GORMAN-RUPP PUMPS T SERIES User manual

OM---01936---OB03
August 15, 1984
Rev. K 11/22/02
CDSW
THE GORMAN-RUPP COMPANY DMANSFIELD, OHIO
GORMAN-RUPP OF CANADA LIMITED DST. THOMAS, ONTARIO, CANADA Printed in U.S.A.
www.gormanrupp.com
ECopyright by the Gorman-Rupp Company
INSTALLATION, OPERATION,
AND MAINTENANCE MANUAL
WITH PARTS LIST
TSERIESPUMP
MODEL
T10A61---B
INCLUDING: /FM, /WW

TABLE OF CONTENTS
i
INTRODUCTION PAGE I --- 1.................................................
SAFETY --- SECTION A PAGE A --- 1...........................................
INSTALLATION --- SECTION B PAGE B --- 1....................................
Pump Dimensions PAGE B --- 1.....................................................
PREINSTALLATION INSPECTION PAGE B --- 1............................................
Battery Specifications And Installation PAGE B --- 2....................................
POSITIONING PUMP PAGE B --- 2.......................................................
Lifting PAGE B --- 2.................................................................
Mounting PAGE B --- 2.............................................................
SUCTION AND DISCHARGE PIPING PAGE B --- 2.........................................
Materials PAGE B --- 2..............................................................
Line Configuration PAGE B --- 2......................................................
Connections to Pump PAGE B --- 2..................................................
Gauges PAGE B --- 3...............................................................
SUCTION LINES PAGE B --- 3...........................................................
Fittings PAGE B --- 3...............................................................
Strainers PAGE B --- 3..............................................................
Sealing PAGE B --- 3...............................................................
Suction Lines In Sumps PAGE B --- 3.................................................
Suction Line Positioning PAGE B --- 3................................................
DISCHARGE LINES PAGE B --- 4........................................................
Siphoning PAGE B --- 4.............................................................
Valves PAGE B --- 4................................................................
Bypass Lines PAGE B --- 4..........................................................
AUTOMATIC AIR RELEASE VALVE PAGE B --- 5...........................................
Theory of Operation PAGE B --- 6....................................................
Air Release Valve Installation PAGE B --- 6............................................
ALIGNMENT PAGE B --- 7..............................................................
Coupled Drives PAGE B --- 8........................................................
V-Belt Drives PAGE B --- 8...........................................................
OPERATION --- SECTION C PAGE C --- 1......................................
PRIMING PAGE C --- 1.................................................................
STARTING PAGE C --- 1................................................................
OPERATION PAGE C --- 1..............................................................
Lines With a Bypass PAGE C --- 1....................................................
Lines Without a Bypass PAGE C --- 1.................................................
Leakage PAGE C --- 2..............................................................
Liquid Temperature And Overheating PAGE C --- 2.....................................
Strainer Check PAGE C --- 2.........................................................
Pump Vacuum Check PAGE C --- 2..................................................
STOPPING PAGE C --- 3................................................................
Cold Weather Preservation PAGE C --- 3..............................................
BEARING TEMPERATURE CHECK PAGE C --- 3..........................................
TROUBLE SHOOTING --- SE CTION D PAGE D --- 1..............................
PREVENTIVE MAINTENANCE PAGE D --- 3...............................................

TABLE OF CONTENTS
(continued)
ii
PUMP MAINTENANCE AND REPAIR --- SECTION E PAGE E --- 1................
PERFORMANCE CURVE PAGE E --- 1...................................................
PARTS LISTS:
Pump Model PAGE E --- 3..........................................................
Repair Rotating Assembly PAGE E --- 5...............................................
PUMP AND SEAL DISASSEMBLY AND REASSEMBLY PAGE E --- 6.........................
Cleanout Access And Suction Check Valve Removal PAGE E --- 6.......................
Suction Head And Wear Plate Removal PAGE E --- 6...................................
Rotating Assembly Removal PAGE E --- 7.............................................
Impeller Removal PAGE E --- 8......................................................
Seal Removal And Disassembly PAGE E --- 8.........................................
Shaft and Bearing Removal and Disassembly PAGE E --- 8.............................
Shaft and Bearing Reassembly and Installation PAGE E --- 9............................
Seal Reassembly and Installation PAGE E --- 10........................................
Impeller Installation PAGE E --- 12.....................................................
Rotating Assembly Installation PAGE E --- 13...........................................
Suction Head And Wear Plate Installation PAGE E --- 13.................................
Suction Check Valve Installation PAGE E --- 13.........................................
PRESSURE RELIEF VALVE MAINTENANCE PAGE E --- 14..................................
LUBRICATION PAGE E --- 14.............................................................
Seal Assembly PAGE E --- 14.........................................................
Bearings PAGE E --- 14..............................................................

TSERIES OM--01936
PAGE I -- 1INTRODUCTION
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 Installation, Operation, and Maintenance
manual is designed to help you achieve the best
performance and longest life from your Gorman-
Rupp pump.
This pump is a T Series, semi-open impeller, self-
priming centrifugal model with a suction check
valve. The pump is designed for handling mild in-
dustrial corrosives, residues and slurries contain-
ing large entrained solids. The basic material of
constructionisgrayiron, withstainless steelimpel-
ler, impeller shaft and wearing parts.
Ifthereareanyquestionsregardingthepump orits
applicationwhicharenotcoveredinthismanualor
in other literature accompanying this unit, please
contact your Gorman-Rupp distributor, or write:
The Gorman-Rupp Company
P.O. Box 1217
Mansfield, Ohio 44901--1217
Phone: [phone]
or:
Gorman-Rupp of Canada Limited
70 Burwell Road
St. Thomas, Ontario N5P 3R7
Phone: [phone]
Forinformationortechnicalassistanceonthepow-
er source, contact the power source manufactur-
er’s local dealer or representative.
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
neitheroperatorsafetynorpumpintegrity arecom-
promised by the installation. Pumps and related
equipment must be installed and operated ac-
cording to all national, local and industry stan-
dards.
The following are used to alert maintenance per-
sonnel to procedures which require special atten-
tion,tothosewhichcoulddamage 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.
HazardsorunsafepracticeswhichCOULD
result in minor personal injury or product
or property damage. These instructions
describe the requirements and the possi-
ble damage which couldresult from failure
to follow the procedure.
NOTE
Instructions to aid in installation, operation,and
maintenance, or which clarify a procedure.

TSERIES OM--01936
PAGE A -- 1SAFETY
SAFETY --- SECTION A
This information applies to T Series ba-
sic pumps. Gorman-Rupp has no con-
trol over or particular knowledge of the
power source which will be used. Refer
to the manual accompanying the power
source before attempting to begin op-
eration.
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.
Beforeattemptingtoopenorservicethe
pump:
1. Familiarize yourself with this man-
ual.
2. Disconnect or lock out the power
source, or take other action to en-
sure that the pump will remain in-
operative.
3. Allow the pump to completely cool
if overheated.
4. Vent the pump slowly and cau-
tiously.
5. Close the suction and discharge
valves.
6. Check the temperature before
opening any covers, plates, or
plugs.
7. Drain the pump.
This pump is designed to handle mild
industrial corrosives, mud and slurries
containing large entrained solids. Do
not attempt to pump volatile, flam-
mable, or highly corrosive liquids
which may damage the pump or endan-
ger personnel as a result of pump fail-
ure.
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
shields and /or guards in place over the
drive shafts, belts and/or couplings, or
other rotating parts. Exposed rotating
parts can catch clothing, fingers, or
tools. causing severe injury to person-
nel.
Do not operate the pump against a
closed discharge valve for long periods
oftime.Ifoperatedagainstacloseddis-
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.

TSERIESOM--01936
PAGE A -- 2 SAFETY
Use lifting and moving equipment in
good repair and with adequate capacity
to prevent injuries to personnel or dam-
age to equipment.
Overheated pumps can cause severe
burns and injury. If overheating of the
pump occurs:
1. Stop the pump immediately.
2. Allowthepumptocompletelycool.
3. Refertoinstructionsinthismanual
before restarting the pump.
Donotattempttodisengageanypartof
an overheated pump unit. Vapor pres-
sure within the pump casing can eject
these parts with great force when they
are disengaged. Allow the pump to
completely cool before servicing it.
Use lifting and moving equipment in
good repair and with adequate capacity
to prevent injuries to personnel or dam-
age to equipment.

OM--01936TSERIES
PAGE B -- 1INSTALLATION
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 posi-
tionedabovethefreelevelofliquidtobepumped.
If installedinafloodedsuctionapplicationwhere
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.
Forfurther assistance,contact yourGorman-Rupp
distributor or the Gorman-Rupp Company.
Pump Dimensions
SeeFigure1fortheapproximatephysicaldimen-
sionsofthispump.
OUTLINE DRAWING
Figure 1. Pump Model T10A61--B
PREINSTALLATION INSPECTION
The pump assemblywas inspectedand tested be-
fore shipment from the factory. Before installation,
inspect the pump for damage whichmay haveoc-
curred during shipment. Check as follows:
a. Inspectthepump forcracks,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 warnings and cautions con-
tained in this manual or affixed to the pump,
and perform all duties indicated. Note the di-
rection of rotation indicated on the pump.

OM--01936 TSERIES
PAGE B -- 2 INSTALLATION
Check that the pump shaft rotates counter-
clockwise when facing the impeller.
Only operate this pump in the direction in-
dicated by the arrow on the pump body
and on the accompanying decal. Refer to
Rotation in OPERATION,SectionC.
d. Check levels and lubricate as necessary. Re-
fer to LUBRICATION in the MAINTENANCE
AND REPAIR section of this manual and per-
form duties as instructed.
e.Ifthepumpandpowersourcehavebeen
stored for more than 12 months, some of the
components or lubricants may have ex-
ceeded their maximum shelf life. These must
be inspected or replaced to ensure maxi-
mum pump service.
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-
minethe repairor updating policy. Donotputthe
pump into service until appropriate action has
been taken.
POSITIONING PUMP
Lifting
Use lifting equipment with a capacity of at least
6,700 pounds. This pump weighs approximately
1,340 pounds, not including the weight of acces-
sories or customer installed equipment. Customer
installed equipment such as suction and dis-
chargepipingmustberemovedbeforeattempting
to lift.
Make sure that hoists and other lifting equipment
are of sufficient capacity tosafelyhandle the pump
assembly.Ifchainsandcablesareused,makecer-
tain that they are positioned so that they will not
damage the pump, and so thatthe loadwill bebal-
anced.
Thepumpassemblycanbeseriously
damaged ifthecables or chainsusedtolift
andmovetheunitareimproperlywrapped
around the pump.
Mounting
Locatethepumpinanaccessibleplaceascloseas
practical tothe liquid being pumped. Levelmount-
ing is essential for proper operation.
The pump may have to be supported or shimmed
to provide for level operation or to eliminate vibra-
tion.
SUCTION AND DISCHARGE PIPING
Pump performance is adversely effected by in-
creased suction lift, discharge elevation, and fric-
tion losses. See the performance curve and oper-
ating range shown on Page E-1 to be sure your
overall application allows the 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
compatiblewiththeliquidbeingpumped.Ifhoseis
used insuction lines, it must be the rigid-wall, rein-
forced type to prevent collapseunder 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-
tiallyincreasefriction loss.Ifelbowsarenecessary,
use the long-radius type to minimize friction loss.
Connections to Pump
Before tightening a connecting flange, align it ex-
actly with the pump port. Never pulla pipe line into
place by tightening the flange bolts and/or cou-
plings.

OM--01936TSERIES
PAGE B -- 3INSTALLATION
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
linesareused,theyshouldhaveadequatesupport
to secure them when filled with liquid and under
pressure.
Gauges
Most pumps are drilled and tapped for installing
dischargepressureandvacuumsuctiongauges.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 mm) from the
suction and discharge ports and install the lines.
Installation closer to the pump mayresult in erratic
readings.
SUCTION LINES
Toavoidairpockets whichcouldaffectpumpprim-
ing, the suction line must be as short and direct as
possible.Whenoperationinvolvesasuctionlift,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 withthe flat part ofthe 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
If a strainer is furnished with the pump, be certain
touseit;anysphericalsolidswhichpass througha
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 willnot permit passage
of solids larger than the solids handling capability
of the pump.
Thispumpisdesignedtohandleupto3-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-
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 distanceequalto 1-1/2 times thediame-
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 willcarry air downinto
the sump, and air entering the suction line will re-
duce pump efficiency.
If it is necessary to position inflow close to the suc-
tioninlet, installa bafflebetween theinflow 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 two suction lines are installed in a single sump,
theflowpathsmayinteract, reducingtheefficiency
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 2 shows
recommended minimum submergence vs. veloc-
ity.

OM--01936 TSERIES
PAGE B -- 4 INSTALLATION
NOTE
The pipe submergence required may be reduced
by installing a standard pipe increaser fitting at the
end of thesuction 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).
Figure 2. 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
A check valve in the discharge line is normally rec-
ommended, but it is not necessary in low dis-
charge head applications.
If a throttling valve is desired in the discharge line,
useavalveaslargeasthelargestpipetominimize
friction losses. Never install a throttling valve in a
suction line.
Withhighdischargeheads,itisrecommendedthat
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.
Ifthe application involves a highdischarge
head, gradually close the discharge
throttling valve before stopping the pump.
Bypass Lines
If it is mecessary to permit the escape of air to at-
mosphere during initial priming or in the repriming
cycle, install a bypass line between th epump and
thedischargecheck valve. Thebypasslineshould
be sized sothat it does not affect pump discharge
capacity.
ItisrecommendedthataGorman---RuppAutomat-
ic Air Release Valve be installed in the bypass line.

OM--01936TSERIES
PAGE B -- 5INSTALLATION
Do Not install a manual shut---off valve in a bypass
line. If a manual shut---off valve is installed to facili-
tateserviceoftheAirReleaseValve,thevalvemust
not be left closed during operation. See the sup-
plement at the end of this section for additional in-
formation on bypass lines and the Gorman---Rupp
Automatic Air Release Valve.
NOTE
Thebypass line may clog occasionally, particularly
when pumping liquids containing large solids. If
cloggingoccurs,locateandremovetheclog. Ifthe
clog is located between the discharge check valve
andtheAirReleaseValve,thevalvewillnotclose. If
the clog is located in theRelief Valve itself, or in the
line between the Relief Valve and the sump, the
valve will not open.
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 could result, causing damage to
the pump.
Inlow discharge head applications (less than 30
feet or 9,1 meters), it is recommended that the by-
pass line be run back to the wet well, and located 6
inches (152,4 mm) below the water level or cut-off
point of the low level pump. In some installations,
this bypass line may be terminated with a six-to-
eight foot length of 1-1/4 inch (31,8 mm) I.D.
smooth-bore hose; air and liquid vented during
the priming process will then agitate the hose and
break up any solids, grease, or other substances
likely to cause clogging.
A bypass line that is returned to a wet well
must be secured against being drawn into
the pump suction inlet.
It is also recommended that pipe unions be in-
stalled at each 90_elbow in a bypass line to ease
disassembly and maintenance.
In high discharge head applications (more than
30 feet or 9,1 meters), an excessive amount of liq-
uid may be bypassed and forced back to the wet
well under the full working pressure of the pump;
this will reduce overall pumping efficiency. There-
fore, it is recommended that a Gorman-Rupp
Automatic Air Release Valve be installed in the
bypass line.
Gorman-Rupp Automatic Air Release Valves are
reliable, and require minimum maintenance. See
AUTOMATIC AIRRELEASE VALVEin this section
for installation and theory of operation of the Auto-
matic Air Release Valve. Consult your Gorman-
Rupp distributor, or contact the Gorman-Rupp
CompanyforselectionofanAutomaticAirRelease
Valve to fit your application.
A manual shut-off valve should not be
installed in any bypass line. A manual
shut-off valve may inadvertently be left
closed during operation. A pump which
has lost prime may continue to operate
without reaching prime, causing dan-
gerousoverheating and possible explo-
sive rupture of the pump casing. Per-
sonnel could be severely injured.
Allow an over-heated pump to cool be-
fore servicing. Do not remove plates,
covers,gauges, orfittingsfroman over-
heated pump. Liquid within the pump
can reach boiling temperatures, and va-
porpressurewithinthe pump cancause
parts being disengaged to be ejected
with great force. After the pump cools,
drain the liquid from the pump by re-
moving the casing drain plug. Use cau-
tion when removing the plug to prevent
injury to personnel from hot liquid.
AUTOMATIC AIR RELEASE VALVE
When properly installed and correctly adjusted to
the specific hydraulic operating conditions of the
application, the Gorman-Rupp Automatic Air Re-
leaseValvewillpermitairtoescapethroughtheby-
pass line, and then close automatically when the
pump is fully primed and pumping at fullcapacity.

OM--01936 TSERIES
PAGE B -- 6 INSTALLATION
Theory of Operation
Figures 3 and 4 show a cross-sectional view of the
AutomaticAir Release Valve, and a corresponding
description of operation.
Figure 3 Valve in Open Position
Duringthe priming cycle, airfrom the pumpcasing
flowsthroughthebypassline,andpassesthrough
theAirReleaseValvetothewetwell(Figure3).
Figure 4 Valve in Closed Position
When the pump is fully primed, pressure resulting
from flow against the valve diaphragm com-
presses the spring and closes the valve (Figure 4).
The valve will remain closed, reducing the bypass
ofliquidto1to5gallonsperminute,untilthepump
loses its prime or stops.
Some leakage (1 to 5 gallons [3.8 to 19
liters] per minute) will occur when the
valve is fullyclosed. Be sure the bypass
line is directed back to the wet well or
tank to prevent hazardous spills.
Whenthepumpshutsdown,thespringreturnsthe
diaphragm to its original position. Any solids that
mayhave accumulatedin the diaphragm chamber
settle to the bottom and are flushedout duringthe
next priming cycle.
NOTE
The valve will remain open if the pump does not
reach its designed capacity or head. Valve closing
pressureis dependent upon thedischargehead of
the pump at full capacity. The range of the valve
closing pressure is established by the tension rate
ofthespringasorderedfromthefactory.Valveclos-
ing pressure can be further adjusted to the exact
system requirements by moving the spring retain-
ing pin up or down the plunger rod to increase or
decrease tension on the spring. Contact your Gor-
man-Rupp distributor or the Gorman-Rupp Com-
pany for information about an Automatic Air Re-
lease Valve for your specific application.
Air Release Valve Installation
The Automatic Air Release Valve must be inde-
pendently mounted in a horizontal position and
connected to the discharge line of the self-priming
centrifugal pump (see Figure 5).
NOTE
IftheAirReleaseValveistobeinstalledonastaged
pump application, contact the factory for specific
installation instructions.

OM--01936TSERIES
PAGE B -- 7INSTALLATION
DISCHARGE PIPE
DISCHARGE
CHECK VALVE
PUMP DISCHARGE
SELF-PRIMING
CENTRIFUGAL
PUMP
SUCTION
LINE
SUPPORT
BRACKET
CLEAN-OUT
COVER
INSTALL AIR RELEASE VALVE
IN HORIZONTAL POSITION
90_LONG
RADIUS
ELBOW
WET WELL
OR SUMP
BLEED LINE 1”
(25,4 MM) DIA. MIN.
(CUSTOMER FUR-
NISHED) EXTEND 6”
(152 MM) BELOW
PUMP OFF LIQUID
LEVEL
Figure 5. Typical Automatic Air Release Valve Installation
The valve inlet line must be installed between the
pumpdischargeportandthenon-pressurizedside
of the discharge check valve. The valve inlet is at
thelargeendofthevalvebody,andisprovided
with standard 1 inch NPT pipe threads.
The valve outlet is located at the opposite end of
the valve, and is also equipped with standard 1
inch NPT pipe threads. The outlet should be con-
nectedtoableedlinewhichslopesbackto the wet
well orsump. The bleed line must be the same size
astheinletpiping, orlarger. Ifpipingisusedforthe
bleed line, avoid the use of elbows whenever pos-
sible.
NOTE
It is recommended that each Air Release Valve be
fitted with an independent bleeder line directed
back to the wet well. If multiple Air Release Valves
areinstalledinasystem,theymustbefitted with in-
dependent bleeder lines; never use a common
manifold pipe. Contact your Gorman-Rupp dis-
tributor or the Gorman-Rupp Company for informa-
tion about installation of an Automatic Air Release
Valve for your specific application.
ALIGNMENT
The alignment ofthe pump and itspower source is
critical for trouble-free mechanical operation. In
either a flexible coupling or V-belt driven system,
thedriverandpumpmustbemountedsothattheir
shaftsare alignedwith andparallelto each other. It
is imperative that alignment be checked after the
pump and piping are installed, and before opera-
tion.
NOTE
Check Rotation, Section C, before final alignment
of the pump.
WhenmountedattheGorman-Ruppfactory,driver
andpumparealignedbeforeshipment.Misalign-
ment will occur in transit and handling. Pumps
must be checked and realigned before operation.
Before checking alignment, tighten the foundation
bolts. The pump casing feet and/or pedestal feet,
andthedrivermountingboltsshouldalsobetightly
secured.

OM--01936 TSERIES
PAGE B -- 8 INSTALLATION
When checking alignment, disconnect
the power source to ensure that the
pump will remain inoperative.
Adjusting the alignment in one direction
may alter the alignment in another direc-
tion. check each procedure after altering
alignment.
Coupled Drives
When using couplings, the axis of the power
source must be aligned to the axis of the pump
shaft in both the horizontal and vertical planes.
Mostcouplings requirea specificgap or clearance
between the drivingand the driven shafts. Refer to
the coupling manufacturer’s service literature.
Alignspiderinserttypecouplingsbyusingcalipers
to measure the dimensions on the circumference
of the outer ends of the coupling hub every 90 de-
grees. The coupling is in alignment when the hub
ends are the same distance apart at all points (see
Figure 6A).
Figure 6A. Aligning Spider-Type Couplings
Figure6B. Aligning Non-Spider Type Couplings
Align non-spider type couplings by using a feeler
gaugeortapergaugebetweenthecouplinghalves
every 90 degrees. The coupling is in alignment
whenthehubsarethesamedistanceapartatall
points (see Figure 6B).
Checkparalleladjustmentbylayingastraightedge
across both coupling rims at the top, bottom, and
side. When the straightedge rests evenly on both
halves of the coupling, the coupling is in horizontal
parallel alignment. If the coupling is misaligned,
use a feeler gauge between the coupling and the
straightedge to measure the amount of misalign-
ment.
V-Belt Drives
When using V-belt drives, the power source and
the pump must be parallel. Use a straightedge
alongthesidesofthepulleystoensurethatthepul-
leys are properly aligned (see Figure 6C). In drive
systemsusingtwoormorebelts,makecertainthat
the belts are a matched set; unmatched sets will
cause accelerated belt wear.
MISALIGNED:
SHAFTS
NOT P
A
R
A
LLEL
MISALIGNED:
SHAFTS
NOT IN LINE
ALIGNED: SHAFTS
PARALLEL AND
SHE
A
V
ES IN LINE
Figure 6C. Alignment of V-Belt Driven Pumps

OM--01936TSERIES
PAGE B -- 9INSTALLATION
Tightenthebeltsinaccordancewiththebeltmanu-
facturer’s instructions. If the belts are too loose,
they will slip; if the belts are too tight, there will be
excessive power loss and possible bearing failure.
Select pulleys that will match the proper speed ra-
tio; overspeeding the pump may damage both
pump and power source.
Do not operate the pump without the
guard in place over the rotating parts.
exposed rotating parts can catch cloth-
ing, fingers, or tools, causing severe in-
jury to personnel.

TSERIES OM--01936
OPERATION PAGE C -- 1
OPERATION --- SECTION C
Review all SAFETY information in Section A.
Follow the instructions on all tags, labels and de-
cals attached to the pump.
This pump is designed to handle mild
industrialcorrosives,residuesand slur-
ries containing large entrained solids.
Do not attempt to pump volatile, corro-
sive, or flammable materials which may
damage the pump or endanger person-
nel as a result of pump failure.
Pump speed and operating condition
points must be within the continuous per-
formance range shown on the curve.
(See Section E, Page 1.)
PRIMING
Install the pump and piping as described in IN-
STALLATION. Make sure that the piping connec-
tions are tight, and that the pump is securely
mounted. Check that the pump is properly lubri-
cated (see LUBRICATION in MAINTENANCE
AND REPAIR).
This pump is self-priming, but the pump should
never be operated unless there is liquid in the
pump casing.
Never operate this pump unless there is
liquid in the pump casing. The pump will
not prime when dry. Extended operationof
a dry pump will destroy the seal assembly.
Add liquid to the pump casing when:
1. The pump is being put into service for the
first time.
2. Thepumphas notbeenusedforaconsider-
able length of time.
3. The liquid in the pump casing has evapo-
rated.
Once the pump casing has been filled, the pump
will prime and reprime as necessary.
After filling the pump casing, reinstall
and tighten the fill plug. Do not attempt
to operate the pump unlessall connect-
ing piping is securely installed. Other-
wise, liquid in the pump forced out
under pressure could cause injury to
personnel.
To fill the pump, remove the pump casing fillcover
or fill plug in the top of the casing, and add clean
liquid until the casing is filled. Replace the fill cover
or fill plug before operating the pump.
STARTING
Consult the operations manual furnished with the
power source.
OPERATION
Lines With a Bypass
Ifa Gorman-RuppAutomaticAirReleaseValvehas
been installed, the valve will automatically open to
allow the pump to prime, and automatically close
after priming is complete (see INSTALLATION for
Air Release Valve operation).
If the bypass line is open, air from the suction line
willbe discharged through the bypass line back to
thewetwellduringtheprimingcycle.Liquidwill
then continue to circulate through the bypass line
while the pump is in operation.
Lines Without a Bypass
Open all valves in the discharge line and start the
power source. Priming is indicated by a positive

TSERIES
OM--01936
OPERATIONPAGE C -- 2
reading on the discharge pressure gauge or by a
quieter operation. The pump maynot primeimme-
diately because the suction line must first fill with
liquid.If the pumpfailstoprimewithin five minutes,
stop it and check the suction line for leaks.
Afterthepumphasbeenprimed,partiallyclosethe
discharge line throttling valve in order to fill the line
slowly and guard against excessive shock pres-
sure which could damage pipe ends, gaskets,
sprinkler heads, and any other fixtures connected
to the line. When the discharge line is completely
filled,adjustthethrottlingvalve tothe requiredflow
rate.
Do not operate the pump against a
closed discharge throttling valve for
long periods of time.If operated against
a closed discharge throttling valve,
pump components will deteriorate, and
the liquid could come to a boil, build
pressure,andcausethepump casingto
rupture or explode.
Leakage
No leakage should be visible at pump mating sur-
faces, or at pump connections or fittings. Keep all
lineconnectionsandfittingstighttomaintainmaxi-
mum pump efficiency.
Liquid Temperature And Overheating
The maximum liquid temperature for this pump is
160_F(71_C). Do not apply it ata higher operating
temperature.
Overheating can occur if operated with the valves
in the suction or discharge lines closed. Operating
against closed valves could bring the liquid to a
boil, build pressure, and cause the pump to rup-
ture or explode. If overheating occurs, stop the
pump and allow it to cool before servicing it. Refill
the pump casing with cool liquid.
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-
gagedtobeejectedwithgreatforce. Al-
low the pump to cool before servicing.
As asafeguard against rupture or explosion dueto
heat, this pump is equipped with a pressure relief
valve which will open if vapor pressure within the
pumpcasingreachesacriticalpoint.Ifoverheating
does occur, stop the pump immediately and allow
it to cool before servicing it. Approach any over-
heated pump cautiously. It is recommended that
the pressure relief valve assembly be replaced at
each overhaul, or any time the pump casing over-
heats and activates the valve. Never replace this
valve with a substitute which has not been speci-
fied or provided by the Gorman-Rupp Company.
Strainer Check
If a suction strainer has been shipped with the
pump or installed by the user, check the strainer
regularly, and clean it as necessary. The strainer
shouldalsobecheckedifpumpflowratebeginsto
drop. If a vacuum suction gauge has been in-
stalled, monitor and record the readings regularly
to detect strainer blockage.
Never introduce air or steam pressure into the
pump casing or piping to remove a blockage. This
could result in personal injury or damage to the
equipment. If backflushing is absolutely neces-
sary, liquid pressure must be limited to 50% of the
maximum permissible operating pressure shown
on the pump performance curve.
Pump Vacuum Check
Withthepumpinoperative, installavacuumgauge
in the system, using pipe dope on the threads.
Block the suction line andstart the pump. At oper-
ating speed the pump should pull a vacuum of 20
inches (508 mm) or more of mercury. If it does not,
check for airleaks inthe seal, gasket, ordischarge
valve.
Openthesuctionline,and readthevacuumgauge
with the pump primed and at operation speed.

TSERIES OM--01936
OPERATION PAGE C -- 3
Shut off the pump. The vacuumgauge reading will
immediately drop proportionate to static suction
lift,andshouldthenstabilize.Ifthevacuumreading
falls off rapidly after stabilization, an air leak exists.
Before checking for the source of the leak, check
the point of installation of the vacuum gauge.
STOPPING
Never halt the flow of liquid suddenly. If the liquid
being pumped is stopped abruptly, damaging
shock waves can be transmitted to the pump and
piping system. Close all connecting valves slowly.
On engine driven pumps, reduce the throttle
speedslowlyandallowtheenginetoidlebrieflybe-
fore stopping.
If the application involves a high discharge
head, gradually close the discharge
throttling valve before stopping the pump.
After stopping the pump, disconnect or lock out
the power source or take other action to ensure
that the pump will remain inoperative.
Cold Weather Preservation
In below freezing conditions, drain the pump to
prevent damage from freezing. Also, clean out any
solids by flushing with a hose. Operate the pump
for approximately one minute; this will remove any
remaining liquid that could freeze the pump rotat-
ing parts. If the pump will be idle for more than a
few hours, or if it has been pumping liquids con-
taining a large amount of solids, drain the pump,
and flush it thoroughly with cleanwater. Toprevent
large solids from clogging the drain port and pre-
venting the pump from completely draining, insert
a rod or stiff wire in the drain port, and agitate the
liquid during the draining process. Clean out any
remaining solids by flushing with a hose.
BEARING TEMPERATURE CHECK
Bearings normally run at higher than ambient tem-
peratures because of heat generated by friction.
Temperatures up to 160_F(71_C) are considered
normalforbearings,andtheycanoperatesafelyto
at least 180_F(82_C).
Checkingbearingtemperatures byhandisinaccu-
rate. Bearing temperatures can be measured ac-
curately by placing a contact-type thermometer
against the housing. Record this temperature for
future reference.
A sudden increase in bearing temperature is a
warning that the bearings are at thepoint of failing
to operate properly. Make certain that the bearing
lubricant is of the proper viscosity and at the cor-
rect level (see LUBRICATION in MAINTENANCE
AND REPAIR). Bearing overheating can also be
caused by shaft misalignment and/or excessive vi-
bration.
When pumps are first started, the bearings may
seem to run at temperatures above normal. Con-
tinued operation should bring the temperatures
down to normal levels.

OM--01936TSERIES
TROUBLESHOOTING PAGE D -- 1
TROUBLESHOOTING --- SECTION D
Review all SAFETY information in Section A.
Beforeattemptingtoopenorservice the
pump:
1. Familiarize yourself with this manual.
2. Disconnect or lock out the power
source, ortake other action toensure
that the pump will remain inopera-
tive.
3. Allow the pump to completely cool if
overheated.
4. Vent the pump slowly and cautiously.
5. Close the suction and discharge
valves.
6. Check the temperature before open-
ing any covers, plates, or plugs.
7. Drain the pump.
Table 1. Trouble Shooting Chart
TROUBLE POSSIBLE CAUSE PROBABLE REMEDY
PUMP FAILS TO PRIME Not enough liquid in casing.
Suction check valve contaminatedor
damaged.
Air leak in suction line.
Lining of suction hose collapsed.
Leakingorwornsealorpumpgas-
ket.
Suction lift or discharge head too
high.
Strainer clogged.
Addliquidtocasing.SeePRIMING.
Clean or replace check valve.
Correct leak.
Replace suction hose.
Check pump vacuum. Replace leak-
ingorwornsealorgasket.
Check piping installation and install
bypass line if needed. See INSTAL-
LATION.
Check strainer and clean if neces-
sary.
PUMP STOPS OR FAILS
TO DELIVER RATED
FLOW OR PRESSURE
Air leak in suction line.
Lining of suction hose collapsed.
Correct leak.
Replace suction hose.

OM--01936 TSERIES
TROUBLESHOOTINGPAGE D -- 2
Table 1. Trouble Shooting Chart (cont.)
TROUBLE POSSIBLE CAUSE PROBABLE REMEDY
PUMP STOPS OR FAILS
TO DELIVER RATED
FLOW OR PRESSURE
(cont.)
Leakingorwornsealorpumpgas-
ket.
Strainer clogged.
Suction intake not submerged at
proper level or sump too small.
Impellerorotherwearingparts
worn or damaged.
Impeller clogged.
Discharge head too high.
Suction lift too high.
Pump speed too slow.
Check pump vacuum. Replace
leakingorwornsealorgasket.
Check strainer and clean if neces-
sary.
Check installation and correct sub-
mergence as needed.
Replace worn or damaged parts.
Check that impeller is properly cen-
tered and rotates freely.
Free impeller of debris.
Install bypass line.
Measure lift w/vacuum gauge. Re-
duce lift and/or friction losses in
suction line.
Check engine output; consult en-
gine operation manual.
PUMP REQUIRES TOO
MUCH POWER Pump speed too high.
Discharge head too low.
Liquid solution too thick.
Bearing(s) frozen.
Check engine output.
Adjust discharge valve.
Dilute if possible.
Disassemble pump and check
bearing(s).
PUMP CLOGS
FREQUENTLY Discharge flow too slow.
Suction check valve or foot valve
clogged or binding.
Liquid solution too thick.
Open discharge valve fully to in-
crease flow rate, and run engine at
maximum governed speed.
Clean valve.
Dilute if possible.
EXCESSIVE NOISE Cavitation in pump.
Pumping entrained air.
Pump or drive not securely
mounted.
Impeller clogged or damaged.
Reduce suction lift and/or friction
losses in suction line. Record vacu-
um and pressure gauge readings
and consult local representative or
factory.
Locate and eliminate source of air
bubble.
Secure mounting hardware.
Clean out debris; replace damaged
parts.