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7/25/2019 Canned motoer pump
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62 PLANT ENGINEERING JUNE 3,1993
FILE 4010
7/25/2019 Canned motoer pump
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ontaining a fluid while moving it
under pressure has been a problem as
long as there have been pum ps. Early
pumps with packings leaked, but develop-
ments in mechanical face seals dramatical-
ly reduced this problem. However, a study
of
pump failures cited in Practical Ma
chinery Management fo r Process Plants by
H Bloch indicates the nu mber-one cause of
failures is m echanical seals (40%) and, in
second place, antifriction bearings
(7 ).
Sleeve bearings accounted for a small
amount of pum p failures (1 ).
Canned m ot o r and m agne t i c d r i ve
pumps have bypassed the seal problem by
eliminating it. Both pum ps have sealed pri-
mary enc losures, but thats where the sim i-
larity ends. Both canned m otor pu mp bear-
ings are sleeved. M agnetid drive p um ps
have two sleeved bearings and two to four
antifriction bearings.
Canned m otor pumps are one-piece, stat-
ically-sealed, primarily volute-types avail-
able for moving corrosive, volatile, envi-
ronmentally sensitive, and other hard-
to-handle fluids. The pump and motor ro-
tor are assembled on a com mon shaft in a
single unit (Fig. 1 . This design eliminates
alignment, does not re quire external lubri-
ca t ion , and of fe r s double conta in-
ment.
Retrofit canned mo tors are av ailable that
fit an existing pum p w ith little or
no
change
required in piping and hydraulics. Data
such s bearing loads and recirculation
flow are evaluated to en sure that motor and
pump performance do not change (Fig. 2).
The pumped fluid is circulated through
the rotor section to provide cooling for the
mo tor and bearings, lubricant fo r the sleeve
bearings, and thrust control. Fluid is isolat-
ed from motor stator windings by a corro-
sion-resistant nonmagnetic liner. This lin-
er, or can, leads to the term canned
pump.
Liner thickness ranges from 0.0
15
to
0.030 in. and contains pressure to 300 psig.
An outer shell, or secondary containment,
is thicker and capable of containing pres-
sures up to
450
psig, with special designs
rated at
5000
psig.
Pump s are available from 1 to 250 hp,
capacities to
2000
gpm, and fluid tempera-
tures from
-300
to 1000 F.
A common design has a dry stator.
No
dielectric oil or other ty pe of fluid is in th e
stator cavity. This a pproa ch eliminates the
need for an expansion chamber.
Some designs provid e additional cooling
capacity by filling the stator cavity with a
dielectric oil. Besides dissipating heat, th e
oil protects against condensation damage
resulting in expected motor life exceeding
NEMA standards. In this case, an expan-
sion cham ber is required.
An other design fills the stato r cavity with
an inert, high-thermal-conductivity com-
poun d th at helps dissipate heat. Stator vol-
ume is completely filled to prevent the ac-
cumulation of vapor. E xpansion chambers
are not required.
A canned motor pump offers a simple
design, which is inherently efficient. The
pump has two bearings, no coupling or
seals, primary and secondary leak contain-
ment, and low noise levels. In addition, it
doesnt require alignment or lubrication.
Th e overall size is sm all, about 50 of the
space requi rement of a convent iona l
pumping arrangement (Fig. 3 .
Conven tional pumps have four bearings,
seals and seal support system, coupling,
and rigid baseplate to absorb loads and
maintain alignment. There
is
noise from
the motor cooling fan and no secondary
containment.
Magnetic drive pumps have four to six
bearings, are close coupled, or have a cou-
pling and rigid baseplate to absorb loads
and maintain alignment. There is noise
from the motor cooling fan and normally
no
secondary containment.
Fig 1 Canned
motor
pumps
have the stator
chamber dry, oil-Blled, r
solid-fitled. Some designs
providefor dry running
(Courtesy Sundstrand Fluid
Handling,
Diu.
of Milton
Roy Co.).
FILE
4010 JUNE 3 1993
PLANT
ENGINEERING 63
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Canned
motor
pumlbs use sleeve bearings made of
carbon graphite or s i l b n curbide
Fig
2.
Remfitting canned
motors to existing pumps i s
done quickly without dis-
turbing piping. Bearing
flush systems and monitors
are available. (Courtesy
Hayward Tyler, Inc.).
Bearings
Typical sleeve bearing m aterials a re car-
bon graphite and silicon carbide. Carbon
graphite is widely used because of its low
cost. It is self-sacrificing an d un de r certain
conditions runs dry.
If applied properly u nder specific condi-
tion s, silicon carbide p rovides longer bear-
ing life than carbon graphite, particularly
when particles are present. Dry running
and thermal shock are two serious prob-
lems for silicon carbide bearings, because
of their tendency to crack. They ar e consid-
ered an expensive alternative to carbon
graphite.
Since sleeve bearing cleara nces ar e typi-
cally
0.002
to
0.006
in. in canned motor as
well as magnetic drive pumps, large parti-
cles in the fluid stream must be removed
or
ground up by the bearings. Particulate in a
pumping system can consist of weld slag,
pipe scale, sand , ferrous particles, and car-
bonized fluid. Slurries up to
6
by weight
and up t o 0.03-in. in size are removed from
the fluid stream
by
various devices, includ-
ing centrifugal separators, filters, and con-
trolled clearances.
When slurries cannot be removed by
these methods, they are excluded from the
bearing-rotor area by a flush fluid. The
flush fluid is constantly circulated to cool
the m otor, lubricate the bearings, and even-
tually mix with the process fluid. Flush flu-
id
loss
t o the process stream is minimized
by
a
close clearance bushing between the
motor and pum p or a lip seal.
Many types
of
thru st control devices are
available in canned motor pumps. Some
utilize double-acting thrust bearings, com-
bination
of
hydraulic systems,
or
variable
orifices.
A canned motor pump adds up to 100
deg
F
temperature rise (based o n water) to
the fluid circulating through the m otor.
Ap-
proximately 2 to
10 of
total pump flow
is circulated through the motor, depending
on design.
A variety of design configurations pre-
vent flashing
of
volatile fluids. One design
uses a connection from th e pu mp discharge
to inject process fluid into the rear of the
motor, where the process fluid is directed
into an auxiliary impeller which pressur-
izes the fluid above discharge pressure. T he
fluid circulates through t he m otor, removes
heat, and returns to the pump discharge.
This design allows the addition of heat to
process f lu ids bu t main ta ins p ressure
above the flash point.
Another design uses reverse circulation
through the motor section of the pump.
Process fluid is returned to the vapor zone
of the supply vessel through a connection a t
the rear of the motor. The return line is
throttled to maintain high liquid pressure
within the m otor an d serves as a vent line.
Shaft Deflection
The L3/D4 ratio, sometim es called the
shaft flexibility factor (SFF), is a measure
of shaft deflection. The higher the ratio,
or
more shaft deflection, the greater the main-
tenance cost on overhung cen t r i fugal
pumps. Increased deflection causes more
wear on bearings, shaft sleeves, wear rings,
and other close-tolerance pump parts.
For
this reason, many users making an econom-
ic analysis assess a maintenance penalty
against pum ps with high ratios.
Canned motor pum ps have low
L3/D4
a-
tios elow 30. Stand ard API pump ra-
tios range from 35 to over 200.
ccessories
Several accessories are available to up-
grade canned motor pump installations.
Bearing
moni to rs
The primary failure
items in canned motor pumps ar e bearings.
Many times they are cooled an d lubricated
by process fluids with very low viscosities
and poor lubricating qualities. T he solution
is to monitor bearing wear in order to re-
place them before failure occurs.
Bearing monitors are available in several
designs and on most ca nned motor pumps.
They are up to 98 accurate in preventing
catastrophic failure and indicate when a
bearing change needs to be m ade. Th is sig-
nal eliminates dismantling a canned motor
pump according to a fixed schedule to
check
for
bearing wear.
Bearing wear causes material in a sensor
64 PLANT
ENGINEERING* JUNE 3,1993
FILE 4010
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to be removed, creatin g a signal that warns
of the amo unt of bearing life remain ing be-
fore failure. One design has a tube with a
mushroom -shaped, gas-pressurized contact
tip. Wear at the monitor tip is caused by
either or both radial and axial shaft move-
ment corresponding to sleeve or thrust
washer wear. At two-thirds of maxim um al-
lowable bearing wear, the tip and end nut
contact, rupturing the tip. The resulting
change in pressure in the tube displays on
an external gauge or actuates a pressure
switch. In ad ditio n, this design is useful in
detecting corrosion of th e rotor sleeve, be-
cause the con tact tip is supp lied in a metal-
lurgy similar to, bu t one -half the thick ness
of, the sleeve.
Another design consis ts of a,Teflon-coat-
ed ring affixed to the rear bearing assembly
and wired to a detector module. When
maximum allowable bearing wear occurs,
the rotor shaft rubs through the Teflon
coating, makes contact with a metal inner
ring, and co mp letes an electrical circuit. A
signal is generated indicating the bearings
shou ld be replaced.
Other designs indicate worn bearings
and eccentric shaft rotation by rubbed-off
dielectric coatings or interrupted fiber op-
tic paths.
Temperature sensors Pumped product
temperature is measured in the rotor area
near the bearings. A thermocouple used
with a temperature indicating device shuts
down the pump w hen abnormal rotor cavi-
t y temp eratures occur. Otherwise, flashing,
polymerization, or crystallization could oc-
cur and cause rapid bearing failure.
Over/under current relays These relays
detect dry running.
Direction
of
rotation indicators Because
rotating pa rts a re no t exp osed, it is difficult
to
determine whether the pump is rotating
in th e right d irection. An electrical*device
senses if the electrical phase sequence is
compatible with the motor windings. A
light indicates if the m otor is running in the
right direction. The usual way to determine
if the pump is rotating properly is to use
two gauges, one in the su ction end and one
in the discharge end. Normally the dis-
charge-end gauge should have the higher
reading.
Thermostats Thermostats are installed
in motor windings to protect insulation
from premature failure. In the event the
moto r windings reach a preset temp erature
limit, the pum p automatically shuts down
before permanent damage occurs.
Selection
Process and fluid information are re-
quired to select a canned m otor pump, be-
FILE
4010
cause each application is fluid specific. D e-
signs are available to handle blended fluids
with different properties, temperatures,
pressures, and particles. Typical selection
factors include:
Substance pumped
Operating temperature and pressure
ranges
I Fluid properties (at startup and pump-
ing temperature)
Viscosity
Specific gravity
r Vapor pressure
Specific h eat
Solids in suspension
Largest solids particle size
c Average solids particle size
I Quantity of solids
Abrasive qualities
Fig.
3.
Spwe
requirements
for canned motor pumps
are approximately 50% of
those needed
by
conventfon-
al and magnetfc drives.
JUNE 3,1993 PLANT ENGINEERING 65
7/25/2019 Canned motoer pump
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Maintenance a n be done ' in-house
s
part of
re g maintenance with avaiGabGe kiis
V Operating conditions
V Flow
V Discharge head
I Suction head
V
NPSH available.
This info rmatio n is necessary to properly
size a pump, select bearing material, pro-
vide sufficient cooling flow to the motor,
lubricate bearings, ensure any axial thrust
is balanced, keep pu mp ed fluid from flash-
ing
or
overheating, and provide bearing
protection from particles. Pum p m anufac-
turers request specific information before
recommending a pump , and provide appli-
cation engineering for unusual or difficult
conditions.
Maintenance
Many canned motor pumps are field re-
pairable, which helps reduce costs when
performing routine maintenance, such as
changing bearings. Some liners in canned
motor pumps are welded and must be re-
turned to the factory for repair.
When repairs are done in the field, they
usually consist of bearing assembly (includ-
ing thrust washers and shaft sleeves),
0
ring seal, and bearing monitor replace-
men t. In many cases these are don e in a few
hours. Prepackaged kits are available and
include par t s , tools , and i l lus t ra te(
instructions.
PLANT ENGIN EERIN Gagazine would like to thank AB
Pumps Lawrence Pump Engine Div.; Carbone
USA
Corp
Chempump Div. Crane Co ; Cooper C ommunications: Gi
lette Brown Assoc.; Gou lds Pumps Inc.; Hayward Tyle
Inc.; Hydraulic Institute; KSB Inc.; Laing Therm otec. Inc
David Moore Assoc iates Inc.; Sundstrand Fluid Har
dling Div. of Milton Roy Co : and Teikoku USA
Inc.; fc
their special contribution s to the development of this articlc
For more information..
Sealless Centrifugal
Pump
Standards HI 5.1
5.6 1992 published by the Hydraulic Institute
is an excellent source of information on the
design use and maintenance of canned and
magnetic drive pumps. Contact the Institute at
9 Sylvan Way Parsippany
NJ
07054-3802
201 267-9700 for information.
API Standard 685 Sealless Centrifugal
Pumps
for Refinery Services is in the process
of being written and reviewed. For additional
information contact the American Petroleum
Institute at 1220
L
St. NW Washington DC
. Joseph
L. Foszcz
Senior Editor 708-390-
2699
20005; 202-682-8000.
For information on how t o order copies of
this
article
circle 10 on post card
For additional nformation on canned motor pumps,
circle the number on the Reader Service Card in this issue.
RS Company
i6 PLANT ENGINEERING JUNE 3,1993
FILE
4010
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