two air EMS setting curves closest to the EMS setting established in example 2.1 (in this case, the point
lies between the air curves for EMS setting
1 and 2). The point representing your EMS
setting (1.8) must be approximated and plotted on the EMS curve along the horizontal
line representing your discharge pressure (in
this case, 40 psig). This air point is different
than the flow point plotted in example 2.1. After estimating (or interpolating) this point on
the curve, draw a vertical line downward until reaching the bottom scale on the chart and
identify the air X Factor (Figure 7).
EMS CURVE
EMS Air
Settings 1 & 2
Figure 7
Example data point =
Step 2
: Determine air consumption. Multiply your
setting 4 air consumption (14 scfm) value by
the air X Factor obtained above (0.40) to determine your actual air consumption.
1
4 scfm x 0.40 = 5.6 SCFM
In summary, for an application requiring 18.9 lpm
(5 gpm) against 2.8 bar (40 psig) discharge pressure,
the pump inlet air pressure should be set to 4.1 bar
(60 psig) and the EMS dial should be set to 1.8. The
pump would then consume 9.5 Nm3/h (5.6 scfm) of
compressed air.
Displacement per stroke was calculated at 4.8 bar (70 psig)
Max. Flow Rate .............615 lpm (162.5 gpm)
air inlet pressure against a 2.1 bar (30 psig) head pressure.
Max. Size Solids ..................6.4 mm (1/4”)
1
Page 24
SUCTION-LIFT CURVES
PX820/PX830 ALUMINUM
SUCTION-LIFT 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 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.
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 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.
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.
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
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.
SUBMERSIBLE APPLICATIONS: Pro-FloX™ pumps can
be used for submersible applications, when using the
Pro-Flo X™ single-point exhaust option. Turbo-Flo™ pumps
are also available in a single-point exhaust (submersible)
configuration.
®
NOTE: Pro-Flo
point exhaust option and are not submersible.
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 do not have a single-
®
) should be installed
WILDEN PUMP & ENGINEERING, LLC 24 WIL-11540-E-01
Page 27
SUGGESTED INSTALLATION
This illustration is a generic
representation of an air-operated
double-diaphragm pump.
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.
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.
WIL-11540-E-01 25 WILDEN PUMP & ENGINEERING, LLC
Page 28
SUGGESTED OPERATION & MAINTENANCE
OPERATION: The PX820/PX830 is 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 PX820/
PX830 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 of fer 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) which
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 which 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 which 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.
WILDEN PUMP & ENGINEERING, LLC 26 WIL-11540-E-01
2. Verify that vacuum required to lift 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 29
Section 7
PUMP DISASSEMBLY
Tools Required:
• Appropriate-sized
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 may vary depending on materials of
construction, elastomer options and specialty codes selected.
Step 1
Please note alignment marks on
liquid chambers. Use to properly
align center section to liquid
chambers.
WIL-11540-E-01 27 WILDEN PUMP & ENGINEERING, LLC
Step 2
Using an appropriately-sized
wrench, loosen the discharge
manifold from the liquid chambers.
Step 3
Remove the discharge manifold to
expose the valve balls and valve
seats. Inspect ball cage area of
manifold for excessive wear or
damage.
Page 30
PUMP DISASSEMBLY
Step 4
After removing discharge valve
balls and valve seats from the
discharge manifold and liquid
chamber, inspect for nicks, gouges,
chemical attack or abrasive wear.
NOTE: Replace worn parts with
genuine Wilden parts for reliable
performance.
Step 5
Using an appropriately-sized
wrench, loosen the inlet manifold
from the liquid chambers.
NOTE: Inverting the pump will
facilitate removal of inlet manifold.
Step 6
Remove the inlet manifold to expose
the valve balls and valve seats.
Step 7
Remove the inlet valve balls and
valve seats from the inlet manifold
and inspect for nicks, gouges,
chemical attack or abrasive wear.
WILDEN PUMP & ENGINEERING, LLC 28 WIL-11540-E-01
Step 8
Using an appropriately-sized
wrench, remove the liquid chamber
from the center section.
Step 9
The liquid chamber should be
removed to expose the diaphragm
and outer piston using an adjustable
wrench. Remove the diaphragm
assembly from the center section.
Repeat for opposite side.
Page 31
PUMP DISASSEMBLY
Step 10
After loosening and removing
the outer piston, the diaphragm
assembly can be disassembled.
Step 11
To remove diaphragm assembly
from shaft, secure shaft with soft
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.
WIL-11540-E-01 29 WILDEN PUMP & ENGINEERING, LLC
Page 32
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 PX820/PX830 Advanced FIT metal pump utilizes the Pro-Flo X™ air distribution
system. Proprietary composite seals reduce the co efficient of friction and allow the
PX820/PX830 to run lube-free. Constructed of acetal, polypropylene or aluminum,
the Pro-Flo X™ air distribution system is designed to perform in on/off, nonfreezing, non-stalling, tough duty applications.
Step 1
Using a 3/16" hex-head wrench,
loosen air valve bolts.
WILDEN PUMP & ENGINEERING, LLC 30 WIL-11540-E-01
Step 2
Remove muffler plate and air valve
bolts from air valve assembly
exposing muffler gasket for
inspection. Replace if necessary.
Step 3
Lift away air valve assembly
and remove air valve gasket for
inspection. Replace if necessary.
Page 33
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. NOTE: Pro-Flo X™ air
valve incorporates an end cap at
both ends of the air valve.
Step 5
Remove the air valve spool from
the air valve body by threading one
air valve bolt into the end of the
air valve 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 6
Remove pilot sleeve retaining snap
ring on both sides of center section
with snap ring pliers.
NOTCHED
END
Step 7
Remove pilot spool sleeve from
center section.
WIL-11540-E-01 31 WILDEN PUMP & ENGINEERING, LLC
Step 8
Using an O-ring pick, gently remove the O-ring from the opposite side of the
notched end on one side of the pilot spool. Gently remove the pilot spool
from pilot spool sleeve and inspect for nicks, gouges and wear. Replace
pilot sleeve or outer sleeve O-rings if necessary. During re-assembly,
never insert the pilot spool into the sleeve with the notched end 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 34
AIR VALVE / CENTER SECTION DISASSEMBLY
Step 9
Check center section shaft seals for
signs of wear. If necessary, remove
the shaft seals with O-ring pick and
replace.
SINGLE-POINT EXHAUST PRO-FLO X™
Step 1
Install a 1/4" NPT pipe plug
(00-7010-08) into the pilot spool
bleed port located at the front of the
center block.
StandardSingle-Point Exhaust
Step 2
Next, install an optional single-point exhaust gasket
(04-2621-52). The single-point exhaust gasket can
be purchased as a spare part or included with the
purchase of a new Pro-Flo X™ pump.
WILDEN PUMP & ENGINEERING, LLC 32 WIL-11540-E-01
Page 35
REASSEMBLY HINTS & TIPS
AS SE MB 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 X™ MAXIMUM TORQUE SPECIFICATIONS
Description of PartTorque
Air Valve13.6 N•m (120 in-lb)
Air Chamber/Center Block27.1 N•m (20 ft-lb)
Liquid Chamber/Air Chamber, Aluminum Bolted Only
Liquid Chamber/Air Chamber, Stainless-Steel Bolted Only
Outer Pistons, Rubber & PTFE, Excluding Stainless-
• 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:
Needle Nose Pliers
Phillips Screwdriver
Electrical Tape
• 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 kidney bean 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.
• Af ter 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 shaf t with a rotating motion.
This will complete the resizing of the seal.
• Perform these steps for the remaining seal.
Figure B
NEEDLE NOSE
PLIERS
NLGI grade 2
Figure A
WIL-11540-E-01 33 WILDEN PUMP & ENGINEERING, LLC
SHA FT SE AL RING
TAPE
SHA FT SE AL RING
TAPE
Page 36
Section 8
EXPLODED VIEW & PARTS LISTING
PX820/830 ALUMINUM
Rubber/TPE/PTFE/Ultra-Flex™-FittedEXPLODED VIEW
FULL-STROKE PTFEFLANGED
REDUCED-STROKE PTFE
REDUCED-STROKE
ULTRA-FLEX™
METAL ADSPLASTIC ADS
LW0184 Rev. A
ALL CIRCLED PART IDENTIFIERS ARE INCLUDED IN REPAIR KITS (see Section 9).
WILDEN PUMP & ENGINEERING, LLC 34WIL-11540-E-01
Page 37
EXPLODED VIEW & PARTS LISTING
PX820/830 ALUMINUM
Item
DescriptionQty.
Rubber/TPE/PTFE/Ultra-Flex™-FittedPARTS LISTING
PX820/830/AAAAA/…/
P/N
PX820/830/AAAPP/…/
P/N
AIR DISTRIBUTION COMPONENTS
1Pro-Flo V™ Assembly, Air Valve
2O-Ring (-225), End Cap (Ø1.859 x Ø.139)204-2390-52-70004-2390-52-700
3End Cap204-2340-0104-2330-20-700
4Screw, SHC, Air Valve (1/4"-20 x 4-1/2")401-6000-03N/A
Screw, SHC, Air Valve (1/4"-20 x 4-1/2")6N/A01-6000-03
5Nut, Square (1/4"-20)6N/A00-6505-03
6Muffler Plate, Pro-Flo V™104-3185-0108-3185-20
7Gasket, Muffler Plate, Pro-Flo V™104-3502-5208-3502-52
8Gasket, Air Valve, Pro-Flo V™104-2620-5208-2620-52
9Center Block Assembly, Pro-Flo X™
10O-Ring (-210), Adjuster (Ø.734" x Ø.139")102-3200-5202-3200-52
11Sleeve, Threaded, Center Block4N/A04-7710-08
12O-Ring (-009) Pilot Spool Retaining (Ø.208 x Ø.070)204-2650-49-70004-2650-49-700
13Pilot Sleeve Assembly104-3880-9904-3880-99
14Shaft Seal208-3210-55-22508-3210-55-225
15Bushing, Shaft208-3306-1308-3306-13
16Gasket, Center Block Pro-Flo V™204-3529-5204-3529-52
17Screw, 10-32 X .50 Self-Tapping Grounding104-6345-08N/A
18Retaining Ring204-3890-0304-3890-03
19Screw, HSFHS (3/8"-16 x 1")871-6250-0871-6250-08
20Air Chamber, Pro-Flo X™ Drop-In208-3694-0108-3694-01
21Muffler 1"115-3510-99R15-3510-99R
25Washer, Flat (Ø.531" x Ø1.062" x .095")3204-6730-0804-6730-08
26Screw, HHC (1/2"-13 x 1-3/4")1608-6190-0808-6190-08
27Screw, HHC (1/2"-13 x 2")1604-6210-0804-6210-08
Metal Center Block Assembly includes item 10, 14 and 15. Plastic Center Block Assembly includes 5, 10, 11, 14 and 15.
All boldface items are primary wear parts.
LW0185 Rev. A
WILDEN PUMP & ENGINEERING, LLC 36WIL-11540-E-01
Page 39
NOTES
Page 40
EXPLODED VIEW & PARTS LISTING
PX820/PX830 STAINLESS STEEL
Rubber/TPE/PTFE/Ultra-Flex™EXPLODED VIEW
FULL-STROKE PTFEFLANGED
REDUCED-STROKE PTFE
REDUCED-STROKE
ULTRA-FLEX™
METAL ADSPLASTIC ADS
LW0076 Rev. C
ALL CIRCLED PART IDENTIFIERS ARE INCLUDED IN REPAIR KITS (see Section 9).
WILDEN PUMP & ENGINEERING, LLC 38WIL-11540-E-01
Page 41
EXPLODED VIEW & PARTS LISTING
PX820/PX830 STAINLESS STEEL
Item
DescriptionQty.
Rubber/TPE/PTFE/Ultra-Flex™PARTS LISTING
PX820/830/SSAAA/…/
P/N
PX820/830/SSSSS/…/
P/N
AIR DISTRIBUTION COMPONENTS
1Pro-Flo V™ Assembly, Air Valve
2O-Ring (-225), End Cap (Ø1.859 x Ø.139)204-3290-52-70004-3290-52-700
3End Cap204-2340-0104-2340-03
4Screw, SHC, Air Valve (1/4"-20 x 4-1/2")401-6000-0301-6000-03
Screw, SHC, Air Valve (1/4"-20 x 4-1/2")6N/AN/A
5Nut, Square (1/4"-20)6N/AN/A
6Muffler Plate, Pro-Flo V™104-3185-0104-3185-03
7Gasket, Muffler Plate, Pro-Flo V™104-3502-5204-3502-52
8Gasket, Air Valve, Pro-Flo V™104-2620-5204-2620-52
9Center Block Assembly, Pro-Flo X™
10O-Ring (-210), Adjuster (Ø.734" x Ø.139")102-3200-5202-3200-52
11Sleeve, Threaded, Center Block4N/AN/A
12O-Ring (-009) Pilot Spool Retaining (Ø.208 x Ø.070)204-2650-49-70004-2650-49-700
13Pilot Sleeve Assembly104-3880-9904-3880-99
14Shaft Seal208-3210-55-22508-3210-55-225
15Bushing, Shaft208-3306-1308-3306-13
16Gasket, Center Block Pro-Flo V™204-3529-5204-3529-52
17Screw, 10-32 X .50 Self-Tapping Grounding104-6345-0804-6345-08
18Retaining Ring204-3890-0304-3890-03
19Screw, HSFHS (3/8"-16 x 1")871-6250-0871-6250-03
20Air Chamber, Pro-Flo X™ Drop-In208-3694-0108-3698-03
21Muffler 1"115-3510-99R15-3510-99R
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 InformatI on
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 facilit y? 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
NOTE: WARRANTY VOID IF PAGE IS NOT FAXED TO WILDEN
Trade Journal
Trade Show
onCE ComPLEtE, faX to (909) 783-3440
WILDEN PUMP & ENGINEERING, LLC
Internet/E-mail
Distributor
Page 48
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22069 Van Buren Street,
Grand Terrace,CA 92313-5607
Telephone: (909) 422-1731
Fax: (909) 783-3440
22069 Van Buren St.
Grand Terrace, CA 92313-5651
T: +1 (909) 422-1731
www.maag.com
F: +1 (909) 783-3440
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. 10-2013
Authorized PSG Representative:
Copyrigh t 2013, Pump Solu tions Group (PSG), A Do ver Company
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