This pump is part of the Containment Duty Pumps. It is specially tted with PTFE diaphragms as well as elastomeric or elastomeric/PTFE driver diaphragms. The liquid-lled
spill chambers provide an additional chemically-resistant barrier, should a pumping diaphragm fail. The Spill Containment design gives the pump user advanced warning of
diaphragm failure, before pumpage can damage the air valve or be released into the work environment. Three optional leak detectors available for this model:
The Containment Duty pumps offer many different levels of materials and spill monitoring devices designed to t a variety of applications and budgets.
* Leak Detectors are not ATEX Compliant
BAR
7
100
90
6
80
5
70
60
4
50
HEAD
3
40
30
2
PSI
10(17)
100 PSI
80 PSI
60 PSI
40 PSI
AIR CONSUMPTION
SCFM (M
20(34)
30(51)
40(68)
3
/hr)
50(85)
MODEL ST1½/ST40 Performance Curve
Performance based on the following: elastomer fitted pump, flooded suction,
water at ambient conditions. The use of other materials and varying hydraulic
60(102)
70(119)
conditions may result in deviations in excess of 5%.
80(136)
90(152.9)
20
1
20 PSI Air Inlet Pressure
10
0
0
0
1020
3040
50
607080
90
US Gallons per minute
050100150200250300350
Liters per minute
CAPACITY
SANDPIPER® pumps are designed to be powered only by compressed air.
st15dl4sm-rev0614 Models ST1½, ST40 Page 1
Explanation of Pump Nomenclature, ST1½ & ST40
II 2GD T5
II 2GD T5
ST1½ -A: 1½"
(37.5mm)
NPT(F)
ST40-A: 1½"
(37.5mm)
BSP(F)
0 to 90 gallons per minute
(0 to 340 liters per minute)
Occasional solids only.
up to ¼"
(6.3mm)
125 psi or 289 ft. of water
(8.8 Kg/cm2 or 88 meters)
No-lube, non-stall
design.
®
pumps are designed to be powered only by compressed air)
Temperature Limit: 212
F -
100C
MAXIMUM
Performance based on water atambient temperature. Averagedisplacement per pump stroke:
1.14 liters.
Performance based on water atambient temperature. Averagedisplacement per pump stroke:
This pump is part of the Containment Duty Pumps. It is specially fitted with PTFEdiaphragms as well as elastomeric or elastomeric/PTFEdriver diaphragms.The liquid-filled spill chambersprovide an additional chemically-resistant barrier, should a pumpIng diaphragm fail.The Spill Containment design gives the pump user advanced warning of diaphragm failure, beforepumpage can damage the air valve or be released into the work environment.Three optional leak detectors available for this model:
The Containment Duty pumps offer many different levels of materials and spill monitoring devices designed to fit a variety of applications and budgets.
I M2 c T5II 2GD T5
MATERIALS OF CONSTRUCTION
To order a pump or replacement parts, rst enter the Model Number ST15, or ST40, followed by the Type Designation listed below in the far left column.
Kit available to convert to top or bottom porting.
SPST1½A-REV0807
Porting
Manifold
ManifoldOuter
Side
Chamber
Driver
Chamber
Chamber
Inner
Outer
Diaphragm
Plate
Inner
Diaphragm
Plate
Intermediate
Housing
Diaphragm
I
CICIDI316SSCICI416SS316SS 304SST/VTTT212
WR-C
WR-C
WR-C
AL = Aluminum
CI = Cast Iron
DC = Die Cast
CIDI316SSCICI416SS 316SS 304SST/VTTT212
DI = Ductile Iron
SS = Stainless Steel
T = PTFE
T/I = PTFE Diaphragm/EDPM Driver
®
is a registered tradenames of E.I. du Pont.
Viton
II 1 G c T5
II 3/1 G c T5
II 1 D c T100oC
I M1 c
I M2 c
Models equipped with Cast Iron, Stainless
Steel, or Alloy C wetted parts, and Cast Iron
midsection parts. See page 6 for ATEX
Explanation of EC-Type Certicate.
®Warren Rupp and SANDPIPER are registered tradenames of Warren Rupp, Inc.
®
Driver
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.
Seat
Gasket
Manifold
Gasket
Sealing
Rings
Shipping
Wt.(lbs)
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.
Operating Temperatures
Materials
EPDM Shows very good water and chemical resistance. Has poor resistance to oil and solvents, but is fair in
ketones and alcohols.
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.
PTFE Chemically inert, virtually impervious. Very few chemicals are known to react chemically with
PTFE: molten alkali metals, turbulent liquid or gaseous uorine and a few uoro-chemicals such as
chlorine triuoride or oxygen diuoride which readily liberate free uorine at elevated temperatures.
FKM (Fluorocarbon) shows good resistance to a wide range of oils and solvents; especially all aliphatic,
aromatic and halogenated hydrocarbons, acids, animal and vegetable oils. Hot water or hot aqueous solu
tions (over 70°F) will attack FKM.
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.
ALLOY C CW-12MW equal to or exceeding ASTM A494 specication for nickel and nickel alloy castings.
For specic applications, always consult “Chemical Resistance Chart" Technical Bulletin
* INDICATES DIMENSIONS WITH SUCTION AND DISCHARGE
PORTS ROTATED 180° TO A VERTICAL POSITION
DIMENSIONAL OUTLINES AVAILABLE SHOWING OPTIONAL TOP AND BOTTOM PORTING
DIMENSIONS WITH SUCTION AND DISCHARGE PORTS ROTATED 90 TO VERTICAL POSITION (SHOWN WITH DOTTED LINES).
*
Model ST1½
-A features NPT threaded connections.
Model ST40-A features British Standard Pipe (BSP) tapered threaded connections.
st15dl4sm-rev0614 Models ST1½, ST40 Page 3
SERVICE & OPERATING MANUAL
II 2GD T5
Model ST1½ Type 4
See pages 18 & 19
for ATEX ratings
PLEASE NOTE!
The photos shown in this manual are for general instruction only. Your specic model
may not be shown. Always refer to the parts list and exploded view drawing for your
specic model when installing, disassembling or servicing your pump.
PRINCIPLE OF OPERATION
All Warren Rupp SANDPlPER pumps, including this Containment Duty SANDPlPER
pump, operate on the same basic principle. They are designed to be powered by compressed
air only which alternately pressurizes the inner side of one diaphragm chamber while
simultaneously exhausting the other inner chamber. The diaphragms are connected by
a common rod; when the inner side of one diaphragm chamber is pressurized, moving
the diaphragm outward on a discharge stroke, the opposite diaphragm is pulled inward
on a suction stroke.
Alternate pressurizing and exhausting of the diaphragm chamber is accomplished
with an externally mounted pilot operated, four way, spool type, air distribution valve.
When the spool is at one end of the valve body, inlet air pressure is connected to one
diaphragm chamber while the other diaphragm chamber is exhausting. When the spool
is moved to the opposite end of the valve body, the porting of chambers is reversed. The
air distribution valve spool is moved from one end position to the other in the valve body
by an internal pilot valve which alternately pressurizes one end of the air distribution valve
spool while simultaneously exhausting the other. The pilot valve is positively shifted at
each end of the diaphragm stroke by the diaphragm plate contacting the end of the pilot
valve spool. This pushes it into position to shift the air distribution valve.
In all SANDPlPER pumps, this reciprocating diaphragm movement creates an alternating
suction and discharge action in the outer diaphragm chamber and the pumped material. A
manifold with a suction and discharge check valve for each chamber serves as a common
inlet and outlet for the pump.
This Containment Duty SANDPlPER unit differs from other SANDPIPER units only in
that it utilizes four (4) diaphragms instead of two (2). Two rod-connected diaphragms are
the driver diaphragms. The other two (outermost) diaphragms are the actual pumping
diaphragms. Each driver diaphragm (of neoprene or other elastomer), and the pumping
diaphragm (of PTFE), are separated by a chamber lled with liquid which transmits the
reciprocating motion of the driver diaphragm to the pumping diaphragm. The PTFE pumping
diaphragms, in turn, create the alternating suction and discharge action in the outer
diaphragm chambers, and are the only diaphragms in contact with liquid being pumped.
Model ST40 Type 4
Original Instructions
INSTALLATION PROCEDURES
CAUTION: This pump should not be applied in pumping applications where the driver
liquid coming in contact with the pumped liquid would create a hazardous condition.
This contact will occur if a PTFE pumping diaphragm fails since this diaphragm normally
separates the two liquids. Also note that care must be taken to guard against the operation
of this unit if it has been subjected to freezing temperatures. If the driver liquid freezes,
possible diaphragm failure may result.
Locate pump as close to product to be pumped as is practical to keep length of suction
line and number of ttings to a minimum. DO NOT REDUCE SUCTION LINE SIZE except
for very low ow rates or where higher velocities are required to keep pumped material
in suspension in the carrying liquid.
This unit is completely self-priming from a dry start up to a static suction lift of 10
feet (3.05 meters). For priming at suction lifts in excess of 10 feet (3.05 meters), ll the
pumping chambers with liquid prior to operation. POSITIVE SUCTION HEAD IN EXCESS
OF 10 FEET (3.05 METERS) OF LIQUID SHOULD ALSO BE AVOIDED FOR BEST
DIAPHRAGM SERVICE LIFE.
st15dl4sm-rev0614 Models ST1½, ST40 Page 4
INSTALLATION GUIDE
Top Discharge Ball or Flap Valve Unit
Available from
Warren Rupp
1
Tranquilizer
Filter/Regulator�
2
®
/Surge Supressor
CAUTION
The air exhaust should be
piped to an area for safe
disposition of the product
being pumped, in the event
of a diaphragm failure.
1
Surge
Suppressor
2
st15dl4sm-rev0614 Models ST1½, ST40 Page 5
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