To establish Approvals and if the product itself is CE
Marked check the serial number plate and the
Certification.
1.1 General
These Instructions must always be kept
close to product's operating location or directly
with the product.
Flowserve's products are designed, developed and
manufactured with state-of-the-art technologies in
modern facilities. The unit is produced with great care
and commitment to continuous quality control,
utilising sophisticated quality techniques, and safety
requirements.
Flowserve is committed to continuous quality
improvement and being at service for any further
information about the product in its installation and
operation or about its support products, repair and
diagnostic services.
These instructions are intended to facilitate
familiarization with the product and its permitted use.
Operating the product in compliance with these
instructions is important to help ensure reliability in
service and avoid risks. The instructions may not take
into account local regulations; ensure such regulations
are observed by all, including those installing the
product. Always coordinate repair activity with
operations personnel, and follow all plant safety
requirements and applicable safety and health
laws/regulations.
These instructions must be read prior to
installing, operating, using and maintaining the
equipment in any region worldwide. The
equipment must not be put into service until all
the conditions relating to safety, noted in the
instructions, have been met. Failure to follow and
apply the present user instructions is considered
to be misuse. Personal injury, product damage,
delay or failure caused by misuse are not covered
by the Flowserve warranty.
1.3 Disclaimer
Information in these User Instructions is believed
to be reliable. In spite of all the efforts of
Flowserve Corporation to provide sound and all
necessary information the content of this manual
may appear insufficient and is not guaranteed by
Flowserve as to its completeness or accuracy.
Flowserve manufactures products to exacting
International Quality Management System Standards
as certified and audited by external Quality
Assurance organisations. Genuine parts and
accessories have been designed, tested and
incorporated into the products to help ensure their
continued product quality and performance in use. As
Flowserve cannot test parts and accessories sourced
from other vendors the incorrect incorporation of such
parts and accessories may adversely affect the
performance and safety features of the products. The
failure to properly select, install or use authorised
Flowserve parts and accessories is considered to be
misuse. Damage or failure caused by misuse is not
covered by Flowserve's warranty. In addition, any
modification of Flowserve products or removal of
original components may impair the safety of these
products in their use.
1.4 Copyright
All rights reserved. No part of these instructions may
be reproduced, stored in a retrieval system or
transmitted in any form or by any means without prior
permission of Flowserve.
1.5 Duty conditions
This product has been selected to meet the
specifications of your purchaser order. The
acknowledgement of these conditions has been sent
separately to the Purchaser. A copy should be kept
with these instructions.
1.2 CE marking and approvals
It is a legal requirement that machinery and
equipment put into service within certain regions of
the world shall conform with the applicable CE
Marking Directives covering Machinery and, where
applicable, Low Voltage Equipment, Electromagnetic
Compatibility (EMC), Pressure Equipment Directive
(PED) and Equipment for Potentially Explosive
Atmospheres (ATEX).
Where applicable the Directives, and any additional
Approvals, cover important safety aspects relating to
machinery and equipment and the satisfactory
provision of technical documents and safety
instructions. Where applicable this document
incorporates information relevant to these Directives.
Page 3 of 52
The product must not be operated beyond
the parameters specified for the application. If
there is any doubt as to the suitability of the
product for the application intended, contact
Flowserve for advice, quoting the serial number.
If the conditions of service on your purchase order
are going to be changed (for example liquid pumped,
temperature or duty) it is requested that the user
seeks Flowserve´s written agreement before start
up.
1.6 Safety
1.6.1 Summary of safety markings
These user instructions contain specific safety
markings where non-observance of an instruction
would cause hazards. The specific safety markings
are:
This symbol indicates electrical safety instructions
where non-compliance will involve a high risk to
personal safety or the loss of life.
This symbol indicates safety instructions
where non-compliance would affect personal safety
and could result in loss of life.
This symbol indicates "hazardous and toxic
fluid" safety instructions where non-compliance would
affect personal safety and could result in loss of life.
instructions where non-compliance will involve some
risk to safe operation and personal safety and would
damage the equipment or property.
field" safety instructions where non-compliance would
affect personal safety, pacemakers, instruments or
stored data sensitive to magnetic fields.
This symbol indicates safety
This symbol indicates "strong magnetic
WUC USER INSTRUCTIONS ENGLISH - 07/14
1.6.2 Personnel qualification and training
All personnel involved in the operation, installation,
inspection and maintenance of the unit must be
qualified to carry out the work involved. If the
personnel in question do not already possess the
necessary knowledge and skill, appropriate training
and instruction must be provided. If required the
operator may commission the manufacturer / supplier
to provide applicable training.
Always co-ordinate repair activity with operations and
health and safety personnel, and follow all plant
safety requirements and applicable safety and health
laws/regulations.
1.6.3 Safety action
This is a summary of conditions and actions to
help prevent injury to personnel and damage to
the environment and to equipment. For products
used in potentially explosive atmospheres
section 1.6.4 also applies.
PREVENT EXCESSIVE
EXTERNAL PIPE LOAD
Do not use pump as a support for piping. Do not
mount expansion joints so that their force, due to
internal pressure, acts on the pump flange.
ONLY CHECK DIRECTION OF
MOTOR ROTATION WITH COUPLING ELEMENT/
PINS REMOVED
Starting in reverse direction of rotation will damage
the pump.
This symbol indicates explosive atmosphere
marking according to ATEX. It is used in safety
instructions where non-compliance in the hazardous
area would cause the risk of an explosion.
This symbol is used in safety instructions to
remind not to rub non-metallic surfaces with a dry
cloth; ensure the cloth is damp. It is used in safety
instructions where non-compliance in the hazardous
area would cause the risk of an explosion.
The sign is not a safety symbol but
indicates an important instruction in the assembly
process.
This symbol indicates potential risks
connected with extremely high temperatures.
This symbol indicates potential risks
connected with extremely low temperatures.
ENSURE CORRECT
LUBRICATION
(See section 5 Commissioning, startup, operation and shutdown.)
START THE PUMP WITH
OUTLET VALVE PART OPENED
(Unless otherwise instructed at a specific point in the
user instructions.)
This is recommended to avoid the risk of overloading
and damaging the pump motor at full or zero flow.
Pumps may be started with the valve further open
only on installations where this situation cannot
occur. Pump outlet valve shall be adjusted to comply
with the duty following the run-up process (See
section 5 Commissioning, startup, operation and shutdown).
START THE PUMP WITH
OUTLET VALVE FULLY OPEN
This is recommended to avoid the risk of overloading
and damaging the pump motor where greater power
is taken at low or shut off flow. Pump outlet valve
shall be adjusted to comply with the duty following the
Page 4 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
run-up process (See section 5 Commissioning, startup, operation and shutdown).
NEVER RUN THE PUMP DRY
INLET VALVES TO BE FULLY
OPEN WHEN PUMP IS RUNNING
Running the pump at zero flow or below the
recommended minimum flow continuously will cause
damage to the seal.
DO NOT RUN THE PUMP AT
ABNORMALLY HIGH OR LOW FLOW RATES
Operating at a flow rate higher than normal or at a
flow rate with no back pressure on the pump may
overload the motor and cause cavitation. Low flow
rates may cause a reduction in pump/bearing life,
overheating of the pump, instability and
cavitation/vibration.
When ambient temperatures are
likely to drop below freezing point, the pump and any
cooling and flushing arrangements must be drained
or otherwise protected.
HANDLING COMPONENTS
Many precision parts have sharp corners and the
wearing of appropriate safety gloves and equipment
is required when handling these components. To lift
heavy pieces above 25 kg (55 lbs) use a crane
corresponding to the mass and in accordance with
current local regulations.
NEVER DO MAINTENANCE WORK WHILST THE
UNIT IS CONNECTED TO POWER
HAZARDOUS LIQUIDS
When the pump is handling hazardous liquids care
must be taken to avoid exposure to the liquid by
appropriate sitting of the pump, limiting personnel
access and by operator training. If the liquid is
flammable and/or explosive strict safety procedures
must be applied.
Gland Packing must not be used when pumping
hazardous liquids.
condition these are extremely dangerous and skin
contact must be avoided.
GUARDS MUST NOT BE REMOVED WHILE
PUMP IS OPERATIONAL
THERMAL SHOCK
Rapid changes in the temperature of the liquid within
the pump can cause thermal shock, which can result
in damage or breakage of components and should be
avoided.
NEVER APPLY HEAT TO REMOVE
IMPELLER
Trapped lubricant or vapour could cause an
explosion.
If hot or freezing components or auxiliary heating
supplies can present a danger to operators, they
must be shielded to avoid accidental contact. If
complete protection is not possible, the machine
access must be limited to maintenance staff only.
Note: bearing housings must not be insulated and
drive motors and bearings may be hot.
If the temperature is greater than 68 °C (155 °F) o r
below 5 °C (41 °F) in a restricted zone, or exceeds
local regulations, action as above shall be taken.
1.6.4 Products used in potentially explosive
atmospheres
Measures are required to:
• Avoid excess temperature
• Prevent build up of explosive mixtures
• Prevent the generation of sparks
• Prevent leakages
• Maintain the pump to avoid hazard
The following instructions for pumps and pump units
when installed in potentially explosive atmospheres
must be followed to help ensure explosion protection.
Both electrical and non-electrical equipment must
meet the requirements of European Directive
94/9/EC.
1.6.4.1 Scope of compliance
HOT AND COLD PARTS
DRAIN PUMP AND ISOLATE PIPEWORK
BEFORE DISMANTLING THE PUMP
The appropriate safety precautions should be taken
where the pumped liquids are hazardous.
FLUORO-ELASTOMERS (When fitted)
When a pump has experienced temperatures over
250 °C (482 ºF), partial decomposition of fluoroelastomers (example: Viton) will occur. In this
Page 5 of 52
Use equipment only in the zone for which it is
appropriate. Always check that the driver, drive
coupling assembly, seal and pump equipment are
suitably rated and/or certified for the classification of
the specific atmosphere in which they are to be
installed.
Where Flowserve has supplied only the bare shaft
pump, the Ex rating applies only to the pump. The
WUC USER INSTRUCTIONS ENGLISH - 07/14
party responsible for assembling the pump set shall
select the coupling, driver and any additional
equipment, with the necessary CE Certificate/
Declaration of Conformity establishing it is suitable for
the area in which it is to be installed.
The output from a variable frequency drive (VFD) can
cause additional heating affects in the motor and so,
for pump sets with a VFD, the ATEX Certification for
the motor must state that it covers the situation where
electrical supply is from the VFD. This is particular
requirement still applies even if the VFD is in a safe
area.
1.6.4.2 Marking
An example of ATEX equipment marking is shown
below. The actual classification of the pump will be
engraved on the nameplate.
II 2 GD c IIC135ºC (T4)
Equipment Group
I = Mining
II = Non-mining
Category
2 or M2 = High level protection
3 = normal level of protection
Gas and/or Dust
G = Gas; D= Dust
c = Constructional safety
(in accordance with EN13463-5)
b = Control of ignition source
(in accordance with EN13463-6)
Gas Group
IIA – Propane (Typical)
IIB – Ethylene (Typical)
IIC – Hydrogen (Typical)
Maximum surface temperature (Temperature Class)
(see section 1.6.4.3)
1.6.4.3 Avoiding excessive surface temperatures
ENSURE THE EQUIPMENT TEMPERATURE
CLASS IS SUITABLE FOR THE HAZARD ZONE
Pumps have a temperature class as stated in the
ATEX Ex rating on the nameplate. These are based
on an ambient in the range of -80 to +55 ºC (-112 to
+131 ºF); refer to Flowserve for ambient
temperatures outside this range for this product.
The surface temperature on the pump is influenced
by the temperature of the liquid handled. The
maximum permissible liquid temperature depends on
the ATEX temperature class and must not exceed the
values in the table that follows.
Temperature
class to
EN 13463-1
T6
T5
T4
T3
T2
T1
Maximum
surface
temperature
permitted
85 °C (185 °F)
100 °C(212 °F)
135 °C (275 °F)
200 °C (392 °F)
300 °C (572 °F)
450 °C (842 °F)
Temperature limit of liquid
handled (* depending on
material and construction
variant - check which is
lower)
Consult Flowserve
Consult Flowserve
115 °C (239 °F) *
180 °C (356 °F) *
275 °C (527 °F) *
400 °C (752 °F) *
* The table only takes the ATEX temperature class into
consideration. Pump design or material, as well as component
design or material, may further limit the maximum working
temperature of the liquid.
The temperature rise at the seals and bearings and
due to the minimum permitted flow rate is taken into
account in the temperatures stated.
The responsibility for compliance with the
specified maximum liquid temperature is with the
plant operator.
Temperature classification “Tx” is used when the
liquid temperature varies and when the pump is
required to be used in differently classified potentially
explosive atmospheres. In this case the user is
responsible for ensuring that the pump surface
temperature does not exceed that permitted in its
actual installed location.
Do not attempt to check the direction of rotation with
the coupling element/pins fitted due to the risk of
severe contact between rotating and stationary
components.
Where there is any risk of the pump being run against
a closed valve generating high liquid and casing
external surface temperatures it is recommended that
users fit an external surface temperature protection
device.
Avoid mechanical, hydraulic or electrical overload by
using motor overload trips or a Power Monitor and
make routine vibration monitoring.
In dirty or dusty environments, regular checks must
be made and dirt removed from areas around close
clearances, bearing housings and motors.
Level control shall be fitted in the sump to prevent
liquid level dropping below minimum acceptable.
It is recommended that a Service Plan with vibration
monitoring is adopted, alternatively the user should fit
external bearing housing surface temperature
protection device(s) to ensure the temperature class,
i.e. maximum surface temperature, is not exceeded.
For external flush the flow should be monitored.
Page 6 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
1.6.4.4 Preventing the build up of explosive
mixtures
ENSURE THE PUMP IS PROPERLY FILLED
AND VENTED AND DOES NOT RUN DRY
Ensure the pump and relevant suction and discharge
pipeline system is totally filled with liquid at all times
during the pump operation, so that an explosive
atmosphere is prevented. In addition it is essential to
make sure that seal chambers, auxiliary shaft seal
systems and any heating and cooling systems are
properly filled.
If the operation of the system cannot avoid this
condition the fitting of an appropriate Dry Run
protection device is recommended (eg liquid
detection or a Power Monitor).
To avoid potential hazards from fugitive emissions of
vapour or gas to atmosphere the surrounding area
must be well ventilated.
1.6.4.5 Preventing sparks
To prevent a potential hazard from mechanical
contact the coupling guard must be non-sparking and
anti-static.
To avoid the potential hazard from random induced
current generating a spark the earth contact on the
baseplate must be used.
Avoid electrostatic charge: do not rub nonmetallic surfaces with a dry cloth; ensure cloth is
damp.
The coupling must be selected to comply with
94/9/EC and correct alignment must be maintained.
1.6.4.5 Preventing leakage
The pump must only be used to handle liquids
for which it has been approved to have the correct
corrosion resistance.
Avoid entrapment of liquid in the pump and
associated piping due to closing of suction and
discharge valves, which could cause dangerous
excessive pressures to occur if there is heat input to
the liquid. This can occur if the pump is stationary or
running.
Bursting of liquid containing parts due to freezing
must be avoided by draining or protecting the pump
and ancillary systems.
Where there is the potential hazard of a loss of a seal
barrier fluid or external flush, the fluid must be
monitored.
If leakage of liquid to atmosphere can result in a
hazard, the installation of a liquid detection device is
recommended.
1.6.4.6 Maintenance to the centrifugal pump to
avoid the hazard
CORRECT MAINTENANCE IS REQUIRED
TO AVOID POTENTIAL HAZARDS WHICH GIVE A
RISK OF EXPLOSION
The responsibility for compliance with
maintenance instructions is with the plant
operator.
To avoid potential explosion hazards during
maintenance, the tools, cleaning and painting
materials used must not give rise to sparking or
adversely affect the ambient conditions. Where there
is a risk from such tools or materials, maintenance
must be conducted in a safe area.
It is recommended that a maintenance plan and
schedule is adopted (see section 6, Maintenance).to
include the following.
a) Any auxiliary systems installed must be
monitored, if necessary, to ensure they function
correctly.
b) Gland packings must be adjusted correctly to
give visible leakage and concentric alignment of
the gland follower to prevent excessive
temperature of the packing or follower.
c) Check for any leaks from gaskets and seals. The
correct functioning of the shaft seal must be
checked regularly
d) Check bearing lubricant level, and if the hours run
show a lubricant change is required.
e) Check that the duty condition is in the safe
operating range for the pump.
f) Check vibration, noise level and surface
temperature at the bearings to confirm
satisfactory operation.
g) Check dirt and dust is removed from areas
around close clearances, bearing housings and
motors.
h) Check coupling alignment and re-align if
necessary.
Page 7 of 52
1.7 Warning label
WUC USER INSTRUCTIONS ENGLISH - 07/14
Page 8 of 52
1.8 Specific machine performance
For performance parameters see section 1.5, Duty
conditions. When the Contract requirement specifies
these to be incorporated into user instructions these
are included here. Where performance data has been
supplied separately to the purchaser these should be
obtained and retained with these user instructions if
required.
1.9 Noise level
Attention must be given to the exposure of personnel
to the noise, and local legislation will define when
guidance to personnel on noise limitation is required,
and when noise exposure reduction is mandatory.
This is typically 80 to 85 dBA.
The usual approach is to control the exposure time to
the noise or to enclose the machine to reduce
emitted sound. You may have already specified a
limiting noise level when the equipment was ordered,
however if no noise requirements were defined, then
attention is drawn to the following table to give an
indication of equipment noise level so that you can
take the appropriate action in your plant.
Pump noise level is dependent on a number of
operational factors, flow rate, pipework design and
acoustic characteristics of the building, and so the
values given are subject to a 3 dBA tolerance and
cannot be guaranteed.
Similarly the motor noise assumed in the “pump and
motor” noise is that typically expected from standard
and high efficiency motors when on load directly
driving the pump. Note that a motor driven by an
inverter may show an increased noise at some
speeds.
If a pump unit only has been purchased for fitting with
your own driver then the “pump only” noise levels in
the table should be combined with the level for the
driver obtained from the supplier. Consult Flowserve
or a noise specialist if assistance is required in
combining the values.
It is recommended that where exposure approaches
the prescribed limit, then site noise measurements
should be made.
The values are in sound pressure level LpA at 1 m
(3.3 ft) from the machine, for “free field conditions
over a reflecting plane”.
For estimating sound power level LWA (re 1 pW) then
add 14 dBA to the sound pressure value.
WUC USER INSTRUCTIONS ENGLISH - 07/14
Page 9 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
the combined noise level,dB
levels to be combined, dB
Octave MID BAND frequency [Hz]
Motorstand 0
1450 rpm
1760 rpm
2900 rpm
3600 rpm
Motorstand 1
3000 rpm
1500 rpm
3600 rpm
1800 rpm
Motorstand 3
3000 rpm
1500 rpm
3600 rpm
1800 rpm
Motorstand 4
3000 rpm
1500 rpm
1800 rpm
Motorstand 5
3000 rpm
1500 rpm
1800 rpm
Motorstand 6
1500 rpm
1800 rpm
Motorstand 7
1500 rpm
1800 rpm
Motorstand 8
1500 rpm
1800 rpm
Sound pressure readings are for information only and are not subject to guarantee by Flowserve/IDP.
Decibel readings do not include driver or system noise.
Pump tested at 100% of the best efficiency point at max.impeller diameter with water.
dB correction for combining noises (pump+motor)
Difference between two
Add to the higher level to obtain
Note :
1) The values showed are measured at a distance of 1 mt. (horizontally) from major pump
surfaces and 1.5 mt. above the floor.
2) The values shown are expressed in dB (A)
3) For Noise Test Procedure refer to Works Standard L-109
4) The values shown have been derived from actual noise-test data and are based on the following conditions:
-
-
-
-
When the required condition flow is outside the range of 75 to 125% BEP, a part load correction (PLC) must be
added to the noise level as follows:
Equipment is located in a free field above a reflecting plane in which the reductionin noise level
in all directions is 6db in each octave band for each doubling of distance.
Background noise is 10dB minimum below all noise levels in each octave band.
The values shown are at a distance of 1 meter (horizontally) from the major pump surface and
1,5 meters above the floor, using a standard pressure reference of 0,00002 newton per square meter.
Overall noise level, dB(A) is determined at points of maximum noise level and the values of all
mid-band frequences are basis A scale readings.
Percent of BEP @
required impeller
diameter
PLC in
dB
74 to 62 or 126 to 136+1
61 to 50 or 137 to 150+2
49 to 38+3
37 to 25+4
Page 10 of 52
1.10 CE Declaration
WUC USER INSTRUCTIONS ENGLISH - 07/14
Page 11 of 52
2.0 TRANSPORT AND STORAGE
2.1 Consignment receipt and unpacking
Immediately after receipt of the equipment it must be
checked against the delivery and shipping documents
for its completeness and that there has been no
damage in transportation.
Any shortage and or damage must be reported
immediately to Flowserve and received in writing
within one month of receipt of the equipment. Later
claims cannot be accepted.
Check any crates, boxes and wrappings for any
accessories or spare parts which may be packed
separately with the equipment or attached to side
walls of the box or equipment.
Each product has a unique serial number. Check that
this number corresponds with that advised and
always quote this number in correspondence as well
as when ordering spare parts or further accessories.
WUC USER INSTRUCTIONS ENGLISH - 07/14
on their respective nameplates.
In some cases the pumps are not
complete assembled (refer to section 4, Installation).
If Can and supporting flange are delivered
separately, lifting shall be performed as follows:
Suction barrel [1100.1] (also referred as ‘Can’) is
supplied together with supporting flange [6110] and
has to be installed into the sump first. Suction barrel
and supporting flange are delivered assembled
together. 4 distance sleeves are installed to fix both
parts together.
Install 4 lifting screws (also referred as ‘Eye Bolts’) on
the supporting flange and attach slings and straps to
bring the suction barrel to a vertical position. Move
the barrel for installation. Provide hand support to
prevent the suction barrel from swaying during
movement.
2.2 Handling
Boxes, crates, pallets or cartons may be unloaded
using fork lift vehicles or slings dependent on their
size and construction.
2.3 Lifting
To avoid distortion, the pump unit should be
lifted as shown.
For lifting the driver refer to the
dimension drawing of driver.
2 holes Ø 45mm (1.77 in.) for
lifting the pump without can
and driver
4 pieces lifting screw
according DIN 580 only for
CAN lifting
Depending on the pump
size the pump unit is
packed separately from the
Can, or is put partially into
the Can.
Distance sleeves are only used for fixing the
base plate during transportation.
A crane must be
used for all pump sets in
excess of 25 kg (55 lb).
Fully trained personnel
must carry out lifting, in
accordance with local
regulations. The driver and
pump weights are recorded
Page 12 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
2.4.1 Long period storage
If the pump is delivered in a plastic bag, the
preservations stand up for one year. If the storage
period exceeds this time, the preservation must be
checked and renewed. Also the air tight plastic bag
must be changed. Moreover we recommend to order
a Flowserve Service Engineer for checking the pump
before the first start up.
2.5 Recycling and end of product life
At the end of the service life of the product or its
parts, the relevant materials and parts should be
recycled or disposed of using an environmentally
acceptable method and local regulations. If the
product contains substances which are harmful to the
environment, these should be removed and disposed
of in accordance with current regulations. This also
includes the liquids and or gases in the "seal system"
or other utilities.
Make sure that hazardous substances are
disposed of safety and that the correct personal
protective equipment is used. The safety
specifications must be in accordance with the current
regulations at all times.
2.4 Storage
If the pump will not be put immediately into service, it
should be stored in a dry room. To avoid any damage
during the storage period, the influence of any low or
high frequency vibration must be totally inhibited. If
the pump is delivered sealed in a plastic-wrapper, it is
of max. importance to avoid any damage of that
wrapper, because this will protect the pump against
humidity. Therefore it must be checked if this wrapper
has become cracked and if so, the wrapper must be
renewed. If a vertical pump will be stored in horizontal
position, be sure to support the pump sufficiently to
avoid any deformation or bending of the pump.
To avoid the presence of dust and humidity on the
driver, it shall also be wrapped in the same way.
3.0 DESCRIPTION
3.1 Configuration
The model WUC covers the highly engineered
specialty end of the Flowserve family of double
casing vertical turbine pumps. The pump line is
based on a modular system, thus providing maximum
design and operating flexibility. This is combined with
specific design features, including stiff shaft
construction, a self-contained axial thrust bearing
housing and pressure containing parts certified to
various international standards. Altogether, this
makes the WUC the pump of choice for the most
critical applications where space considerations or
marginal NPSHA values preclude the use of a
horizontal multistage pump.
Liquid is flowing through the suction flange of the
headstock and through the Can to the impellers. The
last stage impeller is discharging the liquid via the
column pipes, to the discharge flange. The thrust is
balanced by back wearing rings and balancing holes.
The headstock is equipped with a drain connection,
which allows to flush the Can with Nitrogen before
disassembly.
A vent connection for the suction is standard.
The sense of rotation of the pump is counter
clockwise (CCW), looking from the coupling to the
shaft end of the pump.
Page 13 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
3.2 Nomenclature
Example:
200WUC-2M-5+I
200 Flow at BEP
WUC Pump type - Can
WUJ = without Can
2 indicates speed 2–poles
4 = 4-poles
Mindicates hydraulic Medium Head L = Low Head
H = High Head
R = Radial Flow
5 Number of stages
I indicates Inducer as option
D Dummy stage as option
3.3 Design of major parts
3.3.1 Motor stool
The motor stool supports the thrust bearing. On top
the driver is mounted.
balanced by back wear rings and balancing holes.
The diffusers are designed with 7 to 11 vanes to
minimize the radial forces at part load operation. All
impellers are slipped on the shaft and axially fixed by
the impeller nut. The shaft is supported in the suction
casing and in each bowl.
Optional the hydraulics can be fitted with an inducer
for low NPSH requirement.
3.3.4.3 10WUC-2H
The hydraulic consists of bowls, which are pushed
together and hold by strong tie bolts. The impellers
are secured to the shaft by split rings. Due to the
small size, the impellers are only equipped with front
wear rings and therefore unbalanced.
Optional the hydraulics can be fitted with an inducer
for low NPSH requirement.
3.3.4.4 20WUC-2L, 45WUC-2L, 80WUC-2L
The hydraulics consists of flanged bowls and a
suction casing. The impellers are secured to the shaft
by split rings. Due to the small size, the impellers are
only equipped with front wear rings and therefore
unbalanced.
Optional the hydraulics can be fitted with an inducer
for low NPSH requirement.
3.3.2 Headstock
Headstock has inline suction and discharge nozzle,
including all the necessary vent and drain
connections. It is a major part of the pump unit, which
supports the column pipes with the hydraulics as well
as the motor stool and driver.
3.3.3 Can
The Can is subjected to suction pressure and guides
the fluid to the first stage impeller.
3.3.4 Hydraulics
3.3.4.1 Radial flow hydraulics
This are ring section type hydraulics. Suction, stage
and discharge casing are hold together by strong tie
bolts, which allows a very compact and short design.
The radial impellers are hydraulically balanced by
back wear rings and balancing holes. The diffusers
are designed with 7 to 11 vanes to minimize the
radial forces at part load operation. All impellers are
slipped on the shaft and axially fixed by the impeller
nut. The shaft is supported in the suction casing, in
every diffuser and in the discharge casing.
Optional the hydraulics can be fitted with an inducer
for low NPSH requirement.
3.3.4.2 Mixed flow hydraulics
The hydraulics consists of flanged bowls and a
suction casing. The impellers are hydraulically
3.4 Performance and operating limits
In the interest of operator safety
the unit must not be operated above the nameplate
conditions. Such operation could result in unit failure
causing injury to operating personnel. Consult
instruction book for correct operation and
maintenance of the pump and its supporting
components.
4.0 INSTALLATION
Equipment operated in hazardous locations
must comply with the relevant explosion protection
regulations, see section 1.6.4, Products used in
potentially explosive atmospheres.
4.1 Location
The pump should be located to allow room for
access, ventilation, maintenance and inspection with
ample headroom for lifting and should be as close as
practicable to the supply of liquid to be pumped.
Refer to the general arrangement drawing for the
pump set.
Page 14 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
4.2 Part Assemblies
With exception of the Can the pumps are delivered
completely mounted and adjusted; also the shaft seal is
in the correct position. So no further axial alignment of
the rotor is necessary. If drivers and/or seal systems
are delivered separately, follow the assembly
procedure in section 6.9.
Axial alignment and rotor setting axial
adjustment need to be distinguished. For correct axial
adjustment of the rotor refer to 5.3.1 Adjusting of the rotor.
4.3 Foundation
The foundation shall be located on a place that
allows a minimum of pipe work and that is easily
accessible for inspection during operation. According
to the environment the foundation may consist of
concrete or of steel. It must be rigid and heavy
enough to absorb normal vibrations and shocks. The
flange of the Can must be supported on the whole
surface. It should be at least 20 – 30 mm
(0.8 – 1.2 in) higher than the surrounding to avoid the
deposit of dust and humidity.
4.3.1 Vertical alignment
Vertical alignment is done with leveling screws.
Use a spirit level for correct horizontal alignment of
the baseplate.
The max. vertical misalignment is 0.5 mm/m
pump length.
4.3.2 Steel foundation
When the pump unit is mounted directly on structural
steel frame, it shall be well supported by constructural
beams. It is recommended to check the natural
frequency of the steel frame, because it shall not
coincide with the pump speed. The flange of the Can
has to be fixed on a flat surface with studs or hex
screws, the exact horizontal alignment is very
important!
4.3.3 Concrete foundation
A concrete foundation must have an exact horizontal
alignment and must be placed on solid ground. First
a basic foundation shall be built with square shaped
holes for embedding the foundation bolts. After
putting the Can in the foundation the proper
alignment can be obtained by adjusting it with shims
under the flange. Now insert the foundation bolts and
grout the space between the basic foundation and
the Can with grouting cement (refer to illustration)
It is very helpful to use a properly made and stable
wooden frame around the Can. So the grouting cement
will not flow a side. When the grouting is totally set and
hardened the foundation bolts shall be tightened in a
firm and symmetrical way.
4.3.4 Final assembly for not complete assembled
pumps
Pumps exceeding a total length of approximately 6 m
(19.7 ft) are delivered in various components and
must be assembled on site. The main parts are:
hydraulic bowls section - various line shafts and
column pipes - headstock and thrust bearing.
To install the pump in the Can, clamps for the column
pipes are delivered with the pump.
1) Mount the first rising main column pipe [1350.3]
and line shaft to the already assembled hydraulic
section.
1350.3
Page 15 of 52
WUC USER INSTRUCTIONS ENGLISH - 07/14
2) Mount a clamp to the column pipe. The clamp
has lifting lugs, which allow to use a crane for
lowering this assembly into the pit (see picture).
clamp
3) Connect the next line shaft (refer to section 6,
Maintenance) and put on the next rising main
column pipes [1350.2] (see picture) by using a
second clamp.
4) Now the assembly consists of the hydraulic
section and two column sections. This assembly
is taken by a crane using the second clamp.
5) Take off the first clamp and lowering down the
assembly until the clamp is supported by the
wooden frame (see picture).
second clamp
1350.2
Repeat step 1 to 5 until the pump is completely
assembled.
Page 16 of 52
Loading...
+ 36 hidden pages
You need points to download manuals.
1 point = 1 manual.
You can buy points or you can get point for every manual you upload.