The information contained in this book is intended
to assist operating personnel by providing
information on the characteristics of the purchased
equipment.
It does not relieve the user of their responsibility of
using accepted engineering practices in the
installation, operation, and maintenance of this
equipment.
Any further questions, contact AC Fire Pump,
(847) 966-3700.
The 9100 Series Centrifugal Fire Pumps are frame
mounted pumps which feature – high efficiency,
rugged construction, compact design, foot
mounted volute and regreasable bearings. These
features, along with the horizontal split case, make
installation, operation and service easy to perform.
OPERATIONAL LIMITS
Unless special provisions have been made for
your pump by AC Fire Pump Systems, the
operational limits for 9100 Series Centrifugal Fire
Pumps are as follows:
MAXIMUM WORKING PRESSURE
Listed on pump nameplate.
SEAL OPERATING LIMITS
PACKING
PH Limitations 7-9; Temperature Range 0 to
+200°F
For use on open or closed systems which require
a large amount of makeup water, as well as
systems which are subjected to widely varying
chemical conditions and solids buildup.
PUMP IDENTIFICATION
Permanent records for this pump are referenced
by the Serial Number and it must, therefore, be
used with all correspondence to order all spare
and replacement parts. The fourth digit indicates
the specific pump on orders for more than one
pump. For example, if an order called for six
pumps, all pumps would have the same first three
sets of digits and the last digit will change to
, 03-
identify each of the six. (e.g. 03-123456-01123456-01-02
, etc.)
01
FIGURE 1 – RATING PLATE
3
SAFETY INSTRUCTIONS
SAFETY
INSTRUCTIONS
This safety alert symbol will be used in this manual
and on the pump safety instruction decals to draw
attention to safety related instructions. When used
the safety alert symbol means ATTENTION!
BECOME ALERT! YOUR SAFETY IS INVOLVED!
FAILURE TO FOLLOW THE INSTRUCTIONS
MAY RESULT IN A SAFETY HAZARD.
Your 9100 Series Centrifugal Fire Pump should
have the following safety instruction decals
displayed. If the decals are missing or illegible
contact your local AC Fire Pump Systems
representative for a replacement.
WARNING
ROTATING COMPONENTS
DISCONNECT AND LOCKOUT
POWER BEFORE SERVICING.
DO NOT OPERATE WITHOUT
ALL GUARDS IN PLACE.
CONSULT INSTALLATION
AND SERVICE INSTRUCTION
SHEET BEFORE OPERATING
OR SERVICING.
FAILURE TO FOLLOW
INSTRUCTIONS COULD
RESULT IN INJURY
OR DEATH.
Additional Safety Requirements:
1. Electrical connections to be made by
qualified Electrician in accordance with all
national, state and local codes.
2. Motor must have properly sized starter
with properly sized heaters to provide
overload and undervoltage protection.
3. If pump, motor or piping are operating at
extremely high or low temperatures,
guarding or insulation is required.
4. The maximum working pressure of the
pump is listed on the pump nameplate, do
not exceed this pressure.
RATING PLATE
WARNING
EYEBOLTS OR LIFTING
LUGS IF PROVIDED ARE
FOR LIFTING ONLY THE
COMPONENTS TO WHICH
THEY ARE ATTACHED.
FAILURE TO FOLLOW
INSTRUCTIONS COULD
RESULT IN INJURY
OR DEATH.
CAUTIONCAUTION
COUPLER ALIGNMENT IS
REQUIRED! LEVEL AND
GROUT PUMP BEFORE USE!
CHECK ALIGNMENT BEFORE
GROUTING, AFTER SYSTEM
IS FILLED, AFTER SERVICING
PUMP, AND AS REQUIRED.
CONSULT THE SERVICE
INSTRUCTIONS FOR DETAILS.
FAILURE TO FOLLOW THESE
INSTRUCTIONS COULD
RESULT IN INJURY OR
PROPERTY DAMAGE.
FIGURE 2 – SAFETY INSTRUCTION DECALS
4
DO NOT RUN PUMP DRY,
SEAL DAMAGE MAY OCCUR.
INSPECT PUMP SEAL
REGULARKY FOR LEAKS,
REPLACE AS REQUIRED.
FOR LUBRICATION
REQUIREMENTS, CONSULT
SERVICE INSTRUCTIONS.
FAILURE TO FOLLOW
INSTRUCTIONS COULD
RESULT IN INJURY OR
PROPERTY DAMAGE.
ADDITIONAL SAFETY REQUIREMENTS
ELECTRICAL SAFETY
WARNING: Electrical Shock Hazard
Electrical connections to be made by a
qualified electrician in accordance with all
applicable codes, ordinances, and good practices.
Failure to follow these instructions could result in
serious personal injury or death, and property
damage.
WARNING: Electrical Overload Hazard
Three phase motors must have properly
sized heaters to provide overload and under
voltage protection. Single-phase motors have
built-in overload protectors. Failure to follow these
instructions could result in serious personal injury
or death, and property damage.
THERMAL SAFETY
WARNING: Extreme Temperature
Hazard
If pump, motor, or piping is operating at extremely
high or low temperature, guarding or insulation is
required. Failure to follow these instructions could
result in serious personal injury or death, and
property damage.
MECHANICAL SAFETY
WARNING: Unexpected Startup Hazard
Disconnect and lockout power before
servicing. Failure to follow these instructions could
result in serious personal injury or death, and
property damage.
WARNING: Excessive System Pressure
Hazard
The maximum working pressure of the pump is
listed on the nameplate, do not exceed this
pressure. Failure to follow these instructions could
result in serious personal injury or death, and
property damage.
WARNING: Excessive Pressure Hazard
Volumetric Expansion
WARNING
The heating of water and other fluids causes
volumetric expansion. The associated forces may
cause failure of system components and release
of high temperature fluids. Installing properly sized
and located compression tanks and pressure relief
valves will prevent this. Failure to follow these
instructions could result in serious personal injury
or death, and property damage.
CAUTION
WARNING
5
PUMP LOCATION
Locate the pump so there is sufficient room for
inspection, main-tenance and service. If the use of
a hoist or tackle is needed, allow ample head
room.
WARNING: Falling Objects Hazard
Eyebolts or lifting lugs, if provided, are for
lifting only the components to which they are
attached. Failure to follow these instructions could
result in serious personal injury or death, or
property damage.
If lifting base pump is required, use a nylon string,
chain, or wire rope, hitch around both bearing
supports. If lifting of the entire pump is required,
do so with slings placed under the base rails as
shown.
CHOKER
HITCH
AROUND
BEARING
FRAME
NYLON SLING,
CHAIN OR WIRE
ROPE
Care must be taken to size equipment for
unbalanced loads which may exist if the motor is
not mounted on the base at the time of lifting.
Motor may or may not be mounted at the factory.
Pump, base, and driver assemblies where the
base length exceeds 100 inches may not be safe
to lift as a complete assembly. Damage to the
baseplate may occur. If the driver has been
mounted on the baseplate at the factory, it is safe
to lift the entire assembly. If the driver has not
been mounted at the factory, and the overall
baseplate length exceeds 100 inches, do not lift
the entire assembly consisting of pump, base, and
driver. Instead, lift the pump and baseplate to its
final location without the driver. Then mount the
driver.
The best pump location for sound and vibration
absorption is on a concrete floor with subsoil
underneath. If the pump location is overhead,
special precautions should be undertaken to
reduce possible sound transmission. Consult a
sound specialist.
FIGURE 3
If the pump is not on a closed system, it should be
placed as near as possible to the source of the
liquid supply, and located to permit installation with
the fewest number of bends or elbows in the
suction pipe.
The installation must be evaluated to determine
that the Net Positive Suction Head Available
(NPSHA) meets or exceeds the Net Positive
Suction Head Required (NPSHR), as stated by the
pump performance curve. See page 15 for more
details on proper suction piping installation.
6
INTRODUCTION
1. PURPOSE OF MANUAL
This manual is furnished to acquaint you with
some of the practical ways to install, operate,
and maintain this pump. Read it completely
before doing any work on your unit and keep
it handy for future reference.
Equipment cannot operate well without
proper care. To keep this unit at top
efficiency, follow the recommended
installation and servicing procedures outlined
in this manual.
2. WARRANTY
Refer to your local representative for warranty
coverage.
3. PUMP IDENTIFICATION
All pumps are designated by Serial Number,
Model Number, and Size. This information is
stamped on an identification plate which is
mounted on the pump.
4. INSTALLATION
5. RECEIVING PUMP
Check pump for shortages and damage
immediately upon arrival. (An absolute must.)
Prompt reporting to the carrier’s agent with
notations made on the freight bill, will
expedite satisfactory adjustment by the
carrier.
Pumps and drivers normally are shipped from
the factory mounted and painted with primer
and one finish coat. Couplings may be either
completely assembled or have the coupling
hubs mounted on the shafts and the
connecting members removed. When the
connecting members are removed, they will
be packaged in a separate container and
shipped with the pump or attached to the
base plate.
Shafts are in alignment when the unit is
shipped; however, due to shipping, the
pumps may arrive misaligned and, therefore,
alignment must be established during
installation. AC Fire Pump Systems has
determined that proper and correct alignment
can only be made by accepted erection
practices. Refer to the following paragraphs
on “Foundation,” “Base Plate Setting,”
“Grouting Procedure,” “Alignment Procedure”
and “Doweling.”
6. TEMPORARY STORAGE
If the pump is not to be installed and operated
soon after arrival, store it in a clean, dry place
having slow, moderate changes in ambient
temperature. Rotate the shaft periodically to
coat the bearings with lubricant and to retard
oxidation, corrosion, and to reduce the
possibility of false brinelling of the bearings.
7. LOCATION
The pump should be installed as near the
suction supply as possible, but no less than
five suction diameters (refer to page 15,
suction and discharge piping section) with the
shortest and most direct suction pipe
practical. The total dynamic suction lift (static
lift plus friction losses in suction line) should
not exceed the limits for which the pump was
sold.
The pump must be primed before starting.
Whenever possible, the pump should be
located below the fluid level to facilitate
priming and assure a steady flow of liquid.
This condition provides a positive suction
head on the pump. It is also possible to prime
the pump by pressurizing the suction vessel.
When installing the pump, consider its
location in relation to the system to assure
that sufficient Net Positive Suction Head
(NPSH) at pump suction is provided.
Available NPSH must always equal or exceed
the required NPSH of the pump.
The pump should be installed with sufficient
accessibility for inspection and maintenance.
A clear space with ample head room should
be allowed for the use of an overhead crane
or hoist sufficiently strong to lift the unit.
NOTE: Allow sufficient space to be able to
dismantle pump without disturbing the pump
inlet and discharge piping.
Select a dry place above the floor level
wherever possible. Take care to prevent pump
from freezing during cold weather when not in
operation. Should the possibility of freezing
exist during a shut-down period, the pump
should be completely drained, and all passages
and pockets where liquid might collect should
be blown out with compressed air.
Make sure there is a suitable power source
available for the pump driver. If motor driven,
electrical characteristics should be identical to
those shown on motor data plate.
7
8. FOUNDATION
A substantial foundation and footing should
be built to suit local conditions. The
foundation must be substantial enough to
absorb vibration. (Hydraulic Institute
Standards recommends the foundation weigh
at least five (5) times the weight of the pump
unit.) It must form a permanent and rigid
support for the baseplate. This is important in
maintaining the alignment of the flexibly
coupled unit.
ALLOW 1" FOR
SHIMS. PLACE ON
BOTH SIDES OF
ANCHOR BOLTS.
APPROX.
1" GAP
NOTE:
TO KEEP SHIMS IN
PLACE ALLOW GROUT
TO FLOW AROUND
HOLD DOWN LUGS.
GROUT ONLY TO
TOP OF BASE RAIL.
PUMP BASE
RAIL
GROUT
The foundation should be poured without
interruption to within 1/2 to 1-1/2 inches of the
finished height. The top surface of the
foundation should be well scored and
grooved before the concrete sets; this
provides a bonding surface for the grout.
Foundation bolts should be set in concrete as
shown in Figure 4. An optional 4-inch long
tube around the bolts at the top of the
concrete will allow some flexibility in bolt
alignment to match the holes in the base
plate. Allow enough bolt length for grout,
shims, lower base plate flange, nuts and
washers. The foundation should be allowed
to cure for several days before the base plate
is shimmed and grouted.
FOUNDATION
BOLT
WASHER
(OPTIONAL)
PIPE SLEEVE
BUILT-UP CONCRETE
FOUNDATION
FIGURE 4 – FOUNDATION
9. BASE PLATE SETTING (BEFORE PIPING)
NOTE: This procedure assumes that a
concrete foundation has been prepared with
anchor or hold down bolts extending up ready
to receive unit. It must be understood that
pump and motor have been mounted and
rough aligned at the factory. If motor is
to be field mounted, consult factory for
recommendations. AC Fire Pump
Systems cannot assume responsibility for
final alignment.
CONCRETE
LEVELING OF PUMP BASE
ON CONCRETE FOUNDATION.
FOUNDATION
FIGURE 5 – SETTING BASE PLATE AND
GROUTING
a. Use blocks and shims under base for
support at anchor bolts and midway
between bolts, to position base
approximately 1" above the concrete
foundation, with studs extending through
holes in the base plate.
b. By adding or removing shims under the
base, level and plumb the pump shaft and
flanges. The base plate does not have to
be level.
c. Draw anchor nuts tight against base, and
observe pump and motor shafts or
coupling hubs for alignment. (Temporarily
remove coupling guard for checking
alignment.)
d. If alignment needs improvement, add
shims or wedges at appropriate positions
under base, so that retightening of anchor
nuts will shift shafts into closer alignment.
Repeat this procedure until a reasonable
alignment is reached.
NOTE: Reasonable alignment is defined as
that which is mutually agreed upon by pump
contractor and the accepting facility (final
operator). Final alignment procedures are
covered under “Alignment Procedures.”
e. Check to make sure the piping can be
aligned to the pump flanges without
placing pipe strain on either flange.
f. Grout in base plate completely (See
“Grouting Procedure”) and allow grout to
dry thoroughly before attaching piping to
pump. (24 hours is sufficient time with
approved grouting procedure.)
8
10. GROUTING PROCEDURE
Grout compensates for uneven foundation,
distributes weight of unit, and prevents
shifting. Use an approved, non-shrinking
grout, after setting and leveling unit (See
Figure 5).
a. Build strong form around the foundation to
contain grout.
b. Soak top of concrete foundation
thoroughly, then remove surface water.
c. Base plate should be completely filled with
grout.
d. After the grout has thoroughly hardened,
check the foundation bolts and tighten if
necessary.
e. Check the alignment after the foundation
bolts are tightened.
f. Approximately 14 days after the grout has
been poured or when the grout has
thoroughly dried, apply an oil base paint to
the exposed edges of the grout to prevent
air and moisture from coming in contact
with the grout.
11. SEE ANSI/OSHA COUPLER GUARD
REMOVAL/INSTALLATION
(page 9)
12. ALIGNMENT PROCEDURE
NOTE: A flexible coupling will only
compensate for small amounts of
misalignment. Permissible misalignment will
vary with the make of coupling. Consult
coupling manufacturer’s data when in doubt.
Allowances are to be made for thermal
expansion during cold alignment, so that the
coupling will be aligned at operating
temperature. In all cases, a coupling must be
in alignment for continuous operation. Even
though the coupling may be lubricated,
misalignment causes excessive wear,
vibration, and bearing loads that result in
premature bearing failure and ultimate seizing
of the pump. Misalignment can be angular,
parallel, or a combination of these, and in the
horizontal and vertical planes. Final alignment
should be made by moving and shimming the
motor on the base plate, until the coupling
hubs are within the recommended tolerances
measured in total run-out. All measurements
should be taken with the pump and motor foot
bolts tightened. The shaft of sleeve bearing
motors should be in the center of its
mechanical float.
NOTE: Proper alignment is essential for
correct pump operation. This should be
performed after base plate has been properly
set and grout has dried thoroughly according
to instructions. Final alignment should be
made by shimming driver only. Alignment
should be made at operating temperatures.
WARNING: Unexpected Start-up Hazard
Disconnect and lock out power before
servicing. Failure to follow these instructions could
result in serious personal injury or death and
property damage.
13. ANSI/OSHA COUPLER GUARD
REMOVAL/INSTALLATION
WARNING: Unexpected Start-up Hazard
Disconnect and lock out power before
servicing. Failure to follow these instructions could
result in serious personal injury or death and
property damage.
NOTE: Do not spread the inner and outer
guards more than necessary for guard
removal or installation. Over spreading the
guards may alter their fit and appearance.
Removal
a. Remove the two capscrews that hold the
outer (motor side) coupler guard to the
support bracket(s).
b. Spread the outer guard and pull it off the
inner guard.
c. Remove the capscrew that holds the inner
guard to the support bracket.
d. Spread the inner guard and pull it over the
coupler.
Installation
a. Check coupler alignment before
proceeding. Correct if necessary.
b. Spread the inner guard and place it over
the coupler.
c. With the inner guard straddling the
support bracket, install a capscrew
through the hole (or slot) in the support
bracket and guard located closest to the
pump. Do not tighten the capscrew.
d. Spread the outer guard and place it over
the inner guard.
9
e. Install the outer guard capscrews by
following the step stated below which
pertains to your particular pump:
i. For pumps with a motor saddle support
bracket: Ensure the outer guard is
straddling the support arm, and install
but do not tighten the two remaining
capscrews.
ii. For pumps without a motor saddle
support bracket: Insert the spacer
washer between the holes located
closest to the motor in the outer guard,
ANSI/OSHA Coupling Guard Exploded View
For Typical 9100 Series Fire Pump Installation
OUTER GUARD
and install, but do not tighten, the two
remaining capscrews.
f. Position the outer guard so it is centered
around the shaft, and so there is less than
a 1/4" of the motor shaft exposed. On
guards that utilize a slotted support
bracket, the inner guard will have to be
positioned so there is only a 1/4" of the
pump shaft exposed.
g. Holding the guard in this position, tighten
the three capscrews.
INNER GUARD
ATTACH SUPPORT BRACKET
TO BEARING HOUSING
LOCATE SUPPORT ARM
BETWEEN OUTER GUARD ENDS.
ALIGN THE ARM WITH HOLES IN
THE OUTER GUARD AND HOLES
IN THE SADDLE BRACKET.
NUT
LOCKWASHER
MOTOR SADDLE
BRACKET ATTACH
TO MOTOR SADDLE
BRACKET SUPPORT
CAPSCREW
FLAT WASHER
SPACER WASHER
THIS OPTION USED IN PLACE OF SPACER WHERE
OVERALL LENGTH OF GUARD EXCEEDS 12 INCHES
OR GUARD WITH IS OVER 10 INCHES ACROSS
THE FLATS.
ATTACHES INSIDE HERE
IN LINE WITH BOLT
BRACKET
SUPPORT
SUPPORT
BRACKET
10
Method 1 – Straight Edge Alignment for
Standard Sleeve Type Coupler with Black
Rubber Insert
(See Figure 6A)
Proceed with this method only if satisfied that
face and outside diameters of the coupling
halves are square and concentric with the
coupling borers. If this condition does not
exist or elastomeric couplings do not make
this method convenient, use Method 2.
1. Check angular misalignment using a
micrometer or caliper. Measure from the
outside of one flange to the outside of the
opposite flange at four points 90° apart.
DO NOT ROTATE COUPLER.
Misalignment up to 1/64" per inch of
coupler radius is permissible.
2. At four points 90° apart (DO NOT
ROTATE COUPLER), measure the
parallel coupler misalignment by laying a
straight edge across one coupler half and
measuring the gap between the straight
edge and opposite coupler half. Up to a
1/64" gap is permissible.
STRAIGHT EDGE
DIAL
PARALLEL
INDICATOR
ALIGNMENT
INDEX LINE
RESILIENT
SEPARATOR
ANGULAR
ALIGNMENT
DIAL
INDICATOR
FIGURE 6B - CHECKING ALIGNMENT
(Method 2)
Method 2 – For Orange Hytrel Insert, 3500
RPM Operation, or All Other Coupler
Types Except as Noted Below
(See Figure 6B)
a. Make sure each hub is secured to its
respective shaft and that all connecting
and/or spacing elements are removed at
this time.
b. The gap between the coupling hubs is set
by the manufacturer before the units are
shipped. However, this dimension should
be checked. (Refer to the coupling
manufacturer’s specifications supplied
with the unit.)
FEELER GAGE
ANGULAR ALIGNMENT PARALLEL ALIGNMENT
INCORRECT ALIGNMENT
STRAIGHT EDGE
FEELER GAGE
CORRECT ALIGNMENT
FIGURE 6A – CHECKING ALIGNMENT
(Method 1)
c. Scribe index lines on coupling halves as
shown in Figure 6B.
d. Mount dial indicator on one hub as shown
for parallel alignment. Set dial to zero.
e. Turn both coupling halves so that index
lines remain matched. Observe dial
reading to see whether driver needs
adjustment (See paragraph i below).
f. Mount dial indicator on one hub as shown
for angular alignment. Set dial to zero.
g. Turn both coupling halves so that index
lines remain matched. Observe dial
reading to see whether driver needs
adjustment (See paragraph i below).
h. Assemble coupling. Tighten all bolts and
set screw(s). It may be necessary to
repeat steps c through f for a final check.
i. For single element couplings, a
satisfactory parallel misalignment is
.004"T.I.R., while a satisfactory angular
11
misalignment is .004"T.I.R. per inch of
radius R (See Figure 6B).
Grid Couplings
NOTE: The following procedure is intended
for mounting and alignment of Rexnord
Industries, LLC. and Clarke Fire Protection
Products, Inc., Tapered Grid Couplings.
Adequate lubrication is essential for
satisfactory operation. Grease supplied by
the coupling manufacturer is highly
recommended. Other greases to be used
should be approved by the coupling
manufacturer.
Alignment is shown using a spacer bar and
straight edge. Rexnord Industries, LLC. and
Clarke Fire Protection Products, Inc. state
this practice has been proven for many
industrial applications. Superior alignment
can be achieved through the use of dial
indicators as shown above.
1. Clean all metal parts using non-flammable
solvent.
2. Lightly coat seals with coupling vendor
supplied grease and place on shafts
before mounting shaft hubs.
3. Install keys and mount hubs with flange
faces flush with shaft ends or as otherwise
specified.
4. Reposition hubs on shafts as required to
achieve the required hub gap shown in
Figure 6H or otherwise specified. The
length of engagement on each shaft
should be roughly equal to the shaft
diameter.
5. Tighten setscrews.
6. Bring the pump and motor halves of the
coupler into approximate height alignment,
by placing equal amounts of shims under
all the motor feet.
7. Tighten the motor bolts.
8. Use a spacer bar equal in thickness to the
gap specified in Figure 6C. Insert bar, as
shown below, to same depth at 90°
intervals and measure clearance between
bar and hub face with feeler gauges. The
difference in minimum and maximum
measurements must not exceed the
angular installation limits shown in Figure
6H.
FIGURE 6C – USING SPACER BAR
9. Align so that a straight edge rests within
the limits shown in Figure 6D on both
hubs as shown below and also at 90°
intervals without rotating the coupling.
Check with feelers. The clearance must
not exceed the PARALLEL OFFSET
installation limits specified in Figure 6H.
FIGURE 6D – USING STRAIGHT EDGE
10. If adjustment is needed, loosen the motor
bolts and add (or remove) an equal
amount of shims under each motor foot to
align the height. To correct side
misalignment, strike the side of the motor
foot with a mallet.
11. Tighten the motor bolts and check again.
If a correction is made, re-check alignment
in all
directions. Repeat this process until
the desired result is obtained.
12. Pack gap and grooves with coupling
vendor supplied grease before inserting
grid. When grids are furnished in two or
more segments, install them so that all cut
ends extend in the same direction as
shown below. This will ensure correct grid
contact with non-rotating pin in cover
halves.
13. Spread the grid slightly to pass over the
coupling teeth and seat with a soft mallet.
12
FIGURE 6E – SEATING THE GRID
14. Pack the spaces between and around the
grid with as much as coupling vendor
supplied grease as possible and wipe off
excess flush with the top of the grid.
15. Position seals on hubs to line-up with
grooves in cover. Position gaskets on
flange of lower cover half and assemble
covers so that the match marks are on the
same side.
16. If the shafts are not horizontal, or coupling
is to be used vertically, assemble cover
halves with the lug and match mark UP or
on the high side. Push gaskets in until
they stop against the seals and secure
cover halves with fasteners, tightening to
torque specified in Figure 6H. Ensure
gaskets stay in position during fastener
tightening.
FIGURE 6G – COVER INSTALLATION,
VERTICAL POSITION
17. Ensure the lube plugs are installed in the
cover.
FIGURE 6F – COVER INSTALLATION
WARNING: Coupling Failure
Do not operate coupling without proper lubrication
Failure to follow these instructions could result in
serious personal injury or death and property
damage.
Final alignment cannot be accomplished until
the pump has been operated initially for a
sufficient length of time to attain operating
temperature. When normal operating
temperature has been attained, secure the
pump to re-check alignment and compensate
for temperature accordingly. See Alignment
Section.
WARNING: Rotating Components
Hazard
Do not operate pump without all guards in place.
Failure to follow these instructions could result in
serious personal injury or death and property
damage.
WARNING: Coupling Failure
Do not operate pump with coupling out of
alignment. Ensure final coupling alignment is
within the values stated above or according to the
coupling manufacturer’s instructions. Coupling,
pump, or driver failure may occur.
Failure to follow these instructions could result in
serious personal injury or death and property
damage.
OPTIONAL Alignment Procedure
If desired, the pump and motor feet can be
doweled to the base after final alignment is
complete. This should not be done until the
unit has been run for a sufficient length of
time and alignment is within the tolerance.
See Doweling Section.
CAUTION: Extreme Temperature and/or
Flying Debris Hazard
Eye protection and gloves required. Failure to
follow these instructions could result in property
damage and/or moderate personal injury.
14
NOTE: Pump may have been doweled to
base at factory.
14. DOWELING
Dowel the pump and driving unit as follows:
a. Drill holes through diagonally opposite feet
and into the base. Holes must be of a
diameter 1/64 inch less than the diameter
of the dowel pins. Clean out the chips.
b. Ream the holes in feet and base to the
proper diameter for the pins (light push fit).
Clean out the chips.
c. Insert pins to be approximately flush with
feet.
15. SUCTION AND DISCHARGE PIPING
General
When installing the pump piping, be sure to
observe the following precautions:
Piping should always be run to the pump.
Do not move pump to pipe. This could make
final alignment impossible.
Both the suction and discharge piping should
be supported independently near the pump
and properly aligned, so that no strain is
transmitted to the pump when the flange bolts
are tightened. Use pipe hangers or other
supports at necessary intervals to provide
support. When expansion joints are used in
the piping system, they must be installed
beyond the piping supports closest to the
pump. Tie bolts should be used with
expansion joints to prevent pipe strain. Do not
install expansion joints next to the pump or in
any way that would cause a strain on the
pump resulting from system pressure
changes. It is usually advisable to increase
the size of both suction and discharge pipes
at the pump connections to decrease the loss
of head from friction.
Provide for pipe expansion when hot fluids
are to be pumped.
Install piping as straight as possible, avoiding
unnecessary bends. Where necessary, use
45-degree or long sweep 90-degree fitting to
decrease friction losses.
Make sure that all piping joints are air-tight.
Where flanged joints are used, assure that
inside diameters match properly.
Remove burrs and sharp edges when making
up joints.
Do not “spring” piping when making any
connections.
15
Suction Piping
When installing the suction piping, observe
the following precautions (See Figure 7).
The sizing and installation of the suction
piping is extremely important. It must be
selected and installed so that pressure losses
are minimized and sufficient liquid will flow
into the pump when started and operated.
Many NPSH (Net Positive Suction Head)
problems can be attributed directly to
improper suction piping systems.
Friction losses caused by undersized suction
piping can increase the fluid’s velocity into the
pump. As recommended by the Hydraulic
Institute Standard ANSI/HI 1.1-1.5-1994,
suction pipe velocity should not exceed the
velocity in the pump suction nozzle. In some
situations pipe velocity may need to be
further reduced to satisfy pump NPSH
requirements and to control suction line
losses. Pipe friction can be reduced by using
pipes that are one to two sizes larger than the
pump suction nozzle in order to maintain pipe
velocities less than 5 feet/second.
SUCTION PIPE INSTALLED WITH A
GRADUAL RISE TO PUMP
LEVEL
CENTER LINE
OF PIPE
AIR POCKET
CORRECT
INCORRECT
AIR POCKET
INCORRECT
INCORRECT
CHECK VALVE
GATE VALVE
INCREASER
AIR POCKET
Suction piping should be short in length, as
direct as possible, and never smaller in
diameter than the pump suction opening. If
the suction pipe is short, the pipe diameter
can be the same size as the suction opening.
If longer suction pipe is required, pipes
should be one or two sizes larger than the
opening depending on piping length.
Suction piping for horizontal double suction
pumps should not be installed with an elbow
close to the suction flange of the pump
except when the suction elbow is in the
vertical plane. A suction pipe of the same size
as the suction nozzle approaching at any
angle other than straight up or straight down
must have the elbow located 10 pipe
diameters from the suction flange of the
pump. Vertical mounted pumps and other
space limitations require special piping.
GRADUAL RISE
TO PUMP
NO AIR
POCKETS
PATH OF WATER
NO AIR
POCKETS
CORRECT
GRADUAL RISE
TO PUMP
ECCENTRIC
REDUCER
CORRECT
DISTANCE PLUS
ECCENTRIC REDUCER
STRAIGNTENS FLOW
CORRECT
INCORRECT
FIGURE 7 – SUCTION PIPE INSTALLATIONS
(PIPING SUPPORTS NOT SHOWN)
16
There is always an uneven turbulent flow
around an elbow and when it is in a position
other than the vertical it causes more liquid to
enter one side of the impeller than the other
(See Figure 8). This results in high
unequalized thrust loads that will overheat the
bearings and cause rapid wear in addition to
affecting hydraulic performance.
WATER PRESSURE
INCREASES HERE CAUSING
A GREATER FLOW TO ONE
SIDE OF THE IMPELLER
SUCTION
ELBOW
PUMP CASING
PUMP SUCTION
FLANGE
CASING RINGS
IMPELLER
FIGURE 8 - UNBALANCED LOADING OF A
DOUBLE SUCTION IMPELLER DUE TO
UNEVEN FLOW AROUND ON ELBOW
ADJACENT TO THE PUMP.
When operating on a suction lift, the suction
pipe should slope upward to the pump
nozzle. A horizontal suction line must have a
gradual rise to the pump. Any high point in
the pipe will become filled with air and thus
prevent proper operation on the pump. When
reducing the piping to the suction opening
diameter use an eccentric reducer with the
eccentric side down to avoid air pockets.
NOTE: When operating on suction lift never
use a straight taper reducer in a horizontal
suction line, as it tends to form an air pocket
in the top of the reducer and the pipe.
To facilitate cleaning pump liquid passage
without dismantling pump, a short section of
pipe (Dutchman or spool piece) so designed
that it can be readily dropped out of the line
can be installed adjacent to the suction
flange. With this arrangement, any matter
clogging the impeller is accessible by
removing the nozzle (or pipe section).
Valves in Suction Piping
When installing valves in the suction piping,
observe the following precautions:
a. If the pump is operating under static
suction lift conditions, a foot valve may be
installed in the suction line to avoid the
necessity of priming each time the pump
is started. This valve should be of the
flapper type, rather than the multiple
spring type, sized to avoid excessive
friction in the suction line. (Under all other
conditions, a check valve, if used, should
be installed in the discharge line.) (See
“Valves in Discharge Piping” below.)
b. When foot valves are used, or where there
are other possibilities of “water hammer,”
close the discharge valve slowly before
shutting down the pump.
c. Where two or more pumps are connected
to the same suction line, install gate
valves so that any pump can be isolated
from the line. Gate valves should be
installed on the suction side of all pumps
with a positive pressure for maintenance
purposes. Install gate valves with stems
horizontal to avoid air pockets. Globe
valves should not be used, particularly
where NPSH is critical.
d. The pump must never be throttled by the
use of a valve on the suction side of the
pump. Suction valves should be used only
to isolate the pump or maintenance
purposes, and should always be installed
in positions to avoid air pockets.
e. A pump drain valve should be installed in
the suction piping between the isolation
valve and the pump.
Discharge Piping
If the discharge piping is short, the pipe
diameter can be the same as the discharge
opening. If the piping is long, pipe diameter
should be one or two sizes larger than the
discharge opening. On long horizontal runs, it
is desirable to maintain as even a grade as
possible. Avoid high spots, such as loops,
which will collect air and throttle the system or
lead to erratic pumping.
Valves in Discharge Piping
A triple duty valve should be installed in the
discharge. The triple duty valve placed on the
pump protects the pump from excessive back
pressure, and prevents liquid from running
back through the pump in case of power
failure.
Pressure Gauges
Properly sized pressure gauges should be
installed in both the suction and discharge
nozzles in the gauge taps (which are
provided on request). The gauges will enable
the operator to easily observe the operation
of the pump, and also determine if the pump
17
is operating in conformance with the
performance curve. If cavitation, vapor
binding, or other unstable operation should
occur, widely fluctuating discharge pressure
will be noted.
Pump Insulation
On chilled water applications most pumps are
insulated. As part of this practice, the pump
bearing housings should not be insulated
since this would tend to “trap” heat inside the
housing. This could lead to increased bearing
temperatures and premature bearing failures.
16. STUFFING BOX LUBRICATION
Contaminants in the pumped liquid must not
enter the stuffing box. These contaminants
may cause severe abrasion or corrosion of
the shaft, or shaft sleeve, and rapid packing
or mechanical seal deterioration; they can
even plug the stuffing box flushing and
lubrication system. The stuffing box must be
supplied at all times with a source of clean,
clear liquid to flush and lubricate the packing
or seal. It is important to establish the
optimum flushing pressure that will keep
contaminants from the stuffing box cavity. If
this pressure is too low, fluid being pumped
may enter the stuffing box. If the pressure is
too high, excessive packing or seal wear may
result; and extreme heat may develop in the
shaft causing higher bearing temperatures.
The most desirable condition, therefore, is to
use a seal water pressure 15-20 psig above
the maximum stuffing box pressure.
17. PACKING
Standard pumps are normally packed before
shipment. If the pump is installed within 60
days after shipment, the packing will be in
good condition with a sufficient supply of
lubrication. If the pump is stored for a longer
period, it may be necessary to repack the
stuffing box. In all cases, however, inspect
the packing before the pump is started.
NOTE: Packing adjustment is covered in the
Maintenance section of this manual.
On some applications, it is possible to use
internal liquid lubrication (pumped liquid) to
lubricate packing. Only when all of the
following conditions prevail, can this be done:
1. Liquid is clean, free from sediment and
chemical precipitation and is compatible
with seal materials.
2. Temperature is above 32°F and below
160°F.
3. Suction pressure is below 75 psig.
4. Lubrication (pumped liquid) has lubricating
qualities.
5. Liquid is non-toxic and non-volatile.
When the liquid being pumped contains
solids or is otherwise not compatible with
packing materials, an outside supply of seal
liquid should be furnished. In general,
external-injection liquid (from an outside
source) is required when any of the above
conditions cannot be met.
The standard stuffing box consists of rings of
packing (see assembly section for number of
rings), a seal cage (optional), and a gland. A
shaft sleeve which extends through the box
and under the gland is normally provided to
protect the shaft.
A tapped hole is supplied in the stuffing box
directly over the seal cage to introduce a
clean, clear sealing medium. The stuffing box
must, at all times, be supplied with sealing
liquid at a high enough pressure to keep the
box free from foreign matter, which would
quickly destroy the packing and score the
shaft sleeve.
Only a sufficient volume of sealing liquid to
create a definite direction of flow from the
stuffing box inward to the pump casing is
required, but the pressure is important. Apply
seal water at a rate of approximately .25
GPM at a pressure approximately 15 to 20
psig above the suction pressure.
(Approximately one (1) drop per second.)
One recommended method to minimize error
in regulating flushing water is a “Controlled
Pressure System” (Figure 9). It is important to
set the pressure reducing valve adjusted to a
value slightly exceeding the maximum
stuffing box operating pressure (assuming it
is reasonably constant). A flow indicating
device will detect a failing of the bottom
packing rings allowing leakage in the pump.
External sealing liquid should be adjusted to
the point where the packing runs only slightly
warm, with a very slow drip from the stuffing
box. Excess pressure from an external
source can be very destructive to packing.
More pressure is required, however, for
abrasive slurries than for clear liquids.
Examination of the leakage will indicate
whether to increase or decrease external
18
pressure. If slurry is present in the leakage,
increase the pressure until only clear liquid
drips from the box. If the drippage is corrosive
or harmful to personnel, it should be collected
and piped away.
A common error is to open the external piping
valve wide and then control the drippage by
tightening the packing gland. A combination
of both adjustments is essential to arrive at
the optimum condition. The life of packing
and sleeve depends on careful control more
than any other factor.
FLOWMETER
PRESSURE
GAUGE
STUFFING BOX
PRESSURE
REDUCING
VALVE
FIGURE 9 – CONTROLLED PRESSURE
SYSTEM
19
OPERATION
WARNING: Unexpected Startup Hazard
Disconnect and lockout power before
servicing. Failure to follow these instructions could
result in serious personal injury or death, or
property damage.
WARNING: Electrical Shock Hazard
Electrical connections to be made by a
qualified electrician in accordance with all
applicable codes, ordinances, and good practices.
Failure to follow these instructions could result in
serious personal injury or death, or property
damage.
1. PRE-START CHECKS
Before initial start of the pump, make the
following inspections:
a. Check alignment between pump and
motor.
b. Check all connections to motor and
starting device with wiring diagram. Check
voltage, phase, and frequency on motor
nameplate with line circuit.
c. Check suction and discharge piping and
pressure gauges for proper operation.
d. Check impeller adjustment, see specific
section for proper adjustment.
WARNING: Rotating Components
Hazard
Do not operate pump without all guards in place.
Failure to follow these instructions could result in
serious personal injury or death and property
damage.
CAUTION: Seal Damage Hazard
Do not run pump dry, seal damage may
occur. Failure to follow these instructions could
result in property damage and/or moderate
personal injury.
2. PRIMING
If the pump is installed with a positive head
on the suction, it can be primed by opening
the suction and vent valve and allowing the
liquid to enter the casing.
If the pump is installed with a suction lift,
priming must be done by other methods such
as foot valves, ejectors, or by manually filling
the casing and suction line.
WARNING: Rotating Components
Hazard
Do not operate pump without all guards in place.
Failure to follow these instructions could result in
serious personal injury or death and property
damage.
e. Turn rotating element by hand to assure
that it rotates freely.
f. Check driver lubrication.
g. Assure that pump bearings are properly
lubricated.
h. Assure that coupling is properly lubricated,
if required.
i. Assure that pump is full of liquid (See 2.
Priming) and all valves are properly set
and operational, with the discharge valve
closed, and the suction valve open.
j. Check rotation. Be sure that the drive
operates in the direction indicated by the
arrow on the pump casing as serious
damage can result if the pump is operated
with incorrect rotation. Check rotation
each time the motor leads have been
disconnected.
3. STARTING
a. Close drain valves and valve in discharge
line.
b. Open fully all valves in the suction line.
c. Prime the pump.
NOTE: If the pump does not prime properly,
or loses prime during start-up, it should be
shutdown and the condition corrected before
the procedure is repeated.
d. When the pump is operating at full speed,
open the discharge valve slowly. This
should be done promptly after start-up to
prevent damage to pump by operating at
zero flow.
4. OPERATING CHECKS
a. Check the pump and piping to assure that
there are no leaks.
b. Check and record pressure gauge
readings for future reference.
20
c. Check and record voltage, amperage per
phase, and kw if an indicating wattmeter is
available.
d. Check bearings for lubrication and
temperature. Normal temperature is 180°
maximum.
e. Make all pump output adjustments with
the discharge line.
CAUTION: Cavitation Damage Hazard
Do not throttle the suction line to adjust the
pump output. Failure to follow these instructions
could result in property damage and/or moderate
personal injury.
5. FREEZING PROTECTION
Pumps that are shut down during freezing
conditions should be protected by one of the
following methods.
a. Drain the pump; remove all liquids from
the casing.
b. Keep fluid moving in the pump and
insulate or heat the pump to prevent
freezing.
CAUTION: Bearing/Seal Damage Hazard
Do not let heated pump temperature rise
above 150°F. Failure to follow these instructions
could result in property damage and/or moderate
personal injury.
21
CHANGING ROTATION
9100 Series Centrifugal Fire Pumps can be
operated clockwise or counter-clockwise when
viewed from the coupling end of the pump. If you
wish to reverse the suction and discharge nozzles,
this can be accomplished with the same pump as
follows:
IMPORTANT: Refer to the disassembly and
assembly procedures section of this manual for
proper disassembly and assembly techniques:
1. Remove the impeller from the shaft, turn it
180° and replace it on the shaft. (Follow the
disassembly procedures given in this manual.)
2. With the rotating element out of the
casing, remove the casing from the
bedplate and turn 180°.
3. Set the rotating element back in the
casing and reassemble the pump.
NOTE: The impeller and casing are in the same
relationship to each other as they were originally.
The shaft and motor are also in the same
relationship to each other as they were originally.
4. Reassemble pump and realign the
coupling as called for in the alignment
instructions.
WARNING: Rotating Components Hazard
Do not operate pump without all guards in
place. Failure to follow these instructions could result
in serious personal injury or death and property
damage.
5. The rotation of the motor must be changed
by switching the motor leads.
NOTE: Unless the motor rotation is reversed, the
impeller will run backward.
DISCHARGE
CW
ROTATION
CLOCKWISE ROTATION VIEWED
FROM THE COUPLING END
SUCTION
COUNTER-CLOCKWISE ROTATION
VIEWED FROM THE COUPLING END
CCW
ROTATION
FIGURE 10 - CORRECT RELATIONSHIP OF IMPELLER AND CASING
DISCHARGE
FIGURE 11 - MAIN JOINT BOLTS
22
TROUBLE SHOOTING
Between regular maintenance inspections, be alert for signs of motor or pump trouble. Common symptoms
are listed below. Correct any trouble immediately and AVOID COSTLY REPAIR AND SHUTDOWN.
CAUSESCURES
No Liquid Delivered
1. Lack of prime. Fill pump and suction pipe completely with liquid.
2. Loss of prime. Check for leaks in suction pipe joints and fittings; vent casing to remove
accumulated air.
3. Suction lift too high. If no obstruction at inlet, check for pipe friction losses. However, static lift
may be too great. Measure with mercury column or vacuum gauge while
pump operates. If static lift is too high, liquid to be pumped must be
raised or pump lowered.
4. Discharge head too high. Check pipe friction losses. Large piping may correct condition. Check
that valves are wide open.
5. Speed too low. Check whether motor is directly across-the-line and receiving full
voltage. Or frequency may be too low; motor may have an open phase.
6. Wrong direction of rotation. Check motor rotation with directional arrow on pump casing.
7. Impeller completely plugged. Dismantle pump and clean impeller.
Not Enough Liquid Delivered
8. Air leaks in suction piping. If liquid pumped is water or other non-explosive, and explosive gas or
dust is not present, test flanges for leakage with flame or match, or by
plugging inlet and putting line under pressure. A gauge will indicate a
leak with a drop of pressure.
9. Speed too low. See item 5.
10. Discharge head too high. See item 4.
11. Suction lift too high. See item 3.
12. Impeller partially plugged. See item 7.
13. Cavitation; insufficient NPSH
a. Increase positive suction head on pump by lowering pump.
(depending on installation)
b. Sub-cool suction piping at inlet to lower entering liquid temperature.
c. Pressurization suction vessel.
14. Defective impeller. Inspect impeller, bearings and shaft. Replace if damaged or vane
sections badly eroded.
15. Foot valve too small or partially
obstructed
Area through ports of valve should be at least as large as area of suction
pipe – preferably 1-1/2 times. If strainer is used, net clear area should be
3 to 4 times area of suction pipe.
16. Suction inlet not immersed
deep enough
If inlet cannot be lowered, or if eddies through which air is sucked persist
when it is lowered, chain a board to suction pipe. It will be drawn into
eddies, smothering the vortex.
17. Wrong direction of rotation. Symptoms are an overloaded drive and about 1/3 rated capacity from
pump. Compare rotation of motor with directional arrow on pump casing.
18. Too small impeller diameter.
(Probable cause if none of
above.)
Check with factory to see if a larger impeller can be used; otherwise, cut
pipe losses or increase speed – or both, as needed. But be careful not
to seriously overload drive.
19. Speed too low. See item 5.
20. Air leaks in suction piping. See item 8.
23
CAUSESCURES
Not Enough Pressure
21. Mechanical defects. See item 14 and 15.
22. Obstruction in liquid passages. Dismantle pump and inspect passages of impeller and casing. Remove
obstruction.
23. Air or gases in liquid. (Test in
laboratory, reducing pressure
on liquid to pressure in suction
line. Watch for bubble
May be possible to over rate pump to point where it will provide
adequate pressure despite condition. Better to provide gas separation
chamber on suction line near pump, and periodically exhaust
accumulated gas. See item 13.
formation.)
24. Too small impeller diameter.
See item 18.
(Probable cause if none above.)
Pump Operates For Short Time, Then Stops
25. Incomplete priming. Free pump, piping and valves of all air. If high points in suction line
prevent this, they need correcting. See page 20.
26. Suction lift too high. See item 3.
27. Air leaks in suction piping. See item 8.
28. Air or gases in liquid. See item 23.
Pump Takes Too Much Power
29. Head lower than rating; thereby
Machine impeller’s OD to size advised by factory.
pumping too much liquid.
30. Cavitation See item 13.
31. Mechanical defects. See items 14 and 15.
32. Suction inlet not immersed
See item 16.
enough.
33. Liquid heavier (in either
viscosity or specific gravity)
Use larger driver. Consult factory for recommended size. Test liquid for
viscosity and specific gravity.
than allowed for.
34. Wrong direction of rotation. See item 6.
35. Casing distorted by excessive
strains from suction or
Check alignment. Examine pump for friction between impeller and
casing. Replace damaged parts.
discharge piping.
36. Shaft bent due to damage –
through shipment, operation, or
overhaul.
37. Mechanical failure of critical
pump parts.
Check deflection of rotor by turning on bearing journals. Total indicator
run-out should not exceed 0.002 on shaft and 0.004 inch on impeller
wearing surface.
Check bearings and impeller for damage. Any irregularity in these parts
will cause a drag on shaft.
38. Misalignment. Realign pump and driver.
39. Speed may be too high (brake
Check voltage on motor.
hp of pump varies as the cube
of the speed; therefore, any
increase in speed means
considerable increase in power
demand).
40. Electrical defects. The voltage and frequency of the electrical current may be lower than
that for which the motor was built; or there may be defects in motor.
The motor may not be ventilated properly due to a poor location.
41. Mechanical defects in turbine,
If trouble cannot be located, consult factory.
engine or other type of drive
exclusive of motor.
24
MAINTENANCE
1. GENERAL MAINTENANCE
Operating conditions vary so widely that to
recommend one schedule of preventative
maintenance for all centrifugal pumps is not
possible. Yet some sort of regular inspection
must be planned and followed. We suggest a
permanent record be kept of the periodic
inspections and maintenance performed on
your pump. This recognition of maintenance
procedure will keep your pump in good
working condition, and prevent costly
breakdown.
One of the best rules to follow in the proper
maintenance of your centrifugal pump is to
keep a record of actual operating hours.
Then, after a predetermined period of
operation has elapsed, the pump should be
given a thorough inspection. The length of
this operating period will vary with different
applications, and can only be determined
from experience. New equipment, however,
should be examined after a relatively short
period of operation. The next inspection
period can be lengthened somewhat. This
system can be followed until a maximum
period of operation is reached which should
be considered the operating schedule
between inspections.
2. MAINTENANCE OF PUMP DUE TO FLOOD
DAMAGE
The servicing of centrifugal pumps after a
flooded condition is a comparatively simple
matter under normal conditions.
Bearings are a primary concern on pumping
units. First, dismantle the bearings; clean and
inspect them for any rusted or badly worn
surfaces. If bearings are free from rust and
wear, reassemble and relubricate them with
one of the recommended pump lubricants.
Depending on the length of time the pump
has remained in the flooded area, it is unlikely
that bearing replacement is necessary;
however, in the event that rust or worn
surfaces appear, it may be necessary to
replace the bearings.
Next, inspect the stuffing box, and clean out
any foreign matter that might clog the box.
Mechanical seals should be cleaned and
thoroughly flushed.
Any pump that is properly sealed at all joints
and connected to both the suction and
discharge should exclude outside liquid.
Therefore, it should not be necessary to go
beyond the bearings, stuffing box, and
coupling when servicing the pump.
3. BEARING LUBRICATION – GREASE
Grease lubricated ball bearings are packed
with grease at the factory and ordinarily will
require no attention before starting, provided
the pump has been stored in a clean, dry
place prior to its first operation. The bearings
should be watched the first hour or so after
the pump has been started to see that they
are operating properly.
The importance of proper lubrication cannot
be over emphasized. It is difficult to say how
often a bearing should be greased, since that
depends on the conditions of operation. It is
well to add one ounce of grease at regular
intervals, but it is equally important to avoid
adding too much grease. For average
operating conditions, it is recommended that
1 oz. of grease be added at intervals of three
to six months, and only clean grease be
used. It is always best if unit can be stopped
while grease is added to avoid overloading.
NOTE: Excess grease is the most common
cause of over-heating.
A lithium based NLGI-2 grade grease should
be used for lubricating bearings where the
ambient temperature is above -20°F. Grease
lubricated bearings are packed at the factory
with Shell Alvania No 2. Other recommended
greases are Texaco Multifak No. 2 and
Mobilux No. 2 grease.
Greases made from animal or vegetable oils
are not recommended due to the danger of
deterioration and forming of acid. Do not use
graphite. Use of an ISO VG 100 mineral base
oil with rust and oxidation inhabitors is
recommended.
The maximum desirable operating
temperature for ball bearings is 180°F.
Should the temperature of the bearing frame
rise above 180°F, the pump should be shut
down to determine the cause.
Couplings should be dismantled and
thoroughly cleaned.
25
4. PACKING SEAL
When a pump with packing is first started it is
advisable to have the packing slightly loose
without causing an air leak. As the pump runs
in, gradually tighten the gland bolts evenly.
The gland should never be drawn to the point
where packing is compressed too tightly and
no leakage occurs. This will cause the
packing to burn, score the shaft sleeve and
prevent liquid from circulating through the
stuffing box cooling the package.
NOTE: Eccentric run-out of the shaft or
sleeve through the packing could result in
excessive leakage that cannot be
compensated for. Correction of this defect
requires shaft and/or sleeve replacement.
Packing should be checked frequently and
replaced as service indicates. Six months
might be a reasonable expected life,
depending on the operating conditions.
5. CLEANING WITHOUT DISMANTLING PUMP
A short section of pipe so designed that it can
be readily dropped out of the line can be
installed adjacent to the suction flange. With
this arrangement, any matter clogging the
impeller is accessible by removing the pipe
section.
If the pump cannot be freed of clogging after
the above methods have been tried,
dismantle the unit as previously described to
locate the trouble.
26
MAINTENANCE TIME TABLE
EVERY MONTH
EVERY 3
MONTHS
EVERY 6
MONTHS
EVERY YEAR
Check bearing temperature with a thermometer, not by hand
running hot (over 180°F), it may be the result of too much lubricant. If changing the
lubricant does not correct the condition, disassembly and inspect the bearings. Lip
seals bearing on the shaft may also cause the housing to run hot. Lubricate lip
seals to correct.
Check the oil on oil lubricated units. Check grease lubricated bearings for
saponification. This condition is usually caused by the infiltration of water or other
fluid past the bearing shaft seals and can be noticed immediately upon inspection,
since it gives the grease a whitish color. Wash out the bearings with a clean
industrial solvent and replace the grease with the proper type as recommended.
Check the packing and replace if necessary. Use the grade recommended. Be
sure the lantern rings are centered in the stuffing box at the entrance of the stuffing
box piping connection.
Take vibration readings on the bearing housings. Compare the readings with the
last set of readings to check for possible pump component failure (e.g. bearings)
Check shaft or shaft sleeve for scoring. Scoring accelerates packing wear.
Check alignment of pump and motor. Shim up units if necessary. If misalignment
reoccurs frequently, inspect the entire piping system. Unbolt piping at suction and
discharge flanges to see if it springs away, thereby indicating strain on the casing.
Inspect all piping supports for soundness and effective support of load. Correct as
necessary.
Remove the upper half of the casing. Inspect the pump thoroughly for wear, and
order replacement parts if necessary.
. If bearings are
Check wear ring clearances. Replace when clearances become three (3) times
their normal clearance or when a significant decrease in discharge pressure for the
same flow rate is observed. See Engineering Data Section for standard
clearances.
Remove any deposit or scaling. Clean out stuffing box piping.
Measure total dynamic suction and discharge head as a test of pump performance
and pipe condition. Record the figures and compare them with the figures of the
last test. This is important, especially where the fluid being pumped tends to form a
deposit on internal surfaces. Inspect foot valves and check valves, especially the
check valve which safeguards against water hammer when the pump stops. A
faulty foot or check valve will reflect also in poor performance of the pump while in
operation.
NOTE: The above time table is based on the assumption that after start-up, the unit had been constantly
monitored and such a schedule was found to be consistent with operation, as shown by stable readings.
Extreme or unusual applications or conditions should be taken into consideration when establishing the
maintenance intervals.
27
SERVICE INSTRUCTIONS
DISASSEMBLY AND REASSEMBLY
PROCEDURES
The procedures outlined in this section cover
the dismantling and reassembly of the 9100
Series Centrifugal Fire Pumps.
When working on the pump, use accepted
mechanical practices to avoid unnecessary
damage to parts. Check clearances and
conditions of parts when pump is dismantled
and replace if necessary. Steps should
usually be taken to restore impeller and
casing ring clearance when it exceeds three
times the original clearance.
DISMANTLING (PUMP WITH PACKING)
WARNING: Unexpected Startup Hazard
Disconnect and lockout power before
servicing. Failure to follow these instructions could
result in serious personal injury or death, or
property damage.
WARNING: Electrical Shock Hazard
Electrical connections to be made by a
qualified electrician in accordance with all
applicable codes, ordinances, and good practices.
Failure to follow these instructions could result in
serious personal injury or death, or property
damage.
WARNING:
Prior to working on pump the power source
should be disconnected with lockout provisions so
power cannot be re-energized to the motor. Close
isolating suction and discharge valves. Failure to
follow these instructions could result in property
damage, severe personal injury, or death.
“A”
LUBRICATION FOR PACKING
Pump Size Dimension A
FIGURE 12 - ASSEMBLY SECTION: PUMP WITH PACKING
28
TABLE “A”
Qty.
CAUTION: Extreme Temperature Hazard
Allow pump temperatures to reach
acceptable levels before proceeding. Open drain
valve, do not proceed until liquid stops coming out
of drain valve. If liquid does not stop flowing from
drain valve, isolation valves are not sealing and
should be repaired before proceeding. After liquid
stops flowing from drain valve, leave valve open
and continue. Remove the drain plug located on
the bottom of the pump housing. Do not reinstall
plug or close drain valve until reassembly is
completed. Failure to follow these instructions
could result in property damage and/or moderate
personal injury.
10. Pull coupling half and key (3-911-2) off
shaft (3-007-0).
NOTE: A spare rotating element can be
installed at this point.
11. Remove cap screws (3-904-9) from
bearing covers (3-01803, -4).
12. Remove bearing housings (3-025-2),
locknut (3-516-4), and lockwasher (3-517-
4). Mount bearing puller and remove
bearings (3-026-2). Remove thrust washer
(3-078-9) and snap ring (3-915-9).
NOTE: Locknut, lockwasher, and thrust
washer are not used on inboard bearing.
(See Appendix “A” for exploded view.)
1. Close valves on suction and discharge
sides of pump. If no valves have been
installed, it will be necessary to drain the
system.
2. Remove the coupler guard. Refer to
section titled “Hex Coupler Guard
Removal/Installation.”
3. Loosen the capscrews which secure the
coupler flanges to the coupler hubs.
Remove the coupler flanges and sleeve
by compressing the flanges and pulling
out from beneath the hubs back on the
shafts. Remove the coupler hub from the
pump shaft.
4. Drain the pump by opening vent plug (0910-0) and remove drain plugs (0-910-0)
on suction and discharge nozzle.
5. Remove seal line (0-910-0, 0-950-0, 0952-0), if supplied.
6. Remove gland bolts (3-904-9), washers
(1-909-9) and slide gland (3-014-2) away
from casing.
7. Remove all casing main joint cap screws
(2-904-1) and dowels (2-916-9). Use slot
in casing main joint and separate the
casing halves with a pry bar. Lift upper
half casing (2-001-7) by cast lugs.
8. Remove packing (1-924-9) and seal cage
(1-013-2) from each stuffing box.
9. Remove cap screws (1-904-9) which hold
bearing housings (3-025-2) to the casing
and lift rotating element out of lower
casing (2-001-08). Rotating element may
now be moved to a suitable working
location.
13. Remove bearing covers (3-018-3, -4) and
push bearing isolators (1-333-1) out of
bearing covers and coupling end bearing
housing (1-332-1, 1-333-1).
CAUTION:
DO NOT REUSE THE BALL BEARINGS.
FIGURE 13 - COMPLETE ROTATING ELEMENT
LESS PACKING AND GLAND
14. Remove casing rings (3-003-9) from
impeller (4-002-0).
15. Remove set screw (3-902-9) from shaft
nuts. Remove shaft nuts (3-015-9), Orings (3-914-9), sleeves (3-009-9) sleeve
gaskets (1-428-1) and impeller (4-002-0).
NOTE: Apply heat uniformly to the shaft
sleeve to loosen the sealant between the
shaft and sleeve. DO NOT HEAT ABOVE
275ºF. To further assist in removing the
sleeves, hold the shaft vertically and drop it
on a block of wood. The impeller weight
should force both the impeller and sleeve
from the shaft.
29
ASSEMBLY (PUMP WITH PACKING)
All bearings, O-rings, bearing isolators,
gaskets, impeller rings, and casing wear rings
should be replaced with new parts during
assembly. All reusable parts should be
cleaned of all foreign matter before
reassembling. The main casing joint gasket
can be made using the upper or lower half as
a template. Lay the gasket material on the
casing joint and mark it by pressing it against
the edges of the casing. Trim the gasket, so
that it is flush with the inside edges of the
casing.
1. Place impeller key (3-911-1) in shaft
(3-007-0).
2. Check the impeller (4-002-0) and casing
to determine the correct impeller rotation
(See Figure 10) and locate the impeller on
the shaft per dimension “A”. (See
Figure 12)
3. Place both shaft sleeve keys (3-911-3) on
shaft (3-007-0).
4. Slide sleeve gaskets (1-428-1) onto shaft
and against hubs of impeller.
FIGURE 15 - DRILLING SET SCREW RECESS
5. Slide sleeves (3-009-9) onto shaft.
FIGURE 14 - CASING RINGS
FIGURE 16 - GREASE LUBRICATED BEARING
HOUSING
6. Place the sleeve O-ring (3-914-9) onto the
shaft, into the sleeve counterbore. Verify
that Dimension “A” (Figure 12) is
maintained, then using a pin spanner
wrench and hammer, securely tighten the
shaft sleeve nuts (3-015-9). Then, drill a
shallow recess in the shaft through the set
screw hole in each of the shaft sleeve
nuts. Lock each shaft sleeve nut in
position with cup point set screws (3-902-
9). (See Figure 15) A low strength sealant,
such as Loctite 271, can be used to retain
set screws.
7. Assemble casing rings (3-003-9).
8. Start heating bearings (3-026-2) so that
they will be ready when called for in step
11. Use dry heat from induction heat
lamps from electric furnace, or a 10-15%
soluble oil and water solution.
30
CAUTION:
DO NOT EXCEED 275°F.
18. Bolt outboard bearing housing in place. Be
sure that both housing are seated properly
in lower half casing.
CAUTION:
These are precision, high quality bearings.
Excercise care at all times to keep them clean and
free from foreign matter.
9. Press bearing isolators (1-333-1) in each
bearing cover. (See Figure 16) Install
gaskets (3-409-9) on each bearing cover.
10. Slide bearing covers (3-018-3, -4) on the
shaft. Install snap rings (3-915-9). Install
thrust washer (3-078-9) on the outboard
end.
For ease of assembly and protection of
rubber parts while sliding rubber parts
onto shaft, cover O-ring groove, keyways,
and threads with electric tape.
NOTE: Inboard bearing cover (3-018-3) is
approximately 1/4 inch less in width than the
outboard bearing cover (3-018-4). This is the
only dimensional difference.
11. Press heated bearing (3-026-2) on shaft
against snap ring or thrust washer. Install
locknut (3-516-4) and lockwasher (3-517-
4) on outboard end. Make certain locknut
is secured and then bend over tab on
lockwasher.
PUMPS WITH GREASE LUBRICATION
12. Cool bearings at room temperature and
coat with 2 or 3 ounces of a
recommended grease.
19. Bolt inboard bearing housing in place.
20. Clean the gasket surfaces of the casing.
Apply Scotch 3M-77 spray adhesive or
equivalent to the lower half of the casing.
21. Within one minute of spraying, set the
gaskets (2-123-5, -6) in place on the lower
half casing, align the holes in the gaskets
with the holes in the casing and press the
gaskets firmly against the lower half
casing face in the area coated by the
adhesive.
22. Lower upper half casing (2-001-7) into
place (See Figure 17) and locate using the
taper dowels (2-916-9) and install casing
main joint bolts (2-904-9). The casing joint
bolts should be tightened to the following
torques: 300 ft-lb minimum for .75"-10
Ferry Cap Counter-bore screws (Grade 8),
400 ft-lb minimum for 1.0"-8 Ferry Cap
Counter-bore screws (Grade 8). Bolt
torquing pattern is shown in Figure 11.
Before tightening bolts, be sure taper
dowels are seated properly in reamed
holes.
CAUTION:
Double check rotation of pump before
installing the upper half casing. (Refer to figure 10)
13. Press bearing isolator (1-333-1) in inboard
bearing housing and install oil seal (3-177-
15. Assemble bearing cover to bearing
housing with two cap screws (3-904-9).
16. Replace pump coupling half and key (3911-2).
17. Assemble rotating element in lower half
casing (2-001-8). Correctly locate casing
ring pins (3-943-9) in casing main joint
slot.
NOTE: Sliding inboard bearing housing
toward coupling prior to assembling rotating
element in casing will ease assembly.
FIGURE 17 - LOWERING CASING COVER
ONTO LOWER HALF
NOTE: Torque values are essential in
obtaining proper gasket compression so no
leakage can occur at main joint.
23. Rotate shaft by hand to assure that it turns
smoothly and is free from rubbing and
binding.
24. Cut full rings of 5/8 inch square packing so
that ends butt, leaving no gap between
31
packing and casing. Install three rings of
packing (1-924-9) and tap fully to bottom
of both stuffing boxes. (See Figure 18)
Stagger joints of each ring of packing t
least 90°. Install seal cage (1-013-2) and
be sure that it will line up with seal water
inlet when packing is compressed. Install
remaining three rings of packing with
joints staggered. Assemble glands (1-014-
2) square with stuffing box and pull up
tight. Then loosen gland bolts (1-904-9) to
permit packing to expand, and retighten
finger tight. Final adjustment of gland bolts
must be done when pump is running.
Allow 30 minutes between adjustments.
(See Figure 19)
25. Assemble seal water lines (0-901-0, 0950-0, 0-952-0) to stuffing box and casing.
Seal water lines go to inside holes. (See
Figure 12)
26. Check coupling alignment and redowel if
necessary.
For units with drivers having sleeve bearings the
coupling halves are set to limit total shaft axial
movement to less than one-half of he motor rotor
assembly end float. This is accomplished by
inserting a phenolic disc, or equivalent, of a
specified thickness between the motor and pump
shaft (See Figure 20).
Some 9100 Fire Pump installations may use the
all metal, gear type coupling. Where limited end
float gear type couplings are used, the coupling
hubs are slip-fit onto the pump and motor shafts.
After installation of the coupling covers and hubs;
with the motor set on its Magnetic Center, butt the
pump and motor shafts with the phenolic disc
inserted between them. (The pump thrust bearing
limits end float toward the pump, and the coupling
covers limit end float towards the motor.) The
thrust bearing of the pump is large enough to carry
any magnetic thrust developed by the motor when
aligned properly.
Once the above instructions have been followed
out completely, the Alignment Procedures
starting on page 9 should then be followed.
ORDERING PARTS
The pumps covered by this manual have been
designed and built with certain replaceable
wearing parts. The recommended inventory of
spare parts depends upon the installation and the
importance of continued operation.
For critical service requiring a minimum of “down
time” a complete or “quick change” rotating
element is recommended.
For normal service, with repairs to be made in the
field, the following parts are recommended for
stock.
1 set of bearings
1 set of wearing rings
1 set of gaskets, “O” rings and grease seals
2 mechanical seals (complete)
or
2 sets of packing (if provided)
1 set of shaft sleeves (if provided)
Parts should be ordered as far in advance of their
use as possible since circumstances beyond the
control of the company may reduce existing stock.
Not all parts are stocked and must be
manufactured for each order.
COVER
PHENOLIC DISC
parts, be sure to include the following information:
1. Serial number of the pump.
To facilitate rapid handling of your order for spare
HUB
2. Catalog number of the part.
3. Quantity of each part.
4. Name of the part.
MOTOR SHAFT PUMP SHAFT
FIGURE 20 - LIMITED END FLOAT COUPLING
ARRANGEMENT
5. Material desired. (Parts will be furnished in
original materials unless specified as a
material change. All material substitutions
should be discussed with the factory.)
CAPSCREW TORQUE (FOOT-POUND)
CAPSCREW TYPE HEAD MARKING
CAPSCREW DIAMETER
1/45/163/87/161/25/83/47/81
SAE Grade 2 613253860120190210300
Brass
Stainless Steel
or
41017274283130200300
SAE Grade 5 1020356090180325525800
SAE Grade 8 13284675115225370590895
35
DEALER SERVICING
If trouble occurs that cannot be rectified, contact
your local A-C Fire Pump Systems
Representative. They will need the following
information in order to give you assistance.
1. Complete nameplate data of pump and
motor.
2. Suction and discharge pipe pressure
gauge readings.
3. Ampere draw of the motor.
4. A sketch of the pumping hook-up and
piping.
36
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