GORMAN‐RUPP OF CANADA LIMITED D ST. THOMAS, ONTARIO, CANADAPrinted in U.S.A.
e2012 The Gorman‐Rupp Company
Register your new
Gorman‐Rupp pump online at
www.grpumps.com
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The engine exhaust from this
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known to the State of California to
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RECORD YOUR PUMP MODEL AND SERIAL NUMBER
Please record your pump model and serial number in the
spaces provided below. Your Gorman‐Rupp distributor
needs this information when you require parts or service.
Pump Model:
Serial Number:
TABLE OF CONTENTS
INTRODUCTIONPAGE I - 1.................................................
WARNINGS ‐ SECTION APAGE A - 1........................................
INSTALLATION - SECTION BPAGE B - 1....................................
Pump DimensionsPAGE B - 1.....................................................
PREINSTALLATION INSPECTIONPAGE B - 1............................................
POSITIONING PUMPPAGE B - 2.......................................................
LiftingPAGE B - 2.................................................................
MountingPAGE B - 2.............................................................
ClearancePAGE B - 2.............................................................
SUCTION AND DISCHARGE PIPINGPAGE B - 2.........................................
MaterialsPAGE B - 2..............................................................
Line ConfigurationPAGE B - 2......................................................
Connections to PumpPAGE B - 2..................................................
GaugesPAGE B - 2...............................................................
SUCTION LINESPAGE B - 3...........................................................
FittingsPAGE B - 3...............................................................
StrainersPAGE B - 3..............................................................
SealingPAGE B - 3...............................................................
Suction Lines In SumpsPAGE B - 3.................................................
Suction Line PositioningPAGE B - 3................................................
DISCHARGE LINESPAGE B - 4........................................................
SiphoningPAGE B - 4.............................................................
ValvesPAGE B - 4................................................................
Bypass LinesPAGE B - 4..........................................................
AUTOMATIC AIR RELEASE VALVEPAGE B - 6...........................................
Theory of OperationPAGE B - 6....................................................
Air Release Valve InstallationPAGE B - 6............................................
ALIGNMENTPAGE B - 7..............................................................
OPERATION - SECTION CPAGE C - 1......................................
PRIMINGPAGE C - 1.................................................................
STARTINGPAGE C - 1................................................................
RotationPAGE C - 1..............................................................
OPERATIONPAGE C - 2..............................................................
Lines With a BypassPAGE C - 2....................................................
Lines Without a BypassPAGE C - 2.................................................
LeakagePAGE C - 2..............................................................
Liquid Temperature And OverheatingPAGE C - 2.....................................
Strainer CheckPAGE C - 2.........................................................
Pump Vacuum CheckPAGE C - 3..................................................
STOPPINGPAGE C - 3................................................................
Cold Weather PreservationPAGE C - 3..............................................
BEARING TEMPERATURE CHECKPAGE C - 3..........................................
TROUBLESHOOTING - SECTION DPAGE D - 1..............................
i
TABLE OF CONTENTS
(continued)
PUMP MAINTENANCE AND REPAIR ‐ SECTION EPAGE E - 1.................
STANDARD PERFORMANCE CURVEPAGE E - 1........................................
PARTS LIST:
Pump ModelPAGE E - 3..........................................................
Pump End AssemblyPAGE E - 5...................................................
PUMP AND SEAL DISASSEMBLY AND REASSEMBLYPAGE E - 6.........................
Suction Check Valve DisassemblyPAGE E - 6........................................
Wear Plate And Suction Head RemovalPAGE E - 6...................................
Impeller RemovalPAGE E - 7......................................................
Seal Removal and DisassemblyPAGE E - 7..........................................
Pump DisassemblyPAGE E - 7.....................................................
Shaft and Bearing Removal and DisassemblyPAGE E - 8.............................
Shaft and Bearing Reassembly and InstallationPAGE E - 9............................
Impeller Back ClearancePAGE E - 10................................................
Seal Reassembly and InstallationPAGE E - 11........................................
Impeller Installation And AdjustmentPAGE E - 12......................................
Pump Casing InstallationPAGE E - 13................................................
Wear Plate And Suction Head InstallationPAGE E - 13.................................
Suction Check Valve AssemblyPAGE E - 13..........................................
Final Pump AssemblyPAGE E - 14..................................................
LUBRICATIONPAGE E - 14.............................................................
BearingsPAGE E - 14..............................................................
Seal AssemblyPAGE E - 14.........................................................
EnginePAGE E - 14................................................................
ii
10 SERIES
OM-06592
INTRODUCTION
Thank You for purchasing a Gorman‐Rupp pump.
Read this manual carefully to learn how to safely
install and operate your pump. Failure to do so
could result in personal injury or damage to the
pump.
This pump is a 10 Series, semi‐open impeller, self‐
priming centrifugal model with a suction check
valve. The pump is flex‐coupled to a Deutz diesel
engine. It is designed for handling most non‐vola
tile, non‐corrosive liquids containing specified en
trained solids. The basic material of construction
for wetted parts is gray iron, with an alloy steel im
peller shaft.
Because pump installations are seldom identical,
this manual cannot possibly provide detailed in
structions and precautions for every aspect of
each specific application. Therefore, it is the re
sponsibility of the owner/installer of the pump to
ensure that applications not addressed in this
manual are performed only after establishing that
neither operator safety nor pump integrity are com
promised by the installation. Pumps and related
equipment must be installed and operated ac
cording to all national, local and industry stan
dards.
If there are any questions regarding the pump or
its application which are not covered in this man
ual or in other literature accompanying this unit,
please contact your Gorman‐Rupp distributor, or
The Gorman‐Rupp Company:
The Gorman‐Rupp Company
P.O. Box 1217
Mansfield, Ohio 44901-1217
Phone: (419) 755-1011
or:
Gorman‐Rupp of Canada Limited
70 Burwell Road
St. Thomas, Ontario N5P 3R7
Phone: (519) 631-2870
For information or technical assistance on the en
gine, contact the engine manufacturer's local
dealer or representative.
The following are used to alert maintenance per
sonnel to procedures which require special atten
tion, to those which could damage equipment, and
to those which could be dangerous to personnel:
Immediate hazards which WILL result in
severe personal injury or death. These
instructions describe the procedure re
quired and the injury which will result
from failure to follow the procedure.
Hazards or unsafe practices which
COULD result in severe personal injury
or death. These instructions describe
the procedure required and the injury
which could result from failure to follow
the procedure.
Hazards or unsafe practices which COULD
result in minor personal injury or product
or property damage. These instructions
describe the requirements and the possi
ble damage which could result from failure
to follow the procedure.
NOTE
Instructions to aid in installation, operation,and
maintenance, or which clarify a procedure.
PAGE I - 1INTRODUCTION
10 SERIESOM-06592
SAFETY - SECTION A
This information applies to 10 Series en
gine driven pumps. Refer to the manual
accompanying the engine before at
tempting to begin operation.
Because pump installations are seldom
identical, this manual cannot possibly
provide detailed instructions and pre
cautions for each specific application.
Therefore, it is the owner/installer's re
sponsibility to ensure that applications
not addressed in this manual are per
formed only after establishing that nei
ther operator safety nor pump integrity
are compromised by the installation.
Before attempting to open or service the
pump:
1. Familiarize yourself with this man
ual.
2. Switch off the engine ignition and
remove the key to ensure that the
pump will remain inoperative.
3. Allow the pump to completely cool
if overheated.
4. Check the temperature before
opening any covers, plates, or
plugs.
5. Close the suction and discharge
valves.
6. Vent the pump slowly and cau
tiously.
7. Drain the pump.
danger personnel as a result of pump
failure.
After the pump has been positioned,
make certain that the pump and all pip
ing connections are tight, properly sup
ported and secure before operation.
Do not operate the pump without the
guards in place over the rotating parts.
Exposed rotating parts can catch cloth
ing, fingers, or tools, causing severe in
jury to personnel.
Do not operate the pump against a
closed discharge valve for long periods
of time. If operated against a closed dis
charge valve, pump components will
deteriorate, and the liquid could come
to a boil, build pressure, and cause the
pump casing to rupture or explode.
This pump is designed to handle most
non‐volatile, non‐flammable liquids
containing specified entrained solids.
Do not attempt to pump volatile, explo
sive, or flammable materials, or any liq
uids which may damage the pump or en
Do not remove plates, covers, gauges,
pipe plugs, or fittings from an over
heated pump. Vapor pressure within the
pump can cause parts being disen
gaged to be ejected with great force. al
low the pump to cool before servicing.
PAGE A - 1SAFETY
Overheated pumps can cause severe
burns and injuries, and produce explo
sive fumes. If overheating of the pump
occurs:
1. Stop the pump immediately.
2. Ventilate the area.
3. Allow the pump completely to cool.
4. Refer to instructions in this manual
before restarting the pump.
Use lifting and moving equipment in
good repair and with adequate capacity
to prevent injuries to personnel or dam
age to equipment. The bail is intended
for use in lifting the pump assembly
only. Suction and discharge hoses and
piping must be removed from the pump
before lifting.
10 SERIESOM-06592
free of leaks. Never refuel a hot or run
ning engine. Avoid overfilling the fuel
tank. always use the correct type of fuel.
Do not operate an internal combustion
engine in an explosive atmosphere.
When operating internal combustion
engines in an enclosed area, make cer
tain that exhaust fumes are piped to the
outside. These fumes contain carbon
monoxide, a deadly gas that is color
less, tasteless, and odorless.
Never tamper with the governor to gain
more power. The governor establishes
safe operating limits that should not be
exceeded. See the performance curve,
page E-1 for the maximum continuous
operating speed for this pump.
Fuel used by internal combustion en
gines presents an extreme explosion
and fire hazard. Make certain that all
fuel lines are securely connected and
Pumps and related equipment must be in
stalled and operated according to all na
tional, local and industry standards.
PAGE A - 2SAFETY
10 SERIESOM-06592
INSTALLATION - SECTION B
Review all SAFETY information in Section A.
Since pump installations are seldom identical, this
section offers only general recommendations and
practices required to inspect, position, and ar
range the pump and piping.
Most of the information pertains to a standard
static lift application where the pump is positioned
above the free level of liquid to be pumped.
If installed in a flooded suction application where
the liquid is supplied to the pump under pressure,
some of the information such as mounting, line
configuration, and priming must be tailored to the
specific application. Since the pressure supplied
to the pump is critical to performance and safety,
be sure to limit the incoming pressure to 50% of the
maximum permissible operating pressure as
shown on the pump performance curve (see Sec
tion E, Page 1).
d. Check levels and lubricate as necessary. Re
fer to LUBRICATION in the MAINTENANCEAND REPAIR section of this manual and per
form duties as instructed.
e. If the pump andengine have been stored for
more than 12 months, some of the compo
nents or lubricants may have exceeded their
maximum shelf life. These must be inspectedor replaced to ensure maximum pump serv
ice.
If the maximum shelf life has been exceeded, or if
anything appears to be abnormal, contact your
Gorman‐Rupp distributor or the factory to deter
mine the repair or updating policy. Do not put the
pump into service until appropriate action has
been taken.
Battery Specifications And Installation
For further assistance, contact your Gorman‐Rupp
distributor or the Gorman‐Rupp Company.
PREINSTALLATION INSPECTION
The pump assembly was inspected and tested be
fore shipment from the factory. Before installation,
inspect the pump for damage which may have oc
curred during shipment. Check as follows:
a. Inspect the pump for cracks, dents, damaged
threads, and other obvious damage.
b. Check for and tighten loose attaching hard
ware. Since gaskets tend to shrink after dry
ing, check for loose hardware at mating sur
faces.
c. Carefully read all tags, decals, and markings
on the pump assembly, and perform all duties
indicated. Note that the pump shaft rotates in
the required direction.
Unless otherwise specified on the pump order, the
engine battery was not included with the unit. Re
fer to the following specifications when selecting a
battery.
Table 1. Battery Specifications
Reserve
Capacity
@ 80_ F
(Minutes)
365
Amp/
Hr.
Rating
175
Approx.
Overall
Dims.
(Inches)
20.5L
x
8.75W
x
9.75H
Voltage
12 Volts
Cold
Crank
Amps
@ 0_ F
960-975
Refer to the information accompanying the battery
and/or electrolyte solution for activation and charg
ing instructions.
Before installing the battery, clean the positive and
negative cable connectors, and the battery termi
nals. Secure the battery by tightening the
holddown brackets. The terminals and clamps
may be coated with petroleum jelly to retard corro
sion. Connect and tighten the positive cable first,
then the negative cable.
PAGE B - 1INSTALLATION
OM-0659210 SERIES
POSITIONING PUMP
Lifting
Pump unit weights will vary depending on the
mounting and drive provided. Check the shipping
tag on the unit packaging for the actual weight, and
use lifting equipment with appropriate capacity.
Drain the pump and remove all customer‐installed
equipment such as suction and discharge hoses
or piping before attempting to lift existing, installed
units.
The pump assembly can be seriously
damaged if the chains or cables used to lift
and move the unit are improperly wrapped
around the pump.
Mounting
Locate the pump in an accessible place as close as
practical to the liquid being pumped. Level mount
ing is essential for proper operation.
SUCTION AND DISCHARGE PIPING
Pump performance is adversely effected by in
creased suction lift, discharge elevation, and fric
tion losses. See the performance curve on Page
E-1 to be sure your overall application allows
pump to operate within the safe operation range.
Materials
Either pipe or hose maybe used for suction and
discharge lines; however, the materials must be
compatible with the liquid being pumped. If hose is
used in suction lines, it must be the rigid‐wall, rein
forced type to prevent collapse under suction. Us
ing piping couplings in suction lines is not recom
mended.
Line Configuration
Keep suction and discharge lines as straight as
possible to minimize friction losses. Make mini
mum use of elbows and fittings, which substan
tially increase friction loss. If elbows are necessary,
use the long‐radius type to minimize friction loss.
Connections to Pump
The pump may have to be supported or shimmed
to provide for level operation or to eliminate vibra
tion.
If the pump has been mounted on a moveable
base, make certain the base is stationary by setting
the brake and blocking the wheels before attempt
ing to operate the pump.
To ensure sufficient lubrication and fuel supply to
the engine, do not position the pump and engine
more than 15_ off horizontal for continuous opera
tion. The pump and engine may be positioned up
to 30_ off horizontal for intermittent operationonly; however, the engine manufacturer should be
consulted for continuous operation at angles
greater than 15_.
Clearance
A minimum clearance of 9 inches is required to
permit removal of the rotating assembly.
Before tightening a connecting flange, align it ex
actly with the pump port. Never pull a pipe line into
place by tightening the flange bolts and/or cou
plings.
Lines near the pump must be independently sup
ported to avoid strain on the pump which could
cause excessive vibration, decreased bearing life,
and increased shaft and seal wear. If hose‐type
lines are used, they should have adequate support
to secure them when filled with liquid and under
pressure.
Gauges
Most pumps are drilled and tapped for installing
discharge pressure and vacuum suction gauges. If
these gauges are desired for pumps that are not
tapped, drill and tap the suction and discharge
lines not less than 18 inches (457,2 mm) from the
suction and discharge ports and install the lines.
Installation closer to the pump may result in erratic
readings.
PAGE B - 2INSTALLATION
10 SERIESOM-06592
SUCTION LINES
To avoid air pockets which could affect pump prim
ing, the suction line must be as short and direct as
possible. When operation involves a suction lift, the
line must always slope upward to the pump from
the source of the liquid being pumped; if the line
slopes down to the pump at any point along the
suction run, air pockets will be created.
Fittings
Suction lines should be the same size as the pump
inlet. If reducers are used in suction lines, they
should be the eccentric type, and should be in
stalled with the flat part of the reducers uppermost
to avoid creating air pockets. Valves are not nor
mally used in suction lines, but if a valve is used,
install it with the stem horizontal to avoid air pock
ets.
Strainers
ommendations when selecting and applying the
pipe dope. The pipe dope should be compatible
with the liquid being pumped.
Suction Lines In Sumps
If a single suction line is installed in a sump, it
should be positioned away from the wall of the
sump at a distance equal to 1‐1/2 times the diame
ter of the suction line.
If there is a liquid flow from an open pipe into the
sump, the flow should be kept away from the suc
tion inlet because the inflow will carry air down into
the sump, and air entering the suction line will re
duce pump efficiency.
If it is necessary to position inflow close to the suc
tion inlet, install a baffle between the inflow and the
suction inlet at a distance 1‐1/2 times the diameter
of the suction pipe. The baffle will allow entrained
air to escape from the liquid before it is drawn into
the suction inlet.
If a strainer is furnished with the pump, be certain
to use it; any spherical solids which pass through a
strainer furnished with the pump will also pass
through the pump itself.
If a strainer is not furnished with the pump, but is
installed by the pump user, make certain that the
total area of the openings in the strainer is at least
three or four times the cross section of the suction
line, and that the openings will not permit passage
of solids larger than the solids handling capability
of the pump.
This pump is designed to handle up to 3‐inch (76,2
mm diameter spherical solids.
Sealing
Since even a slight leak will affect priming, head,
and capacity, especially when operating with a
high suction lift, all connections in the suction line
should be sealed with pipe dope to ensure an air
tight seal. Follow the sealant manufacturer's rec
If two suction lines are installed in a single sump,
the flow paths may interact, reducing the efficiency
of one or both pumps. To avoid this, position the
suction inlets so that they are separated by a dis
tance equal to at least 3 times the diameter of the
suction pipe.
Suction Line Positioning
The depth of submergence of the suction line is
critical to efficient pump operation. Figure B-1
shows recommended minimum submergence vs.
velocity.
NOTE
The pipe submergence required may be reduced
by installing a standard pipe increaser fitting at the
end of the suction line. The larger opening size will
reduce the inlet velocity. Calculate the required
submergence using the following formula based
on the increased opening size (area or diameter).
PAGE B - 3INSTALLATION
OM-0659210 SERIES
Figure B-1. Recommended Minimum Suction Line Submergence vs. Velocity
DISCHARGE LINES
Siphoning
Do not terminate the discharge line at a level lower
than that of the liquid being pumped unless a si
phon breaker is used in the line. Otherwise, a si
phoning action causing damage to the pump
could result.
Valves
If a throttling valve is desired in the discharge line,
use a valve as large as the largest pipe to minimize
friction losses. Never install a throttling valve in a
suction line.
A check valve in the discharge line is normally rec
ommended, but it is not necessary in low dis
charge head applications.
With high discharge heads, it is recommended that
a throttling valve and a system check valve be in
stalled in the discharge line to protect the pump
from excessive shock pressure and reverse rota
tion when it is stopped.
If the application involves a high discharge
head, gradually close the discharge
throttling valve before stopping the pump.
Bypass Lines
Self‐priming pumps are not air compressors. Dur
ing the priming cycle, air from the suction line must
be vented to atmosphere on the discharge side. If
the discharge line is open, this air will be vented
through the discharge. However, if a check valve
has been installed in the discharge line, the dis
charge side of the pump must be opened to atmos
pheric pressure through a bypass line installed be
tween the pump discharge and the check valve. A
self‐priming centrifugal pump will not prime if
there is sufficient static liquid head to hold the dis
charge check valve closed.
NOTE
The bypass line should be sized so that it does not
affect pump discharge capacity; however, the by
pass line should be at least 1 inch (25,4 mm) in di
PAGE B - 4INSTALLATION
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