Polytetrafl uoroethylene (PTFE) 4.4°C to 104.4°C 40°F to 220°F
Polyurethane –12.2°C to 65.6°C 10°F to 150°F
Tetra-Flex™ PTFE with
Neoprene backing 4.4°C to 107.2°C 40°F to 225°F
Tetra-Flex™ PTFE with
EPDM backing –10°C to 137°C 14°F to 280°F
NOTE: Not all materials are available for all models. Refer to Section 2 for
material options for your pump.
CAUTION: Do not apply compressed air to the exhaust
port – pump will not function.
CAUTION: Do not over-lubricate air supply – excess lubrica-
tion will reduce pump performance. Pump is pre-lubricated.
CAUTION: Maximum temperature limits are based upon
mechanical stress only. Certain chemicals will signifi cantly
reduce maximum safe operating temperatures. Consult
Chemical Resistance Guide (E4) for chemical compatibility
and temperature limits.
CAUTION: When choosing pump materials, be sure to
check the temperature limits for all wetted components.
Example: Viton® has a maximum limit of 176.7°C (350°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 signifi cantly
reduce maximum safe operating temperatures. Consult
engineering guide for chemical compatibility and temperature limits.
CAUTION: Always wear safety glasses when operat-
ing pump. If diaphragm rupture occurs, material being
pumped may be forced out of the air exhaust.
WARNING: Prevention of static sparking — If static spark-
ing occurs, fi re or explosion could result. Pump, valve, and
containers must be properly grounded when handling
fl ammable fl uids and whenever discharge of static electricity is a hazard.
CAUTION: Do not exceed 8.6 bar (125 psig) air supply pres-
sure.
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 fl uid
to fl ow into a suitable container.
CAUTION: All piping, valves, gauges and other components
installed on the liquid discharge must have a minimum
pressure rating of 20.7 bar (300 psig).
CAUTION: The discharge pressure generated by this pump
is two times the inlet pressure supplied.
CAUTION: Do not exceed 82°C (180°F) air inlet temperature
for Pro-Flo X™ models.
CAUTION: Pumps should be thoroughly fl ushed before in-
stalling into process lines. FDA and USDA approved pumps
should be cleaned and/or sanitized before being used.
NOTE: Cast-iron PTFE-fi tted 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.
CAUTION: Pro-Flo® pumps cannot be used in submersible
applications. Pro-Flo X™ is available in both submersible
and non-submersible options. Do not use non-submersible
Pro-Flo X™ models in submersible applications. Turbo-Flo®
pumps can also be used in submersible applications.
CAUTION: Blow out air line for 10 to 20 seconds before
attaching to pump to make sure all pipe line debris is clear.
Use an in-line air fi lter. A 5 (micron) air fi lter is recommended.
NOTE: Tighten clamp bands and retainers prior to installa-
tion. Fittings may loosen during transportation.
NOTE: When installing PTFE diaphragms, it is important to
tighten outer pistons simultaneously (turning in opposite
directions) to ensure tight fi t.
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: Verify the chemical compatibility of the process
and cleaning fl uid to the pump’s component materials in
the Chemical Resistance Guide (see E4).
CAUTION: When removing the end cap using compressed
air, the air valve end cap may come out with considerable force. Hand protection such as a padded glove or rag
should be used to capture the end cap.
WIL-11111-E-03 1 WILDEN PUMP & ENGINEERING, LLC
Section 2
PUMP DESIGNATION SYSTEM
HX400S METAL
38 mm (1-1/2") Pump
Maximum Flow Rate:
235 LPM (62 GPM)
LEGEND
XHX400S / XXXXX / XXX / XX / XXX / XXXX
MATERIAL CODES
MODEL
XHX400S = HIGH PRESSURE
SIMPLEX/ATEX
WETTED PARTS / OUTER PISTON
AS = ALUMINUM/STAINLESS STEEL
SS = STAINLESS STEEL/STAINLESS
STEEL
AIR CHAMBER
A = ALUMINUM
S = STAINLESS STEEL
MODEL VALVE SEAT SPECIALTY
ORING CODE (if applicable)
VALVE SEAT
VALVE BALL
DIAPHRAGM
AIR VALVE
CENTER BLOCK
AIR CHAMBER
WETTED PARTS/OUTER PISTON
CENTER BLOCK
A = ALUMINUM
S = STAINLESS STEEL
AIR VALVE
A = ALUMINUM
S = STAINLESS STEEL
DIAPHRAGM
FWS = SANITARY WIL-FLEX™
1
VALVE BALL
WF = WIL-FLEX™ [Santoprene®
(orange dot)]
VALVE SEAT
A = ALUMINUM
S = STAINLESS STEEL
VALVE SEAT ORING
TF = PTFE (white dot)
NOTE: 1 Meets Requirements of FDA CFR21.177
SPECIALTY CODES
0245 Reverse manifolds
0247 Discharge & inlet manifold
facing exhaust
0250 Discharge manifold
facing air inlet
NOTE: Most elastomeric materials use colored dots for identification.
NOTE: Not all models are available with all material options.
Hytrel® and Viton® are registered trademarks of DuPont Dow Elastomers.
WILDEN PUMP & ENGINEERING, LLC 2 WIL-11111-E-03
0320 Submersible center block
0504 DIN flange
Section 3
HOW IT WORKSPUMP DISTRIBUTION SYSTEM
The Wilden diaphragm pump is an air-operated, positive displacement, self-priming pump. These drawings show the flow pattern through
the pump upon its initial stroke. It is assumed the pump has no fluid in it prior to its initial stroke.
FIGURE 1 When air pressure is supplied to
the pump, the air valve directs pressure to the
back side of the diaphragm A. The compressed
air moves the diaphragm away from the
center section 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 the atmosphere
through the exhaust port. The movement of
diaphragm B towards the center section of
the pump creates a vacuum within the chamber B. Atmospheric pressure forces fluid into
the inlet manifold forcing the inlet valve ball
off of its seat. Liquid is free to move past the
inlet valve ball and fill the liquid chamber (see
shaded area).
HOW IT WORKSAIR DISTRIBUTION SYSTEM
CENTER BLOCK
AIR
INLET
MAIN
SHAFT
PILOT SPOOL
AIR VALVE
END CAP
AIR VALVE
SPOOL
MUFFLER
PLATE
FIGURE 2 Once the shaft has reached the end
of its stroke, the air valve redirects pressurized
air to the back side of the diaphragm B. This
pressurized air is also directed to the opposite
side of the diaphragm A through a passageway that is routed through the common shaft
and outer piston. The pressurized air forces
diaphragm B away from the center section
while also pushing diaphragm A to the center
section. 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 of its seat, forcing fluid
to flow through the pump discharge. The pressure on diaphragm A creates a force on the
shaft that is combined with the pressure from
diaphragm B. This total load is transferred to
the liquid creating a liquid pressure that is two
times greater than the supplied air pressure.
The Pro-Flo X™ patented air distribution system incorporates
two moving parts: the air valve spool and the pilot spool. The
heart of the system is the 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 air valve
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 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.
MUFFLER
The repositioning of the air valve spool routes the air to the
other air chamber.
FIGURE 3 At completion of the stroke, the
air valve again redirects air to the back side
of the 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 condition
of the application.
offers fl exibility never before seen in the world of
AODD pumps. The
patent-pending EMS
is simple and easy
to use. With the
turn of an integrated
TM
Operating Principal
control dial, the operator can select the optimal
balance of fl ow and effi ciency that best meets the
application needs. Pro-Flo X™ provides higher
performance, lower
operational costs
and fl exibility that
exceeds previous
industry standards.
AIR CONSUMPTION
$
$
$
Turning the dial
changes the
relationship
between air inlet
and exhaust
porting.
WILDEN PUMP & ENGINEERING, LLC 6 WIL-11111-E-03
Each dial setting
represents an
entirely different
fl ow curve
Pro-Flo X™ pumps
are shipped from
the factory on
setting 4, which
is the highest
fl ow rate setting
possible
Moving the dial
from setting 4
causes a decrease
in fl ow and an even
greater decrease in
air consumption.
When the air
consumption
decreases more
than the fl ow
rate, effi ciency
is improved and
operating costs
are reduced.
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 fl ow rate and
air consumption for your Pro-Flo X™ pump using the Effi ciency 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 fl ow 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 fl ow curve,
draw a vertical line downward until reaching
the bottom scale on the chart. Identify the fl ow
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
identifi es the fl ow 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 fl ow rate (8.2 gpm)
obtained in Step 1 by the fl ow X Factor multiplier (0.58) in Step 2 to determine the fl ow 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
(fl ow rate for Setting 4)
(Flow X Factor setting 2)
(Flow rate for setting 2)
EMS CURVE
fl ow 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 fl ow 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
WIL-11111-E-03 7 WILDEN PUMP & ENGINEERING, LLC
9.8
scfm
(air consumption for setting 4)
.48
4.7
Figure 3
The fl ow 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)
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 specifi c application. For this example we will be using an application requirement of 18.9 lpm
(5 gpm) fl ow rate against 2.8 bar (40 psig) discharge pressure.
This example will illustrate how to calculate the air consumption 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 effi ciently, 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 fl ow 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 fi gure 4.
Step 3
: Determine flow X Factor. Divide the required
fl ow rate 18.9 lpm (5 gpm) by the setting 4 fl ow
rate 38.6 lpm (10.2 gpm) to determine the fl ow
X Factor for the application.
5
gpm / 10.2 gpm = 0.49 (flow X Factor)
EMS CURVE
Figure 5
fl ow 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 fl ow
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 fl ow curve, draw a vertical line downward until reaching the bottom
scale on the chart and identify the fl ow rate.
bar (40 psig) psig discharge pressure line until
it crosses the vertical 0.49 X Factor line. Typically, this point lies between two fl ow EMS
setting curves (in this case, the point lies between the fl ow 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 (fi gure 5). For more precise results you can mathematically interpolate between the two curves to determine the
optimal EMS setting.
For this example the EMS setting is 1.8.
WILDEN PUMP & ENGINEERING, LLC 8 WIL-11111-E-03
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