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
100 PSI
80 PSI
60 PSI
40 PSI
AIR CONSUMPTION
SCFM (M
10(17)
3
/hr)
15(25.4)
20(34)
MODEL ST1/ST25 Performance Curve
Performance based on the following: elastomer fitted pump, flooded suction,
water at ambient conditions. The use of other materials and varying hydraulic
25(42.5)
30(51)
conditions may result in deviations in excess of 5%.
35(59.5)
40(68)
45(76.5)
50(85)
st1dl5sm-rev0614
20
1
20 PSI Air Inlet Pressure
10
0
0
0
48
1216
20
24
2832
36
40
US Gallons per minute
020406080100120140150
Liters per minute
CAPACITY
SANDPIPER® pumps are designed to be powered only by compressed air.
Models ST1 & ST25 Page 1
0 to 42 gallons per minute
(0 to 159 liters per minute)
Occasional solids only,
to nearly
1
/4"
(6.3 mm)
125 psi or 289 ft. of water
(8.8 Kg/cm2 or 88 meters)
MATERIALS OF CONSTRUCTION
INTAKE/DISCHARGE PIPE SIZECAPACITYAIR VALVESOLIDS-HANDLINGHEADS UP TO
No-lube, no-stall
design.
PERFORMANCE CURVES
(SANDPIPER® pumps are designed to be powered only by compressed air)
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.
ST1 & ST25Performance based on waterat ambient temperature.Average displacement perpump stroke: 0.34 liter.
SANDPIPER
®
Models
SANDPIPER
®
ModelsST1 & ST25Performance based on waterat ambient temperature.Average displacement perpump stroke: .09 gallon.
ST1: 1" NPT
ST25: 1" BSP Tapered
Containment Duty
ST1 Type 4 ST25 Type 4
Air-OperatedDouble-Diaphragm Pump
ENGINEERING, PERFORMANCE& CONSTRUCTION DATA
Quality System
ISO9001 Certified
Environmental
Management System
ISO14001 Certified
®
II 2GD T5
Explanation of Pump Nomenclature
MATERIALS OF CONSTRUCTION
To order a pump or replacement parts, rst enter the Model Number ST1, or ST25, followed by the Type Designation listed below in the far left column.
304SS = 304 Stainless Steel except
Manifold Bolts which are PS
T = PTFE
T/N = PTFE Diaphragm/Neoprene Driver
PTFE Diaphragm/FKM Driver
T/V =
T/T/N =
PTFE Diaphragm/PTFE over Neoprene Driver
Inner
Diaphragm
Plate
Intermediate
Housing
Rod
ware
Seat
Diaphragm
Hard-
Valve
Ball
Valve
Material
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 18 for ATEX Explanation of Type
Examination Certicate.
Seat/
Manifold
Gasket
Valve
Materials
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.
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
Maximum Minimum
200°F -10°F
93°C -23°C
220°F -35°F
104°C -37°C
-
350°F -40°F
177°C -40°C
Air
Shipping
CapDiaphragm
Wt. (lbs)
CF-8M Stainless Steel equal to or exceeding ASTM specication A743 for corrosion resistant iron
‡
chromium, 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
st1dl5sm-rev0614
Models ST1 & ST25 Page 2
Maximum* Minimum* Optimum**
Operating Temperatures
NEOPRENE All purpose. Resistant to vegetable oils. Generally not affected by moderatechemicals, 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 chemically reactwith PTFE:molten alkali metals, turbulent liquid or gaseous fluorine and a few fluoro-chemicalssuch as chlorine trifluoride or oxygen difluoride which readily liberate free fluorine at elevatedtemperatures.
170°F-35°F50°F to 130°F
77°C-37°C10°C to 54°C
212°F+-35°F50°F to 212°F
100°C+-37°C10°C to 100°C
MATERIALS
212°F++35°F75°F to 212°F
100°C+ 0°C24°C to 100°C
*Definite reduction in service life.**Minimal reduction in service life at ends of range.
FKMShows 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 hotaqueous solutions (over 70ºF) will attack FKM.
For specific applications, always consult "Chemical Resistance Chart" Technical Bulletin.
STAINLESS STEEL CF-8M equal to or exceeding ASTM specification A743 for corrosion resistant iron chromium, 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 specification for nickel and nickel alloy castings.
Dimensions: ST1 & ST25
Dimensions are ± 1/8"
Figures in parenthesis = millimeters
Tapered
14. 9/32
(363)
4. 3/32
(104)
(313)
12. 5/16
Dimensional outlines available showing
optional top and bottom porting.
(116)
4. 9/16
Tapered
(17)
11/16
Optional installation
4 rubber feet.
Model ST1 features NPT threaded connections.
Model ST25 features British Standard Pipe (BSP)
Tapered threaded connections.
(176)
(349)
13. 3/4
6. 15/16
5/8
(16)
st1dl5sm-rev0614
Models ST1 & ST25 Page 3
II 2GD T5
SERVICE & OPERATING MANUAL
Model ST1 Type 5
See pages 17 & 18
for ATEX ratings
PRINCIPLE OF OPERATION
This ball 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.
This specially-tted SandPIPER pump differs from standard units in that it utilizes
four diaphragms instead of two. The two rod-connected diaphragms being the driver
diaphragms, and the other two (outermost) diaphragms being the actual
pumping diaphragms. Each driver diaphragm (of Neoprene or other elastomer), and the
pumping diaphragm (of TFE), are separated by a chamber lled with liquid. This
transmits the reciprocating motion of the driver diaphragm to the pumping diaphragm.
The TFE pumping diaphragms create alternating suction and discharge action to each
outer diaphragm chamber. The pumping diaphragms are the only ones in contact with
the liquid being pumped.
Model ST25 Type 5
Original Instructions
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 10-15 feet (35 meters) or less.
For suction lifts exceeding 15 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. Use of a
Warren Rupp Filter/Regulator in the air line is recommended.
st1dl5sm-rev0614
Models ST1 & ST25 Page 4
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