125 psi or 289 ft. of water
(8.8 Kg/cm2 or 88 meters)
MODEL HDF3-A Performance Curve
Performance based on the following: elastomer fitted pump, flooded suction,
water at ambient conditions. The use of other materials and varying hydraulic
100(169.9)
conditions may result in deviations in excess of 5%.
120(203.9)
HEADS UP TO
0
0
200
40
6080
100
120
140160
180
200
220
240
U.S. Gallons per minute
01002003004005006007008009001000
Liters per minute
CAPACITY
SANDPIPER® pumps are designed to be powered only by compressed air.
hdf3adl7sm-rev0614 Model HDF3-A & HDF4-A Page 1
260
Explanation of Pump Nomenclature, HDF3-A & HDF4-A
II 2GD T5
MATERIALS OF CONSTRUCTION
To order a pump or replacement parts, rst enter the Model Number HDF3-A, or HDF4-A, followed by the Type Designation listed below in the far left column.
A = Compressed Fibre B = Nitrile N = Neoprene SS = Stainless Steel
AL = Aluminun CI = Cast Iron PS = Plated Steel S = Santoprene
ALM = Almag 35 Aluminum H = Hytrel® R = Urethane
Hytrel is a registered tradename of E.I. du Pont. Santoprene is a registered tradename of Exxon Mobil Corp.
Maximum and Minimum Temperatures are the limits for which
these materials can be operated. Temperatures coupled with
pressure affect the longevity of diaphragm pump components.
Maximum life should not be expected at the extreme limits of
the temperature ranges.
Materials
Nitrile General purpose, oil-resistant. Shows good solvent, oil, water and hydraulic uid resistance. Should
not be used with highly polar solvents like acetone and MEK, ozone, chlorinated hydrocarbons and nitro
hydrocarbons.
NEOPRENE All purpose. Resistant to vegetable oils. Generally not affected by moderate chemicals, fats,
greases and many oils and solvents. Generally attacked by strong oxidizing acids, ketones, esters, nitro
hydrocarbons and chlorinated aromatic hydrocarbons.
®
HYTREL
Urethane
Santoprene
lent abrasion resistance.
‡
For specic applications, always consult “Chemical Resistance Chart" Technical Bulletin
Good on acids, bases, amines and glycols at room temperature.
Shows good resistance to abrasives. Has poor resistance to most solvents and oils.
®
Injection molded thermoplastic elastomer with no fabric layer. Long mechanical ex life. Excel-
CF-8M Stainless Steel equal to or exceeding ASTM specication A743 for corrosion resistant iron chro-
mium, iron chromium nickel, and nickel based alloy castings for general applications. Commonly referred
to as 316 Stainless Steel in the pump industry.
Maximum Minimum
®
Operating Temperatures
190°F -10°F
88°C -23°C
200°F -10°F
93°C -23°C
220°F -20°F
104°C -29°C
150°F +32°F
66°C 0°C
275°F -40°F
135°C -40°C
hdf3adl7sm-rev0614
II 2 G c T5
II 3/2 G c T5
II 2 D c T100oC
All models, including pumps equipped with Aluminum
wetted and midsection parts.
See page 6 for ATEX Explanation of Type
Examination Certicate.
Dimensions:
Dimensions are ± 1/8"
Figures in parenthesis = millimeters
HDF3-A & HDF4-A
hdf3adl7sm-rev0614 Model HDF3-A & HDF4-A Page 3
SERVICE AND OPERATING MANUAL
II 2GD T5
Models HDF3-A Type 7
See pages 16 & 17
for ATEX ratings
PRINCIPLE OF PUMP OPERATION
This ap swing check valve pump is powered by compressed air and is a 1:1
pressure ratio design. It alternately pressurizes the inner side of one diaphragm
chamber, while simultaneously exhausting the other inner chamber. This causes the
diaphragms, which are connected by a common rod, to move endwise. Air pressure
is applied over the entire surface of the diaphragm, while liquid is discharged from
the opposite side. The diaphragm operates under a balanced condition during the
discharge stroke, which allows the unit to be operated at discharge heads over 200
feet (61 meters) of water head.
Since the diaphragms are connected by a common rod, secured by plates to the
center of the diaphragms, one diaphragm performs the discharge stroke, while the
other is pulled to perform the suction stroke in the opposite chamber.
For maximum diaphragm life, keep the pump as close to the liquid being pumped
as possible. Positive suction head in excess of 10 feet of liquid (3.048 meters) may
require a back pressure regulating device. This will maximize diaphragm life.
Alternate pressuring and exhausting of the diaphragm chamber is performed by
means of an externally mounted, pilot operated, four-way spool type air distribution
valve. When the spool shifts to one end of the valve body, inlet air pressure is applied
to one diaphragm chamber and the other diaphragm chamber exhausts. When the
spool shifts to the opposite end of the valve body, the porting of chambers is reversed.
The air distribution valve spool is moved by an internal pilot valve which alternately
pressurizes one side of the air distribution valve spool, while exhausting the other side.
The pilot valve is shifted at each end of the diaphragm stroke by the diaphragm plate
coming in contact with the end of the pilot valve spool. This pushes it into position for
shifting of the air distribution valve.
The chambers are manifolded together with a suction and discharge check valve
for each chamber, maintaining ow in one direction through the pump.
HDF4-A Type 3
INSTALLATION & START-UP
Locate the pump as close to the product being pumped as possible, keeping suction
line length and number of ttings to a minimum. Do not reduce line size.
For installations of rigid piping, short exible sections of hose should be installed
between pump and piping. This reduces vibration and strain to the piping system.
A Warren Rupp Tranquilizer
pulsation in ow.
This pump was tested at the factory prior to shipment and is ready for operation. It is
completely self-priming from a dry start for suction lifts of 20 feet (6.096 meters) or less.
For suction lifts exceeding 20 feet of liquid, ll the chambers with liquid prior to priming.
®
Surge Suppressor is recommended to further reduce
AIR SUPPLY
Air supply pressures cannot exceed 125 psi (8.61 bar). Connect the pump air inlet
to an air supply of sufcient capacity and pressure required for desired performance.
When the air line is solid piping, use a short length of exible hose (not less than 3/4"
(19mm) in diameter) between pump and piping to eliminate strain to pipes.
AIR INLET & PRIMING
For start-up, open an air valve approximately 1/2" to 3/4" turn. After the unit primes,
an air valve can be opened to increase ow as desired. If opening the valve increases
cycling rate, but does not increase ow rate, cavitation has occurred, and the valve
should be closed slightly.
For the most efcient use of compressed air and the longest diaphragm life, throttle
the air inlet to the lowest cycling rate that does not reduce ow.
hdf3adl7sm-rev0614
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