Gorman-Rupp Pumps 12B22-B User Manual

C
OM-00589-OB03
June 17, 1994
INSTALLATION, OPERATION,
AND MAINTENANCE MANUAL
10 SERIES PUMPS
MODEL
12B22---B
THE GORMAN-RUPP COMPANY D MANSFIELD, OHIO
GORMAN-RUPP OF CANADA LIMITED D ST. THOMAS, ONTARIO, CANADA Printed in U.S.A.
eCopyright by the Gorman-Rupp Company

TABLE OF CONTENTS

INTRODUCTION PAGE I --- 1.................................................
WARN ING S - SE CTI ON A PA GE A --- 1........................................
IN STA L LAT ION --- S E CT ION B PA GE B --- 1....................................
Pump Dimensions PAGE B --- 1.....................................................
PREINSTALLATION INSPECTION PAGE B --- 1............................................
POSITIONING PUMP PA GE B --- 2.......................................................
Lifting PA GE B --- 2.................................................................
Mounting PA GE B --- 2.............................................................
Clearance PA GE B --- 2.............................................................
SUCTION AND DISCHARGE PIPING PAGE B --- 2.........................................
Materials PA GE B --- 2..............................................................
Line Configuration PAGE B --- 2......................................................
Connections to Pump PAGE B --- 2..................................................
Gauges PA GE B --- 3...............................................................
SUCTION LINES PAGE B --- 3...........................................................
Fittings PA GE B --- 3...............................................................
Strainers PA GE B --- 3..............................................................
Sealing PAGE B --- 3...............................................................
Suction Lines In Sumps PAGE B --- 3.................................................
Suction Line Positioning PAGE B --- 3................................................
DISCHARGE LINES PA GE B --- 4........................................................
Siphoning PAGE B --- 4.............................................................
Valves PA GE B --- 4................................................................
Bypass Lines PAGE B --- 4..........................................................
AUTOMATIC AIR RELEASE VALVE PAGE B --- 5...........................................
Theory of Operation PAGE B --- 5....................................................
Air Release Valve Installation P AGE B -- - 6............................................
ALIGNMENT PAGE B --- 7..............................................................
Coupled Drives PA GE B --- 8........................................................
V --- Belt Drives PA GE B --- 8.........................................................
OPER AT IO N --- S ECT IO N C PAG E C --- 1......................................
PRIMING PA GE C --- 1.................................................................
STARTING PA GE C --- 1................................................................
Rotation PA GE C --- 1..............................................................
OPERATION PAGE C --- 2..............................................................
Lines W ith a Bypass PAGE C --- 2....................................................
Lines Without a Bypass PAGE C --- 2.................................................
Leakage PA GE C --- 2..............................................................
Liquid Temperature And Overheating PAGE C --- 2.....................................
Strainer Check PAGE C --- 2.........................................................
Pump Vacuum Check PAGE C --- 2..................................................
STOPPING PA GE C --- 3................................................................
Cold Weather Preservation PAGE C --- 3..............................................
BEARING TEMPERATURE CHECK PAGE C --- 3..........................................
TR OUB LES HOO TI NG --- SE C TIO N D PA GE D --- 1..............................
i
TABLE OF CONTENTS
(continued)
PUMP MAINTENANCE AND REPAIR - SECTION E PAGE E --- 1.................
STANDARD PERFORMANCE CURVE PAGE E --- 1........................................
PARTS LIST:
Pump Model PA GE E --- 3..........................................................
PUMP AND SEAL DISASSEMBLY AND REASSEMBLY PAGE E --- 4.........................
Suction Check Valve Removal and Disassembly PAGE E --- 4...........................
Back Cover Removal PA GE E --- 4...................................................
Pump Casing Removal PAGE E --- 4.................................................
Impeller Removal P AGE E -- - 5......................................................
Seal Removal and Disassembly PAGE E --- 5..........................................
Shaft and Bearing Removal and Disassembly PAGE E --- 5.............................
Shaft and Bearing Reassembly and Installation PAGE E --- 6............................
Seal Reassembly and Installation PAGE E - -- 7........................................
Impeller Installation And Adjustment P AGE E -- - 9......................................
Pump Casing Installation PAGE E --- 9................................................
Back Cover Installation PAGE E --- 9.................................................
Suction Check Valve Installation P AGE E --- 9.........................................
Final Pump Assembly PAGE E --- 10..................................................
LUBRICATION PA GE E --- 10.............................................................
Seal Assembly PAGE E --- 10.........................................................
Bearings PAGE E --- 10..............................................................
Power Sou rce PA GE E --- 10.........................................................
ii
10 SERIES
OM--00589--03

INTRODUCTION

This Installation, Operation, and Maintenance manual is designed to help you achieve the best performance and longest life from your Gorman­Rupp pump.
This pump is a 10 Series, semi-open impeller,self­priming centrifugal model with a suction check valve.Thepumpisdesignedforhandlingcorrosive liquids containing specified entrained solids, resi­dues and slurries. The basic material of construc-
The Gorman-Rupp Company or Gorman-Rupp of Canada Limited P.O. Box 1217 70 Burwell Road Mansfield, Ohio 44901-1217 St. Thomas, Ontario N5P 3R7
The following are used t o alert maintenance personnel to procedures which require special attention, to those which could damage equipment, and to those which could be dangerous to personnel:
tion for wetted parts is type 316 stainless steel. Forinformation ortechnicalassistance onthe pow-
er source, contact the power source manufactur­er’s local dealer or representative.
If there are any questions regarding the pump or its application which are not covered in this man­ual or in other literature accompanying this unit, please contact your Gorman-Rupp distributor, or write:
Immediate hazards whichWILL result in severe personal injury or death. These instructions describe the procedure re­quired and the injury which will result from failure to follow the procedure.
Hazards or unsafe practices which COULDresult 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 possi­ble damagewhich could result fromfailure to follow the procedure.
NOTE
Instructions to aid in installation, operation, and maintenance or which clarify a procedure.
PAGE I -- 1INTRODUCTION
10 SERIES
SAFETY - SECTION A
Thisinformationappliesto10Seriesba ­sic pumps. Gorman-Rupp has no con­trol over or particular knowledge of the power source which will be used. Refer to the manual accompanying the power sourcebefore attempting to beginoper­ation.
OM--00589--03
Afterthe pump hasbeen installed,make certain that the pump and all piping or hose connections are tight, properly supportedand securebeforeoperation.
Beforeattempting toopenorservic e the pump:
1. Familiarize yourself with this man­ual.
2. Disconnect or lock out the power sourcetoensurethatthe pumpwill remain inoperative.
3. Allowthe pump to completelycool 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 cau­tiously.
7. Drain the pump.
Do not operate the pump against a closeddischarge valve forlongperiods oftime.Ifoperatedagainstacloseddis­charge valve, pump components will deteriorate, and the liquid could come to a boil, build pressure, and cause the pump casing to rupture or explode.
Do not remove plates, covers, gauges, pipe plugs, or fittings from an over­heated pump. Vaporpressure within the pump can cause parts being disen ­gagedto be ejected withgreatforce.Al­low the pump to cool before servicing.
This pump is designed to handle corro­sive liquids containing specified en­trained solids,residuesand slurries. Do not attempt to pump volatile or flam­mable liquids which may damage the pumpor endanger personnel asaresult of pump failure.
This pump is designed to pump materi­als which could cause serious illness or injury through direct exposure or emitted fumes. Wear protective cloth­ing, such as rubber gloves, face mask, and rubber apron, as necessary before disassembling the pump or piping.

PAGE A -- 1SAFETY

10 SERIESOM--00589--03
Overheating may produce dangerous fumes. Use extreme caution when vent­ingthepump, orwhenremovingcovers, plates,plugs,orfittings.
Do not operate the pump without shields and/or guards in plac e over the drive shafts, belts, and/or couplings, or other rotating parts. Exposed rotating parts c an catch clothing, fingers, or tools, causing severe injury to person­nel.
Neverrunthispumpbackwards.Be cer­tain that rotation is correct before fully engaging the pump.
PAGE A -- 2
SAFETY
10 SERIES OM--00589--03
INSTALLATION --- SECTION B
Review all SAFETY information in Section A.
Since pump installations areseldom identical,this section offers only general recommendations and practices required to inspect, position, and ar­range the pump and piping.
Most of the information pertains to a standard staticliftapplicationwherethe pump ispositioned above the free level of liquid to be pumped.
If installed in a flooded suction application where the liquidis supplied to the pump under pressure, some of the information such as mounting, line configuration, and priming must be tailored to the
OUTLINE DRAWING
specific application. Since the pressure supplied to the pump is critical to performance and safety, besuretolimittheincomingpressureto50%ofthe maximum permissible operating pressure as shown on the pump performance curve (see Sec­tion E, Page 1).
Forfurther assistance,contact yourGorman-Rupp distributor or t he Gorman-Rupp Company.
Pump Dimensions
SeeFigureB---1fortheapproximatephysicaldi­mensions of this pump.
Figure B--1. Pump Model 12B22--B
PREINSTALLATION INSPECTION
Thepump assembly wasinspected and tested be­fore shipment from the factory. Before installation, inspect the pump fordamage which may have oc­curred during shipment. Check a s follows:
a. Inspect the pump forcracks,dents, damaged
threads, and other obvious damage.
b. Check for and tighten loose attaching hard-
ware. Since gaskets tend to shrink after dry­ing, check for loose hardware at mating sur­faces.

PAGE B -- 1INSTALLATION

OM--00589--03 10 SERIES
c. Carefully read all tags, decals, and markings
onthepump assembly,and perform allduties indicated. Note that the pump shaft rotates in the required direction.
Only operate this pump in the direction in­dicated by the arrow on the pump body and on the accompanying decal. Other­wise, the impeller could become loosened from the shaft and seriously damage the pump.
d. Check levels and lubricate as necessary. Re-
fer to LUBRICATION in the MAINTENANCE AND REPAIR section of this manual and per­form duties as instructed.
e. If the pump has been stored for more than 12
months, some of the components or lubri­cants may have exceeded their maximum shelf life. These must be inspected or re- placed to ensure maximum pump service.
damaged ifthe chains or cables usedtolift andmovetheunitareimproperlywrapped around the pump.
Mounting
Locatethepumpinanaccessibleplaceascloseas practicalto the liquid being pumped. Levelmount­ing is essential for proper operation.
The pump may have to be supported or shimmed to provide for level operation or to eliminate vibra­tion.
Clearance
A minimum clearance of 18 inches in front of the coverplate isrequiredto permitremovalofthe cov­er and easy access to the pump interior.
SUCTION AND DISCHARGE PIPING
Pump performance is adversely effected by in­creased suction lift, discharge elevation, and fric­tion losses. See the performance curve on Page E-1to besureyour overallapplication allowspump to operate within the safe operation range.
If the maximum shelf life has been exceeded, or if anything appears to be abnormal, contact your Gorman-Rupp distributor or the factory to deter­mine the repair or updating policy. Do not put the pump into service until appropriate action has been taken.
POSITIONING PUMP
Lifting
Useliftingequipmentwith a capacity ofatleast650 pounds (295 kg). This pump weighs approxi-
mately 125 pounds (57 kg), not including the weight of accessories, base a nd power source. Customerinstalledequipmentsuchassuctionand discharge piping must be removed before at­tempting to lift.
Thepumpassemblycanbeseriously
Materials
Either pipe or hose maybe used for suction and discharge lines; however, the materials must be compatiblewith theliquidbeingpumped.If hoseis used in suction lines, it must be the rigid-wall, rein­forced type to prevent collapse under suction. Us­ing piping couplings in suction lines is not recom­mended.
Line Configuration
Keep suction and discharge lines as straight as possible to minimize friction losses. Make mini­mum use of elbows and fittings, w hich substan­tiallyincrease frictionloss.Ifelbowsarenecessary, use the long-radius type to minimize friction loss.
Connections to Pump
Before tightening a connecting flange, align it ex­actlywith the pump port. Never pulla pipe lineinto place by tightening the flange bolts and/or cou­plings.
PAGE B -- 2 INSTALLATION
10 SERIES OM--00589--03
Lines near the pump must be independently sup­ported 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 a nd tap the suction and discharge lines not less than 18 inches (457,2 mm) from the suction and discharge ports and install the lines. Installationcloserto the pump may result in erratic readings.
SUCTION LINES
To avoid airpockets whichcouldaffect pumpprim­ing, the suction line must be as short and direct as possible.When operationinvolvesasuctionlift,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
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 1-1/4 inch (31,8 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 air­tight seal. Follow the sealant manufacturer’s rec­ommendations 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 sumpat a distance equal to1-1/2 times thediame­ter 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 suc­tioninlet because the inflowwill carry air down into the sump, and air entering the suction line w ill re­duce pump efficiency.
Suction lines shouldbe the same size as the pump inlet. If reducers are used in suction lines, they should be the eccentric type, and should be in­stalledwith the flat part ofthe reducers uppermost to avoid creating air pockets. Valves are not nor­mally used in suction lines, but if a valve is used, install it with the stem horizontal to avoid air pock­ets.
Strainers
If a strainer is furnished with the pump, be certain touseit; any sphericalsolidswhichpass 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
Ifit is necessary to position inflowclose to the suc­tioninlet,installa bafflebetween theinflowand the suctioninlet at a distance 1-1/2times 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, theflowpaths mayinteract, reducing theefficiency of one or both pumps. To avoid this, position the suction inlets s o that they are separated by a dis­tance 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---2 shows recommended minimum submergence vs.
velocity .
PAGE B -- 3INSTALLATION
OM--00589--03 10 SERIES
NOTE
The pipe submergence required may be reduced by installinga standardpipe increaser fitting at the endof thesuction line. The largeropening size will
reduce the inlet velocity. Calculate the required submergence using the following formula based on the increased opening size (area or diameter).
Figure B--2. Recommended Minimum Suction Line Submergence vs. Velocity
DISCHARGE LINES
Siphoning
Donot terminate the discharge lineat a level lower than that of the liquid being pumped unless a si­phon breaker is used in the line. Otherwise, a si­phoning action causing damage to the pump could result.
Valves
If a throttling valve is desired in the discharge line, useavalveaslargeasthelargestpipetominimize friction losses. Never install a throttling valve in a suction line.
A check valvein the discharge lineis normally rec­ommended, but it is not necessary in low dis­charge head applications.
Withhighdischargeheads,itisrecommendedthat a throttling valve and a system check valve be in­stalled in the discharge line to protect the pump from excessive shock pressure and reverse rota­tion when it is stopped.
Iftheapplicationinvolvesa highdischarge head, gradually close the discharge throttling valve before stopping the pump.
Bypass Lines
Self-primingpumps are not air compressors. Dur­ingtheprimingcycle, 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 dis­chargesideofthepumpmustbeopenedtoatmos­phericpressurethrough abypass line installedbe-
PAGE B -- 4 INSTALLATION
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