KSB Vitaprime Operating Manual

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Hygienic Pump
Vitaprime
Hygienic Side Channel Pump for the Highest Requirements on Cleanability
Installation/Operating Manual
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Installation/Operating Manual Vitaprime
Original operating manual
All rights reserved. The contents provided herein must neither be distributed, copied, reproduced, edited or processed for any other purpose, nor otherwise transmitted, published or made available to a third party without the manufacturer's express written consent.
Subject to technical modification without prior notice.
© KSB SE & Co. KGaA, Frankenthal 13/08/2018
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Contents
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Contents
Glossary .................................................................................................................................................. 5
1 General.................................................................................................................................................... 6
1.1 Principles ...........................................................................................................................................................6
1.2 Installation of partly completed machinery....................................................................................................6
1.3 Target group.....................................................................................................................................................6
1.4 Other applicable documents............................................................................................................................6
1.5 Symbols .............................................................................................................................................................6
1.6 Key to safety symbols/markings.......................................................................................................................7
2 Safety...................................................................................................................................................... 8
2.1 General..............................................................................................................................................................8
2.2 Intended use .....................................................................................................................................................8
2.3 Personnel qualification and training...............................................................................................................8
2.4 Consequences and risks caused by non-compliance with this manual .........................................................9
2.5 Safety awareness ..............................................................................................................................................9
2.6 Safety information for the operator/user.......................................................................................................9
2.7 Safety information for maintenance, inspection and installation ................................................................9
2.8 Unauthorised modes of operation................................................................................................................10
2.9 Explosion protection ......................................................................................................................................10
2.9.1 Marking ..............................................................................................................................................10
2.9.2 Temperature limits.............................................................................................................................10
2.9.3 Monitoring equipment......................................................................................................................11
2.9.4 Operating limits .................................................................................................................................11
3 Transport/Temporary Storage/Disposal............................................................................................. 12
3.1 Checking the condition upon delivery..........................................................................................................12
3.2 Transport.........................................................................................................................................................12
3.3 Storage/preservation......................................................................................................................................12
3.4 Return to supplier...........................................................................................................................................13
3.5 Disposal ...........................................................................................................................................................13
4 Description of the Pump (Set)............................................................................................................. 14
4.1 General description ........................................................................................................................................14
4.2 Designation.....................................................................................................................................................14
4.3 Name plate......................................................................................................................................................16
4.4 Design details..................................................................................................................................................17
4.5 Configuration and function...........................................................................................................................19
4.6 Noise characteristics .......................................................................................................................................19
4.7 Scope of supply...............................................................................................................................................20
4.8 Dimensions and weights ................................................................................................................................20
5 Installation at Site................................................................................................................................ 21
5.1 Checks to be carried out prior to installation...............................................................................................21
5.2 Installing the pump set ..................................................................................................................................21
5.3 Piping ..............................................................................................................................................................21
5.3.1 Connecting the piping.......................................................................................................................21
5.3.2 Permissible forces and moments at the pump nozzles....................................................................23
5.3.3 Auxiliary connections.........................................................................................................................23
5.4 Enclosure/insulation .......................................................................................................................................23
5.5 Electrical system..............................................................................................................................................24
5.5.1 Operation on a frequency inverter...................................................................................................24
5.6 Electrical connection ......................................................................................................................................24
5.6.1 Setting the time relay........................................................................................................................25
5.6.2 Connecting the motor .......................................................................................................................25
5.6.3 Earthing..............................................................................................................................................25
5.7 Checking the direction of rotation................................................................................................................26
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6 Commissioning/Start-up/Shutdown................................................................................................... 27
6.1 Commissioning/Start-up.................................................................................................................................27
6.1.1 Prerequisites for commissioning/start-up .........................................................................................27
6.1.2 Filling in lubricants.............................................................................................................................27
6.1.3 Priming and venting the pump.........................................................................................................27
6.1.4 Start-up...............................................................................................................................................28
6.1.5 Checking the shaft seal......................................................................................................................29
6.1.6 Shutdown ...........................................................................................................................................30
6.1.7 Seal supply system..............................................................................................................................30
6.2 Operating limits..............................................................................................................................................33
6.2.1 Ambient temperature........................................................................................................................33
6.2.2 Frequency of starts.............................................................................................................................33
6.2.3 Cleaning in place (CIP).......................................................................................................................34
6.2.4 Steaming in place (SIP) ......................................................................................................................34
6.2.5 Fluid handled .....................................................................................................................................35
6.3 Shutdown/storage/preservation ....................................................................................................................36
6.3.1 Measures to be taken for shutdown ................................................................................................36
6.4 Returning to service .......................................................................................................................................37
7 Servicing/Maintenance........................................................................................................................ 38
7.1 Safety regulations...........................................................................................................................................38
7.2 Servicing/Inspection........................................................................................................................................39
7.2.1 Supervision of operation...................................................................................................................39
7.2.2 Inspection work..................................................................................................................................41
7.2.3 Lubrication and lubricant change of rolling element bearings ......................................................42
7.3 Drainage/cleaning ..........................................................................................................................................43
7.4 Dismantling the pump set..............................................................................................................................43
7.4.1 General information/Safety regulations...........................................................................................43
7.4.2 Preparing the pump set.....................................................................................................................44
7.4.3 Removing the complete pump set from the piping ........................................................................44
7.4.4 Removing the pump casing and impeller.........................................................................................44
7.4.5 Removing the mechanical seal..........................................................................................................46
7.4.6 Dismantling the bearing assembly....................................................................................................48
7.5 Reassembling the pump set...........................................................................................................................49
7.5.1 General information/Safety regulations...........................................................................................49
7.5.2 Adjusting the clearances ...................................................................................................................50
7.5.3 Fitting the bearing assembly.............................................................................................................50
7.5.4 Installing the mechanical seal ...........................................................................................................51
7.5.5 Fitting the impeller and the pump casing........................................................................................53
7.6 Spare parts stock.............................................................................................................................................55
7.6.1 Ordering spare parts..........................................................................................................................55
7.6.2 Recommended spare parts stock for 2 years' operation to DIN24296 ..........................................55
8 Trouble-shooting.................................................................................................................................. 56
9 Related Documents.............................................................................................................................. 57
9.1 General assembly drawing with list of components (single-stage pumps).................................................57
9.1.1 Pump size 40-146, motor size 90.......................................................................................................57
9.1.2 Pump size 50-164, motor size 132.....................................................................................................58
9.1.3 Pump size 60/65-200, motor size 160................................................................................................59
9.1.4 Pump size 80-240, motor size 160.....................................................................................................60
9.2 General assembly drawing with list of components (two-stage pumps)....................................................61
9.2.1 Pump size 42-146, motor size 112.....................................................................................................61
9.2.2 Pump size 52-164, motor size 132.....................................................................................................62
10 EU Declaration of Conformity............................................................................................................. 63
11 Certificate of Decontamination........................................................................................................... 64
Index ..................................................................................................................................................... 65
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Glossary
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Glossary
Certificate of decontamination
A certificate of decontamination is enclosed by the customer when returning the product to the manufacturer to certify that the product has been properly drained to eliminate any environmental and health hazards arising from components in contact with the fluid handled.
CIP (cleaning in place)
Procedure during which the inside of the pump is cleaned with a cleaning agent. The pump does not need to be dismantled.
Discharge line
The pipeline which is connected to the discharge nozzle
Hydraulic system
The part of the pump in which the kinetic energy is converted into pressure energy
IE3
Efficiency class to IEC60034-30: 3=Premium Efficiency (IE = International Efficiency)
Pool of pumps
Customers/operators’ pumps which are purchased and stored regardless of their later use.
Pump
Machine without drive, additional components or accessories
Pump set
Complete pump set consisting of pump, drive, additional components and accessories
Self-priming ability
Ability of a filled pump to evacuate a suction line, i.e. to self-prime from an unfilled suction line.
SIP (steaming in place)
Procedure during which the inside of the pump is sterilised with steam. The pump does not need to be dismantled.
Suction lift line/suction head line
The pipeline which is connected to the suction nozzle
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1 General
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1 General
1.1 Principles
This operating manual is supplied as an integral part of the type series and variants indicated on the front cover.
The manual describes the proper and safe use of this equipment in all phases of operation.
The name plate indicates the type series and size, the main operating data, the order number and the order item number. The order number and order item number clearly identify the pump set and serve as identification for all further business processes.
In the event of damage, immediately contact your nearest KSB Service centre to maintain the right to claim under warranty.
1.2 Installation of partly completed machinery
To install partly completed machinery supplied by KSB refer to the sub-sections under Servicing/Maintenance.
1.3 Target group
This operating manual is aimed at the target group of trained and qualified specialist technical personnel. (ðSection2.3,Page8)
1.4 Other applicable documents
Table1: Overview of other applicable documents
Document Contents
Data sheet Description of the technical data of the pump (set) General arrangement drawing/
outline drawing
Description of mating and installation dimensions
for the pump (set), weights Drawing of auxiliary connections Description of auxiliary connections Hydraulic characteristic curve Characteristic curves showing head, NPSH
required, efficiency and power input General assembly drawing
1)
Sectional drawing of the pump Sub-supplier product literature1)Operating manuals and other product literature
describing accessories and integrated machinery
components Spare parts lists
1)
Description of spare parts Piping layout
1)
Description of auxiliary piping List of components
1)
Description of all pump components Drawing for assembly
1)
Sectional drawing of the installed shaft seal
For accessories and/or integrated machinery components observe the relevant manufacturer's product literature.
1.5 Symbols
Table2: Symbols used in this manual
Symbol Description
Conditions which need to be fulfilled before proceeding with the
step-by-step instructions
Safety instructions
Result of an action
Cross-references
1) If agreed upon in scope of supply
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Symbol Description
1.
2.
Step-by-step instructions
Note Recommendations and important information on how to handle the product
1.6 Key to safety symbols/markings
Table3: Definition of safety symbols/markings
Symbol Description
!
DANGER
DANGER This signal word indicates a high-risk hazard which, if not avoided, will result in death or serious injury.
!
WARNING
WARNING This signal word indicates a medium-risk hazard which, if not avoided, could result in death or serious injury.
CAUTION
CAUTION This signal word indicates a hazard which, if not avoided, could result in damage to the machine and its functions.
Explosion protection This symbol identifies information about avoiding explosions in potentially explosive atmospheres in accordance with EU Directive 2014/34/EU (ATEX).
General hazard In conjunction with one of the signal words this symbol indicates a hazard which will or could result in death or serious injury.
Electrical hazard In conjunction with one of the signal words this symbol indicates a hazard involving electrical voltage and identifies information about protection against electrical voltage.
Machine damage In conjunction with the signal word CAUTION this symbol indicates a hazard for the machine and its functions.
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2 Safety
!
DANGER
All the information contained in this section refers to hazardous situations. In addition to the present general safety information the action-related safety
information given in the other sections must be observed.
2.1 General
This operating manual contains general installation, operating and maintenance instructions that must be observed to ensure safe operation of the system and prevent personal injury and damage to property.
The safety information in all sections of this manual must be complied with. The operating manual must be read and understood by the responsible specialist
personnel/operators prior to installation and commissioning. The contents of this operating manual must be available to the specialist personnel
at the site at all times. Information attached directly to the product must always be complied with and kept
in a perfectly legible condition at all times. This applies to, for example:
Arrow indicating the direction of rotationMarkings for connectionsName plate
The operator is responsible for ensuring compliance with all local regulations not taken into account in this operating manual.
2.2 Intended use
The pump (set) must only be operated in the fields of application and within the
use limits specified in the other applicable documents. (ðSection1.4,Page6)
Only operate pumps/pump sets which are in perfect technical condition.Do not operate the pump (set) in partially assembled condition.Only use the pump to handle the fluids described in the data sheet or product
literature of the pump model or variant.
Never operate the pump without the fluid to be handled.Observe the minimum flow rates indicated in the data sheet or product literature
(to prevent overheating, bearing damage, etc).
Observe the minimum flow rate and maximum flow rate indicated in the data
sheet or product literature (to prevent overheating, mechanical seal damage, cavitation damage, bearing damage, etc).
Do not throttle the flow rate on the suction side of the pump (to prevent
cavitation damage).
Consult the manufacturer about any use or mode of operation not described in
the data sheet or product literature.
2.3 Personnel qualification and training
All personnel involved must be fully qualified to transport, install, operate, maintain and inspect the machinery this manual refers to.
The responsibilities, competence and supervision of all personnel involved in transport, installation, operation, maintenance and inspection must be clearly defined by the operator.
Deficits in knowledge must be rectified by means of training and instruction provided by sufficiently trained specialist personnel. If required, the operator can commission the manufacturer/supplier to train the personnel.
Training on the pump (set) must always be supervised by technical specialist personnel.
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2.4 Consequences and risks caused by non-compliance with this manual
Non-compliance with these operating instructions will lead to forfeiture of
warranty cover and of any and all rights to claims for damages.
Non-compliance can, for example, have the following consequences:
– Hazards to persons due to electrical, thermal, mechanical and chemical
effects and explosions – Failure of important product functions – Failure of prescribed maintenance and servicing practices – Hazard to the environment due to leakage of hazardous substances
2.5 Safety awareness
In addition to the safety information contained in this manual and the intended use, the following safety regulations shall be complied with:
Accident prevention, health regulations and safety regulationsExplosion protection regulationsSafety regulations for handling hazardous substancesApplicable standards, directives and laws
2.6 Safety information for the operator/user
Fit protective equipment (e.g. contact guards) supplied by the operator for hot,
cold or moving parts, and check that the equipment functions properly.
Do not remove any protective equipment (e.g. contact guards) during operation.Provide the personnel with protective equipment and make sure it is used.Contain leakages (e.g. at the shaft seal) of hazardous fluids handled (e.g.
explosive, toxic, hot) so as to avoid any danger to persons and the environment. Adhere to all relevant laws.
Eliminate all electrical hazards. (In this respect refer to the applicable national
safety regulations and/or regulations issued by the local energy supply companies.)
If shutting down the pump does not increase potential risk, fit an emergency-
stop control device in the immediate vicinity of the pump (set) during pump set installation.
2.7 Safety information for maintenance, inspection and installation
Modifications or alterations of the pump (set) are only permitted with the
manufacturer's prior consent.
Use only original spare parts or parts/components authorised by the
manufacturer. The use of other parts/components can invalidate any liability of the manufacturer for resulting damage.
The operator ensures that maintenance, inspection and installation is performed
by authorised, qualified specialist personnel who are thoroughly familiar with the manual.
Only carry out work on the pump (set) during standstill of the pump.Only perform work on the pump set when it has been disconnected from the
power supply (de-energised).
The pump (set) must have cooled down to ambient temperature.Pump pressure must have been released and the pump must have been drained.
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When taking the pump set out of service always adhere to the procedure
described in the manual. (ðSection6.1.6,Page30) (ðSection6.3,Page36)
Decontaminate pumps which handle fluids posing a health hazard.As soon as the work has been completed, re-install and re-activate any safety-
relevant devices and protective devices. Before returning the product to service, observe all instructions on commissioning. (ðSection6.1,Page27)
2.8 Unauthorised modes of operation
Never operate the pump (set) outside the limits stated in the data sheet and in this manual.
The warranty relating to the operating reliability and safety of the supplied pump (set) is only valid if the equipment is used in accordance with its intended use. (ðSection2.2,Page8)
2.9 Explosion protection
!
DANGER
Always observe the information on explosion protection given in this section when operating the product in potentially explosive atmospheres.
Only pumps/pump sets marked as explosion-proof and identified as such in the data sheet may be used in potentially explosive atmospheres.
Special conditions apply to the operation of explosion-proof pump sets to EU Directive 2014/34/EU (ATEX). Especially adhere to the sections in this manual marked with the symbol opposite and the following sections, (ðSection2.9.1,Page10) to (ðSection2.9.4,Page11) The explosion-proof status of the pump set is only assured if the pump set is used in accordance with its intended use. Never operate the pump set outside the limits stated in the data sheet and on the name plate. Prevent impermissible modes of operation at all times.
2.9.1 Marking
Pump The marking on the pump refers to the pump part only.
Example of such marking: II 2 G c TX (EN 13463-1) or II 2G Ex h IIC T5-T1 Gb (ISO 80079-36)
Refer to the individual Temperature Limits table for the temperatures permitted for the individual pump variants.
The pump complies with the requirements of type of protection constructional safety "c" to ISO80079-37.
Shaft coupling An EC manufacturer's declaration is required for the shaft coupling; the shaft
coupling must be marked accordingly.
Motor The motor must be considered separately.
2.9.2 Temperature limits
In normal pump operation, the highest temperatures are to be expected at the surface of the pump casing and at the shaft seal. The surface temperature at the pump casing corresponds to the temperature of the fluid handled. If the pump is heated, the operator of the system is responsible for observing the specified temperature class and fluid temperature (operating temperature). The table below lists the temperature classes and the resulting theoretical temperature limits of the fluid handled. (A possible temperature rise in the shaft seal area has already been taken into account).
The temperature class specifies the maximum permissible temperature at the surface of the pump set during operation. For the permissible operating temperature of the pump in question refer to the data sheet.
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Table4: Temperature limits
Temperature class to EN 13463-1 Maximum permissible fluid
temperature
T1 Pump temperature limit T2 Pump temperature limit T3 100 °C T4 90 °C
If the pump is to be operated at a higher temperature, if there is no data sheet or if the pump is part of a pool of pumps, contact KSB for the maximum permissible operating temperature.
Motor supplied by the
operator
If a pump is supplied without motor (as part of a pool of pumps), the motor specified in the pump data sheet must meet the following conditions:
The permissible temperature limits at the motor flange and motor shaft must be
higher than the temperatures generated by the pump.
Contact the manufacturer for the actual pump temperatures.
2.9.3 Monitoring equipment
The pump (set) must only be operated within the limits specified in the data sheet and on the name plate. If the system operator cannot warrant compliance with these operating limits, appropriate monitoring devices must be used. Check whether monitoring equipment is required to ensure that the pump set functions properly.
Contact KSB for further information about monitoring equipment.
2.9.4 Operating limits
The minimum flows indicated in (ðSection6.2.5.1,Page35) refer to water and water-like fluids handled. Longer operating periods with these fluids and at the flow rates indicated will not cause an additional increase in the temperatures at the pump surface. However, if the physical properties of the fluids handled are different from water, it is essential to check whether an additional heat build-up may occur and if the minimum flow rate must therefore be increased. The calculation formula in (ðSection6.2.5.1,Page35) can be used to check whether additional heat build-up may lead to a dangerous temperature increase at the pump surface.
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3 Transport/Temporary Storage/Disposal
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3 Transport/Temporary Storage/Disposal
3.1 Checking the condition upon delivery
1. On transfer of goods, check each packaging unit for damage.
2. In the event of in-transit damage, assess the exact damage, document it and notify KSB or the supplying dealer and the insurer about the damage in writing immediately.
3.2 Transport
DANGER
The pump (set) could slip out of the suspension arrangement
Danger to life from falling parts!
Always transport the pump (set) in the specified position.Never attach the suspension arrangement to the free shaft end or the motor
eyebolt.
Observe the information about weights, centre of gravity and fastening points.Observe the applicable local accident prevention regulations.Use suitable, permitted lifting accessories, e.g. self-tightening lifting tongs.
To transport the pump/pump set suspend it from the lifting tackle as shown.
Fig.1: Transporting the pump set
3.3 Storage/preservation
If commissioning is to take place some time after delivery, we recommend that the following measures be taken for pump (set) storage.
CAUTION
Damage during storage due to humidity, dirt or vermin
Corrosion/contamination of the pump (set)!
For outdoor storage cover the pump (set) or the packaged pump (set) and
accessories with waterproof material.
CAUTION
Wet, contaminated or damaged openings and connections
Leakage or damage to the pump!
Clean and cover pump openings and connections as required prior to putting
the pump into storage.
Store the pump (set) in a dry, protected room where the atmospheric humidity is as constant as possible.
Rotate the shaft by hand once a month, e.g. via the motor fan.
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If properly stored indoors, the pump set is protected for a maximum of 12 months. New pumps/pump sets are supplied by our factory duly prepared for storage.
For storing a pump (set) which has already been operated, the shutdown measures must be adhered to. (ðSection6.3.1,Page36)
3.4 Return to supplier
1. Drain the pump as per operating instructions. (ðSection7.3,Page43)
2. Flush and clean the pump, particularly if it has been used for handling noxious, explosive, hot or other hazardous fluids.
3. If the pump has handled fluids whose residues could lead to corrosion damage in the presence of atmospheric humidity or could ignite upon contact with oxygen also neutralise the pump and blow through with anhydrous inert gas to ensure drying.
4. Always complete and enclose a certificate of decontamination when returning the pump. Indicate any safety measures and decontamination measures taken. (ðSection11,Page64)
NOTE
If required, a blank certificate of decontamination can be downloaded from the following web site: www.ksb.com/certificate_of_decontamination
3.5 Disposal
WARNING
Fluids handled, consumables and supplies which are hot and/or pose a health hazard
Hazard to persons and the environment!
Collect and properly dispose of flushing fluid and any fluid residues.Wear safety clothing and a protective mask if required.Observe all legal regulations on the disposal of fluids posing a health hazard.
1. Dismantle the pump (set). Collect greases and other lubricants during dismantling.
2. Separate and sort the pump materials, e.g. by:
- Metals
- Plastics
- Electronic waste
- Greases and other lubricants
3. Dispose of materials in accordance with local regulations or in another controlled manner.
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4 Description of the Pump (Set)
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4 Description of the Pump (Set)
4.1 General description
Hygienic pump
Pump for handling fluids which are not chemically aggressive, are free from solids and do not require hermetic sealing.
Hygienic side channel pump for the food and beverage industry and the pharmaceutical industry
All pumps of this type series are fitted with standardised mechanical seals to EN12756. This ensures reliable operation and interchangeability.
When different standardised mechanical seals are used, verify the axial length of the seal. Type and material of the mechanical seal are specifically selected to match the nature and composition of the fluid to be handled.
NOTE
Before using the pump for any fluids different from those originally specified, check that the mechanical seals and joint rings are suitable for that fluid. If certified seal types and/or materials are used, make sure that the replacement seals also meet the certification requirements.
Design
Seal typeT: internal single mechanical seal (standard design)Seal type VT: internal single mechanical seal with flushing system (quench,
unpressurised)
Seal typeQ: external double mechanical seal with flushing system, with
pressurised barrier fluid
Seal typeH: internal single mechanical seal, enclosed spring, balancedSeal type VH: internal single mechanical seal with flushing system (quench,
unpressurised), enclosed spring, balanced
4.2 Designation
Table5: Designation example
Position
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31
V P 8 0 - 2 4 0 - 1 1 0 4 0 4 K B Q T 8 2 M E C C O O A
See name plate and data sheet See data
sheet
Table6: Designation key
Position Code Description
1-4 Pump type
VP Vitaprime
5-13 Size, e.g.
80 Nominal nozzle diameter [mm] 240 Nominal impeller diameter [mm] 11 Load range
14-16 Motor rating PN [kW]
007 0,70 040 4,00
185 18,50 17 Number of motor poles 18 Scope of supply
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Position Code Description
18 K Ball feet
M Motor foot
T Round base feet
V Trolley 19-20 Shaft seal type
B Single mechanical seal, dead-end arrangement, without flushing
BQ Single mechanical seal, dead-end arrangement, external flushing
(quench)
DB Double mechanical seal in back-to-back arrangement 21-23 Seal code, single mechanical seal
T00 BGEGG
T18 U2U2VGG
T19 U2U2EGG
T64 U2Q1EGG
T66 Q1Q1M3GG
T68 U2Q1VGG
T69 BQ1M3GG
T80 BQ1VGG
T81 Q1Q1VGG
T82 BQ1EGG
T83 Q1Q1EGG
T84 Q1U2EGG
T85 Q1U2VGG
Seal code, double mechanical seal in back-to-back arrangement
Q70 BGEGG
BGEGG
Q71 BU2EGG
BGEGG
Q72 U2U2EGG
BU2EGG
Q74 U2U2VGG
BU2VGG
Q78 U2U2VGG
U2U2EGG
Q79 U2U2M3GG
BU2EGG
24 Pipe connection
A Flange APV
B Threaded connection DIN 11864-1A
C Flange DIN 11864-2A
D Clamped connection DIN 11864-3A
E Threaded connection DIN 11853
F Threaded connection RJT
G Flange Varivent
I Threaded connection ISO 2853 (IDF)
L Flange EN 1092-1
M Threaded connection DIN 11851 (hygienic pipe union)
S Threaded connection SMS
T Clamped connection DIN 32676-A
U Clamped connection DIN32676-C (Tri-Clamp)
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Position Code Description
24 V Clamped connection ISO 2852
Z Flange ANSI B16.5 Class 150 25 O-ring material (casing/impeller)
E EPDM
F FFKM (Kaflon)
K FFKM (Kalrez)
M FEP (encapsulated)
P PTFE
V FPM 26 Pump casing material
C Stainless steel 1.4409 27 Impeller material
C Stainless steel 1.4409 28 Motor shroud
S With shroud
O Without shroud 29 Design
2)
Standard
X Non-standard (BT3D, BT3), including ATEX 30 Drain
O No drain
P Casing drain via pipeline
V Casing drain via valve
D Casing drain with plug 31 Product generation
A Vitaprime
4.3 Name plate
VP 80-240-11040KBQT82ME
E-Nr
Nr
H 20 m
Q 10 m
3
/h
Jahr 2016
n 1450 1/min
1
2
4
3
6
7
5
Johann-Klein-Straße 9
Deutschland
67227 Frankenthal
KSB SE & Co. KGaA
Fig.2: Name plate Vitaprime (example)
1 Type series, size and version 2 KSB order number 3 Manufacturer's No. 4 Flow rate 5 Head 6 Speed 7 Year of construction
2) Blank
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Vitaprime
4.4 Design details
Design
Standard design with materials to Regulation (EC) No.1935/2004Design to ATEX
Design
Side channel pumpHorizontal installationOne or two stagesSelf-priming
Pump casing
Casing with transfer passages
Impeller type
Open star impeller
Bearings
Grease-packed deep groove ball bearing
Shaft seal
Single mechanical seal to EN12756
– Seal typeT3): pump-end seal with non-encapsulated spring surrounded by
fluid handled, uni-directional
Double mechanical seal to EN12756
– Seal type Q: back-to-back arrangement (pressurised barrier fluid)
Drive
Efficiency class IE3 to IEC60034-30
Standard design:
KSB surface-cooled IEC three-phase current squirrel-cage motor50Hz winding, 220-240V/ 380-420V ≤2.20kW50Hz winding, 380-420V/ 660-725V ≥3.00kW60Hz winding, 440-480V ≤2.60kW60Hz winding, 440-480V ≥3.60kWType of construction IMV1 ≤4.00kWType of construction IMV15 ≥5.50kWEnclosure IP55Duty cycle: continuous duty S1Thermal class F with temperature sensor, 3 PTC thermistors
Explosion-proof version:
KSB surface-cooled IEC three-phase current squirrel-cage motor50Hz winding, 220-240V/ 380-420V ≤1.85kW50Hz winding, 380-420V/ 660-725V ≥2.50kWType of construction IMV1 ≤3.30kWType of construction IMV15 ≥4.60kWEnclosure IP55 or IP54
3) Hygienic design
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Vitaprime
Duty cycle: continuous duty S1Type of protection EEx e IITemperature class T3
Automation
Automation options:
PumpDrive
Connections
Axial suction nozzle, tangential discharge nozzle
Types of connection:
Threaded connection to DIN11851 (hygienic pipe union)Threaded connection to DIN11853Threaded connection to DIN11864-1-GS-AThreaded connection to SMS standardThreaded connection to ISO2853 (IDF)Threaded connection to RJT standardClamped connection to DIN32676-C (Tri-Clamp/Tri-Clover fitting)Clamped connection to DIN11864-3-NKS-AClamped connection to DIN32676-AClamped connection to ISO2852Flange to EN1092-1Flange to DIN11864-2-NF-AFlange to ANSI B16.5 Class 150APV flangeVarivent flangeOther connection types on request
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4.5 Configuration and function
Fig.3: Sectional drawing of Vitaprime
1 Suction nozzle 2 Inlet casing 3 Impeller casing 4 Discharge nozzle 5 Impeller 6 Shaft seal 7 Rolling element bearing 8 Drive shaft 9 Side channel 10 Bearing assembly 11 Motor
Design The pump is designed with an axial fluid inlet and a radial outlet. The hydraulic
system is rigidly connected to the motor via a stub shaft.
Function The fluid enters the inlet casing (2) of the pump via the suction nozzle (1) and then
passes through an opening into the impeller casing (3). The rotating impeller (5) conveys the fluid into the side channel (9), so that a liquid ring is formed in the casing. Owing to the conical geometry of the side channel, i.e. a change in volume (positive displacement effect), the fluid is drawn from the inlet casing (2) and transferred to the discharge nozzle (4), where it leaves the pump. The drive shaft (8) enters the casing through an opening at the rear. The shaft passage is sealed with a dynamic shaft seal (6). The drive shaft runs in a rolling element bearing (7), which is supported by a bearing assembly (10). The motor shaft is inserted into the drive shaft (stub shaft). The motor (11) is bolted to the pump casing. The pump is self-priming once the inlet casing has been filled.
Sealing The pump is sealed by a mechanical seal.
Various seal designs can be used.
4.6 Noise characteristics
Table7: Surface sound pressure level L
pA
4)
Size Noise characteristic
[dB]
Vitaprime 40-146 < 80 Vitaprime 42-146 81 - 85 Vitaprime 50-164 81 - 85 Vitaprime 52-164 86 - 90
4) Measured at a distance of 1 metre, 1.6 metres above the installation surface
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Vitaprime
Size Noise characteristic
[dB]
Vitaprime 60-200 86 - 90 Vitaprime 65-200 86 - 90 Vitaprime 80-240 86 - 90
4.7 Scope of supply
Depending on the model, the following items are included in the scope of supply:
PumpDriveFrequency inverterMotor shroudPump foot or foot base (e.g. 3-point ball feet)Trolley with switch and power cableNoise reduction valve
4.8 Dimensions and weights
For dimensions and weights please refer to the general arrangement drawing/outline drawing of the pump/pump set.
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5 Installation at Site
5.1 Checks to be carried out prior to installation
Place of installation
WARNING
Installation on mounting surface which is unsecured and cannot support the load
Personal injury and damage to property!
Use a concrete of compressive strength class C12/15 which meets the
requirements of exposure class XC1 to EN206-1.
The mounting surface must be set, flat, and level.Observe the weights indicated.
1. Check the structural requirements. All structural work required must have been prepared in accordance with the dimensions stated in the outline drawing/general arrangement drawing.
5.2 Installing the pump set
Always install the pump set in a horizontal position.
DANGER
Excessive temperatures due to improper installation
Explosion hazard!
Install the pump in a horizontal position to ensure self-venting of the pump.
CAUTION
Ingress of leakage into the motor
Damage to the pump!
Never install the pump set with the "motor below".
1. Align the pump set with the help of a spirit level placed on the discharge nozzle.
5.3 Piping
5.3.1 Connecting the piping
DANGER
Impermissible loads acting on the pump nozzles
Danger to life from leakage of hot, toxic, corrosive or flammable fluids!
Do not use the pump as an anchorage point for the piping.Anchor the pipes in close proximity to the pump and connect them properly
without transmitting any stresses or strains.
Take appropriate measures to compensate for thermal expansion of the piping.
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CAUTION
Incorrect earthing during welding work at the piping
Destruction of rolling element bearings (pitting effect)!
Never earth the electric welding equipment on the pump or baseplate.Prevent current flowing through the rolling element bearings.
NOTE
Installing check and shut-off elements in the system is recommended, depending on the type of plant and pump. However, such elements must not obstruct proper drainage or hinder disassembly of the pump.
CAUTION
When handling gaseous fluids or fluids which tend to froth, the pump will not be self-priming.
Pump is running, but does not deliver!
Install a check valve in the suction line.
ü Suction lift lines have been laid with a rising slope, suction head lines with a
downward slope towards the pump.
ü A flow stabilisation section having a length equivalent to at least twice the
diameter of the suction flange has been provided upstream of the suction flange.
ü The nominal diameters of the pipes are equal to or greater than the nominal
diameters of the pump nozzles.
ü Adapters to larger nominal diameters are designed with a diffuser angle of
approx. 8° to avoid excessive pressure losses.
ü The pipelines have been anchored in close proximity to the pump and connected
without transmitting any stresses or strains.
1. Thoroughly clean, flush and blow through all vessels, pipelines and connections (especially of new installations).
2. Before installing the pump in the piping, remove the flange covers on the suction and discharge nozzles of the pump.
CAUTION
Welding beads, scale and other impurities in the piping
Damage to the pump!
Remove any impurities from the piping.If necessary, install a filter.Observe the information in (ðSection7.2.2.2,Page41) .
NOTE
Use a filter with laid-in wire mesh (mesh width 0.5mm, wire diameter 0.25mm) of corrosion-resistant material. Use a filter with a filter area three times the cross-section of the piping. Conical filters have proved suitable.
3. Connect the pump nozzles to the piping.
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CAUTION
Aggressive flushing liquid and pickling agent
Damage to the pump!
Match the cleaning operation mode and duration of flushing and pickling to
the casing materials and seal materials used.
5.3.2 Permissible forces and moments at the pump nozzles
No piping-induced forces and moments (from warped pipelines or thermal expansion, for example) must act on the pump.
5.3.3 Auxiliary connections
DANGER
Risk of potentially explosive atmosphere by mixing of incompatible fluids in the auxiliary piping
Risk of burns! Explosion hazard!
Make sure that the barrier fluid or quench liquid are compatible with the fluid
handled.
CAUTION
Failure to use or incorrect use of auxiliary connections (flushing liquid)
Malfunction of the pump!
Use and install any auxiliary connections in such a way that a proper flow is
ensured.
If a shaft seal with flush connection is used, fit the flushing liquid reservoir in the immediate vicinity of the pump set approximately 1metre above the pump centreline. Fluid circulation is ensured by thermosyphon effect or forced circulation.
When mounting the pipe unions comply with the instructions provided by the pipe union manufacturer.
NOTE
The flushing liquid feed line must be laid with a continuously rising slope towards the flushing liquid reservoir.
Make sure that the flushing liquid (if any) circulates properly also before starting up and after shutting down the pump (until the pump set comes to a complete stop).
5.4 Enclosure/insulation
WARNING
The volute casing and casing/discharge cover take on the same temperature as the fluid handled
Risk of burns!
Insulate the volute casing.Fit protective equipment.
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CAUTION
Heat build-up in the bearing bracket
Damage to the bearing!
Never insulate the bearing bracket, bearing bracket lantern and casing cover.
5.5 Electrical system
5.5.1 Operation on a frequency inverter
The pump set is suitable for operation on a frequency inverter as per IEC60034-17.
Selection When selecting a frequency inverter, check the following details:
Data provided by the manufacturerElectrical data of the pump set, particularly the rated currentOnly voltage source inverters (VSI) with pulse width modulation (PWM) and
carrier frequencies between 1 and 16kHz are suitable.
Setting Observe the following instructions for setting a frequency inverter:
Set the current limit to max. 1.2 times the rated current. The rated current is
indicated on the name plate.
Start-up Observe the following instructions for starting the frequency inverter:
Ensure short start ramps (maximum 5 seconds).Only start variable speed control after 2minutes at the earliest.
Pump start-up with long start ramps and low frequency may cause clogging.
Operation Observe the following limits during operation on a frequency inverter:
Only utilise up to 95% of the motor rating P2 indicated on the name plate. ▪ Frequency range 25 to 60Hz
Electromagnetic
compatibility
Operation on a frequency inverter produces interference emissions whose level varies depending on the inverter used (type, interference suppression, make). To prevent the drive system, consisting of a submersible motor and a frequency inverter, from exceeding any given limits always observe the EMC information provided by the inverter manufacturer. If the inverter manufacturer recommends a shielded power cable, make sure to use a submersible motor pump with shielded power cables.
Interference immunity The submersible motor pump generally meets interference immunity requirements.
For monitoring the sensors installed the operator must ensure sufficient interference immunity by appropriately selecting and laying the power cables in the plant. No modifications are required on the power/control cable of the submersible motor pump. Suitable analysing devices must be selected. To monitor the leakage sensor inside the motor using a special relay available from KSB is recommended.
5.6 Electrical connection
DANGER
Electrical connection work by unqualified personnel
Risk of fatal injury due to electric shock!
Always have the electrical connections installed by a trained and qualified
electrician.
Observe regulations IEC 60364 and, for explosion-proof models, EN60079.
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WARNING
Incorrect connection to the mains
Damage to the mains network, short circuit!
Observe the technical specifications of the local energy supply companies.
1. Check the available mains voltage against the data on the motor name plate.
2. Select an appropriate starting method.
NOTE
A motor protection device is recommended.
5.6.1 Setting the time relay
CAUTION
Switchover between star and delta on three-phase motors with star-delta starting takes too long.
Damage to the pump (set)!
Keep switch-over intervals between star and delta as short as possible.
Table8: Time relay settings for star-delta starting:
Motor rating Y time to be set
≤ 30 kW < 3 s
5.6.2 Connecting the motor
NOTE
In compliance with IEC 60034-8, three-phase motors are always wired for clockwise rotation (looking at the motor shaft stub).
The pump's direction of rotation is indicated by an arrow on the pump.
1. Match the motor's direction of rotation to that of the pump.
2. Observe the manufacturer's product literature supplied with the motor.
5.6.3 Earthing
DANGER
Electrostatic charging
Explosion hazard! Damage to the pump set!
Connect the PE conductor to the earthing terminal provided.Provide for potential equalisation between the pump set and foundation.
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5.7 Checking the direction of rotation
DANGER
Temperature increase resulting from contact between rotating and stationary components
Explosion hazard! Damage to the pump set!
Never check the direction of rotation by starting up the unfilled pump set.Separate the pump from the motor to check the direction of rotation.
WARNING
Hands inside the pump casing
Risk of injuries, damage to the pump!
Always disconnect the pump set from the power supply and secure it against
unintentional start-up before inserting your hands or other objects into the pump.
CAUTION
Incorrect direction of rotation with non-reversible mechanical seal
Damage to the mechanical seal and leakage!
Separate the pump from the motor to check the direction of rotation.
CAUTION
Drive and pump running in the wrong direction of rotation
Damage to the pump!
Refer to the arrow indicating the direction of rotation on the pump.Check the direction of rotation. If required, check the electrical connection and
correct the direction of rotation.
The correct direction of rotation of the motor and pump is clockwise (seen from the drive end).
1. Start the motor and stop it again immediately to determine the motor's direction of rotation.
2. Check the direction of rotation. The motor's direction of rotation must match the arrow indicating the direction of rotation on the pump.
3. If the motor is running in the wrong direction of rotation, check the electrical connection of the motor and switchgear, if any.
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6 Commissioning/Start-up/Shutdown
6.1 Commissioning/Start-up
6.1.1 Prerequisites for commissioning/start-up
Before commissioning/starting up the pump set, make sure that the following conditions are met:
The quality of the concrete foundation complies with the regulations.The pump set has been installed and aligned in accordance with the tolerances
specified.
The pump set has been properly connected to the power supply and is equipped
with all protection devices. (ðSection5.6,Page24)
The pump has been primed with the fluid to be handled. The pump has been
vented.
The direction of rotation has been checked. (ðSection5.7,Page26)All auxiliary connections required are connected and operational.The lubricants have been checked.The lock washers, if any, have been removed from the shaft groove.The pump (set) has been installed and connected as described in this manual.After prolonged shutdown of the pump (set), the activities required for returning
the equipment to service have been carried out. (ðSection6.4,Page37)
6.1.2 Filling in lubricants
Grease-lubricated bearings
The bearings have been packed with grease at the factory.
6.1.3 Priming and venting the pump
DANGER
Excessive temperatures due to dry running or excessive gas content in the fluid handled
Explosion hazard! Damage to the pump set!
Prime the pump as per operating instructions.
DANGER
Risk of potentially explosive atmosphere by mixing of incompatible fluids in the auxiliary piping
Risk of burns! Explosion hazard!
Make sure that the barrier fluid or quench liquid are compatible with the fluid
handled.
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DANGER
Risk of potentially explosive atmosphere inside the pump
Explosion hazard!
The pump internals in contact with the fluid to be handled, including the seal
chamber and auxiliary systems must be filled with the fluid to be handled at all times.
Provide sufficient inlet pressure.Provide an appropriate monitoring system.
CAUTION
Increased wear due to dry running
Damage to the pump set!
Never operate the pump set without liquid fill.Never close the shut-off element in the suction line and/or supply line during
pump operation.
1. Vent the pump and suction line and prime both with the fluid to be handled.
2. Fully open the shut-off element in the suction line.
3. Fully open all auxiliary feed lines (barrier fluid, flushing liquid, etc.), if any.
NOTE
For design-inherent reasons some unfilled volume in the hydraulic system cannot be excluded after the pump has been primed for commissioning/start-up. However, once the motor is started up the pumping effect will immediately fill this volume with the fluid handled.
6.1.4 Start-up
DANGER
Formation of a potentially explosive atmosphere inside the pump
Explosion hazard!
The fluid for priming the pump must not be combustible.When the fluid for priming the pump is taken from a potentially explosive
atmosphere, make sure that no potentially explosive atmosphere can enter the pump.
DANGER
Non-compliance with the permissible pressure and temperature limits if the pump is operated with the suction and/or discharge line closed.
Explosion hazard! Hot or toxic fluids escaping!
Never operate the pump with the shut-off elements in the suction line and/or
discharge line closed.
Only start up the pump set with the discharge-side shut-off element slightly or
fully open.
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DANGER
Excessive temperatures due to dry running or excessive gas content in the fluid handled
Explosion hazard! Damage to the pump set!
Never operate the pump set without liquid fill.Prime the pump as per operating instructions.Always operate the pump within the permissible operating range.
CAUTION
Abnormal noises, vibrations, temperatures or leakage
Damage to the pump!
Switch off the pump (set) immediately.Eliminate the causes before returning the pump set to service.
ü The system piping has been cleaned. ü The pump, suction line and inlet tank, if any, have been vented and primed with
the fluid to be handled.
ü The lines for priming and venting have been closed.
CAUTION
Start-up against open discharge line
Motor overload!
Make sure the motor has sufficient power reserves.Use a soft starter.Use speed control.
1. Fully open the shut-off element in the suction head/suction lift line.
2. Close or slightly open the shut-off element in the discharge line.
3. If a mechanical seal with flushing system is used, make sure that the flushing liquid circulates properly.
4. Start up the motor.
5. Immediately after the pump has reached full rotational speed, slowly open the shut-off element in the discharge line and adjust it to comply with the duty point.
6. When the operating temperature has been reached and/or if there is any leakage, check the clamping ring/screw connection between casing and casing cover. If required, re-tighten it.
6.1.5 Checking the shaft seal
Mechanical seal The mechanical seal only leaks slightly or invisibly (as vapour) during operation.
Mechanical seals are maintenance-free.
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6.1.6 Shutdown
CAUTION
Heat build-up inside the pump
Damage to the shaft seal!
Depending on the type of installation, the pump set requires sufficient after-
run time – with the heat source switched off – until the fluid handled has cooled down.
CAUTION
Backflow of fluid handled is not permitted
Motor or winding damage! Mechanical seal damage!
Close the shut-off elements.
ü The shut-off element in the suction line is and remains open.
1. Close the shut-off element in the discharge line.
2. Switch off the motor and make sure the pump set runs down smoothly to a standstill.
NOTE
If the discharge line is equipped with a non-return or check valve, the shut-off element may remain open provided that the system conditions and system regulations are considered and observed.
For prolonged shutdown periods:
1. Close the shut-off element in the suction line.
2. Close any auxiliary lines. If the fluid to be handled is fed in under vacuum, also supply the shaft seal with barrier fluid during standstill.
CAUTION
Risk of freezing during prolonged pump shutdown periods
Damage to the pump!
Drain the pump and the cooling/heating chambers (if any) or otherwise protect
them against freezing.
6.1.7 Seal supply system
6.1.7.1 Application
In order to function properly, the mechanical seals require a flushing liquid. The flushing liquid completely fills the space between the inboard and the outboard mechanical seal.
6.1.7.2 Requirements to be met by the seal supply system
Pipework routing
requirements
When routing pipework and flexible tubing, prevent any high points or ensure that high points can be vented separately to prevent dry running of the mechanical seal. The connecting pipes between the main pipe and the pump must be routed with a continuously rising slope to assure self-venting of the pipe and the mechanical seal, respectively.
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6.1.7.3 Types of seal supply systems
Which of the two types of seal supply systems is used depends on the mechanical seal:
6.1.7.3.1 Quench liquid
6.1.7.3.1.1 Applications
A quench liquid is used in the following cases:
Where a single mechanical seal without supportive measures would not work at
all or unsatisfactorily.
Where a double mechanical seal design with pressurised barrier fluid is not
required.
6.1.7.3.1.2 Quench liquid requirements
The quench liquid should preferably form a solution with the fluid handled and be environmentally compatible.
Typical quench liquids Water with a conductivity of 100 - 800 µS/cm
Water/glycol mixture
Glycerine
5)
The quench liquid should be supplied to the mechanical seals unpressurised (at atmospheric pressure), if possible. Positive pressures of up to 0.5 bar are acceptable.
The one-way quench supply should be adjusted to a constant flow ≥0.4l/min. Periodically check the quench liquid for contamination (replace quench liquid and
clean quench system if necessary).
6.1.7.3.1.3 Applications
For seal types T and H, operating mode BQ
6.1.7.3.2 Barrier fluid system
6.1.7.3.2.1 Applications
Barrier fluid systems serve to:
Dissipate friction heatPrevent the fluid handled from entering the sealing gap
6.1.7.3.2.2 Barrier fluid requirements
The barrier fluid should preferably form a solution with the fluid handled and be environmentally compatible. The barrier fluid should be monitored: Any ingress of the fluid handled can be identified at an early stage by the barrier fluid becoming turbid.
The temperature differences between the barrier fluid and the fluid handled must not exceed 5°C. A general minimum temperature of 0°C applies to the barrier fluid.
The barrier fluid system must be set to a pressure which exceeds the pressure inside the pump by approximately 0.5 to 1bar.
General rule: The maximum permissible pressure inside the barrier fluid system equals 10bar. Actual maximum permissible pressure depending on the material combination and shaft diameter:
5) Make sure the circulation line diameter is ≥¼".
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0
Pressure in flushing system [bar]
Shaft diameter [mm]
0
1
2
3
4
1
2
3
4
5
6
7
8
9
10
10
20 30 40 50
60 70 80
90 100
110
120 130
140 150
11
12
13
14
15
Fig.4: Application limits for mechanical seals6) 2900rpm
1 Hard-soft combination (steel/carbon) 2 Hard-soft combination (ceramic/
carbon)
3 Hard-soft combination (silicon
carbide/carbon; tungsten carbide/ carbon)
4 Hard-hard combination (silicon
carbide/silicon carbide; tungsten carbide/tungsten carbide)
The flow rate of the barrier fluid system depends on the shaft diameter, speed and fluid temperature.
Table9: Flow rate of the flushing liquid
Material combination of seal faces
Hard-soft combination Hard-hard combination
Pump speed 1450
[rpm]
2900
[rpm]
1450
[rpm]
2900
[rpm]
Mechanical seal diameter
[mm]
Flow rate flushing
liquid
[l/min]
Flow rate flushing
liquid
[l/min]
Flow rate flushing
liquid
[l/min]
Flow rate flushing
liquid
[l/min]
20 0,4-1,0 0,7-1,9 0,4-1,2 0,9-2,2 28 0,6-1,2 1,0-2,4 0,7-1,6 1,3-3,1 43 1,0-1,9 1,8-3,8 1,2-2,8 2,2-5,4 55 1,0-2,4 2,0-4,6 1,3-3,4 2,6-6,7
The lower flushing limit refers to a temperature of the fluid handled of 25°C and a barrier pressure of 1bar. The upper flushing limit refers to a temperature of the fluid handled of 100°C and a barrier pressure of 10bar. The flow rate of the flushing liquid must be adjusted to the actual conditions (pressure, temperature). The data refer to a temperature difference of 5°C between the inlet and outlet of the flushing liquid.
6.1.7.3.2.3 Applications
For seal type Q, operating mode DB
6) Valid for unbalanced mechanical seals flushed with clean water of 20°C.
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6.2 Operating limits
DANGER
Non-compliance with operating limits for pressure, temperature, fluid handled and speed
Explosion hazard! Hot or toxic fluid could escape!
Comply with the operating data indicated in the data sheet.Never use the pump for handling fluids it is not designed for.Avoid prolonged operation against a closed shut-off element.Never operate the pump at temperatures, pressures or rotational speeds
exceeding those specified in the data sheet or on the name plate unless the written consent of the manufacturer has been obtained.
DANGER
Formation of a potentially explosive atmosphere inside the pump
Explosion hazard!
When draining tanks take suitable measures to prevent dry running of the
pump (e.g. fill level monitoring).
6.2.1 Ambient temperature
CAUTION
Operation outside the permissible ambient temperature
Damage to the pump (set)!
Observe the specified limits for permissible ambient temperatures.
Observe the following parameters and values during operation:
Table10: Permissible ambient temperatures
Permissible ambient temperature Value
Maximum 40 °C Minimum See data sheet.
6.2.2 Frequency of starts
DANGER
Excessive surface temperature of the motor
Explosion hazard! Damage to the motor!
In case of explosion-proof motors, observe the frequency of starts specified in
the manufacturer's product literature.
The frequency of starts is usually determined by the maximum temperature increase of the motor. This largely depends on the power reserves of the motor in steady­state operation and on the starting conditions (DOL, star-delta, moments of inertia, etc). If the starts are evenly spaced over the period indicated, the pump set can be started up six times per hour (h) with the discharge-side gate valve slightly open.
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CAUTION
Re-starting while motor is still running down
Damage to the pump (set)!
Do not re-start the pump set before the pump rotor has come to a standstill.
6.2.3 Cleaning in place (CIP)
CAUTION
Elastomers do not have sufficient resistance
Damage to the pump!
Effect cleaning/sterilisation only if the elastomer components used in the pump
(e.g. O-rings, mechanical seals) are made of EPDM or other approved materials.
Conditions CIP may be effected with the pump running or with the pump stopped.
Recommended flow velocity: between 2.5 and 3m/s
Cleaning agent, cleaning
process
When performing CIP in the system the pump set is installed in, comply with the concentration limits, temperature limits and contact times given below for the cleaning agents and disinfectants:
Table11: Cleaning sequence
Step Process Cleaning agent Temperature Contact time
[°C] [min]
1 Pre-flushing Water +15 to +25 10 to 15 2 Flushing Water +45 to +60 10 3 Flushing Washing lye +70 to +95 20 to 30 4 Intermediate flushing Water +60 max. 5 to 10 5 Flushing See table below 10 to 15 6 Flushing Water +15 to +25 10 to 15
Table12: Agent for cleaning step5 "Flushing"
Cleaning agent Concentration Temperature
[%] [°C]
Sodium hydroxide (soda lye) 1 to 3 +70 to +90 Phosphoric acid 0,5 +45 Lye, alkaline 5 +95 Nitric acid 1 to 2.5 +45 Citric acid 0.5 to 3 +70
6.2.4 Steaming in place (SIP)
WARNING
Pump casing takes on the same temperature as the sterilisation fluid
Risk of burns!
Fit additional protective devices.Observe the general safety rules and regulations for steam applications.
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CAUTION
Elastomers do not have sufficient resistance
Damage to the pump!
Effect cleaning/sterilisation only if the elastomer components used in the pump
(e.g. O-rings, mechanical seals) are made of EPDM or other approved materials.
CAUTION
SIP with the pump running
Damage to the mechanical seals!
Effect SIP (cleaning using superheated steam) only during standstill of the
pump set.
Conditions Only effect SIP during standstill of the pump set.
Limits Table13: SIP temperature requirements
Elastomer Saturated steam Chemical
EPDM 121°C 82°C FPM/FKM 149°C 82°C
6.2.5 Fluid handled
6.2.5.1 Flow rate
Table14: Flow rate
Temperature range (t) Minimum flow rate Maximum flow rate
0 to +70 ≈ 15 % of Q
opt.
7)
See hydraulic characteristic
curves.
> 70 °C ≈ 25 % of Q
opt.
7)
The calculation formula below can be used to check if an additional heat build-up could lead to a dangerous temperature increase at the pump surface.
×
×
×
Table15: Key
Symbol Description Unit
c Specific heat capacity J/kg K
g Gravitational constant m/s² H Pump discharge head m T
f
Fluid temperature °C
T
O
Temperature at the casing surface °C Pump efficiency at duty point ­Temperature difference K
6.2.5.2 Density of the fluid handled
The pump input power changes in proportion to the density of the fluid handled.
7) Best efficiency point
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CAUTION
Impermissibly high density of the fluid handled
Motor overload!
Observe the information about fluid density in the data sheet.Make sure the motor has sufficient power reserves.
6.2.5.3 Viscosity of the fluid handled
The discharge head, flow rate and power input of the pump are influenced by the viscosity of the fluid handled.
CAUTION
The fluid handled has a higher viscosity than permitted.
Risk of motor overload!
Observe the viscosity limits for the fluid handled given in the data sheet.Make sure the motor has sufficient power reserves.
6.2.5.4 Abrasive fluids
Do not exceed the maximum permissible solids content specified in the data sheet. When the pump handles fluids containing abrasive substances, increased wear of the hydraulic system and shaft seal are to be expected. In this case, reduce the commonly recommended inspection intervals.
6.3 Shutdown/storage/preservation
6.3.1 Measures to be taken for shutdown
The pump (set) remains installed
ü Sufficient fluid is supplied for the operation check run of the pump.
1. For prolonged shutdown periods, start up the pump (set) regularly between once a month and once every three months for approximately five minutes.
ð This will prevent the formation of deposits within the pump and the pump
intake area.
The pump (set) is removed from the pipe and stored
ü The pump has been properly drained. ü The safety instructions for dismantling the pump have been observed.
1. Spray-coat the inside wall of the pump casing and, in particular, the impeller clearance areas with a preservative.
2. Spray the preservative through the suction nozzle and discharge nozzle. It is advisable to then close the pump nozzles (e.g. with plastic caps).
3. Oil or grease all exposed machined parts and surfaces of the pump (with silicone-free oil or grease, food-approved if required) to protect them against corrosion. Observe the additional instructions on preservation. (ðSection3.3,Page12)
If the pump set is to be stored temporarily, only preserve the wetted components made of low-alloy materials. Commercially available preservatives (food-approved, if required) can be used for this purpose. Observe the manufacturer's instructions for application/removal.
Observe any additional instructions and information provided. (ðSection3,Page12)
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6.4 Returning to service
For returning the equipment to service observe the sections on commissioning/start­up and the operating limits. (ðSection6.1,Page27) (ðSection6.2,Page33)
In addition, carry out all servicing/maintenance operations before returning the pump (set) to service. (ðSection7,Page38)
WARNING
Failure to re-install or re-activate protective devices
Risk of injury from moving parts or escaping fluid!
As soon as the work is completed, re-install and re-activate any safety-relevant
devices and protective devices.
NOTE
If the pump has been out of service for more than one year, replace all elastomer seals.
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7 Servicing/Maintenance
7.1 Safety regulations
DANGER
Sparks produced during servicing work
Explosion hazard!
Observe the safety regulations in force at the place of installation!Always perform maintenance work on explosion-proof pump sets outside
potentially explosive atmospheres.
DANGER
Improperly serviced pump set
Explosion hazard! Damage to the pump set!
Service the pump set regularly.Prepare a maintenance schedule with special emphasis on lubricants and shaft
seal.
The operator ensures that maintenance, inspection and installation is performed by authorised, qualified specialist personnel who are thoroughly familiar with the manual.
WARNING
Unintentional starting of the pump set
Risk of injury by moving components and shock currents!
Ensure that the pump set cannot be started unintentionally.Always make sure the electrical connections are disconnected before carrying
out work on the pump set.
DANGER
Improper cleaning of coated pump surfaces
Explosion hazard by electrostatic discharge!
When cleaning coated pump surfaces in atmospheres of Explosion groupIIC,
use suitable anti-static equipment.
WARNING
Fluids handled, consumables and supplies which are hot and/or pose a health hazard
Risk of injury!
Observe all relevant laws.When draining the fluid take appropriate measures to protect persons and the
environment.
Decontaminate pumps which handle fluids posing a health hazard.
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WARNING
Insufficient stability
Risk of crushing hands and feet!
During assembly/dismantling, secure the pump (set)/pump parts to prevent
tilting or tipping over.
A regular maintenance schedule will help avoid expensive repairs and contribute to trouble-free, reliable operation of the pump, pump set and pump parts with a minimum of servicing/maintenance expenditure and work.
NOTE
All maintenance work, service work and installation work can be carried out by KSB Service or authorised workshops. For contact details please refer to the enclosed "Addresses" booklet or visit "www.ksb.com/contact" on the Internet.
Never use force when dismantling and reassembling the pump set.
7.2 Servicing/Inspection
7.2.1 Supervision of operation
DANGER
Risk of potentially explosive atmosphere inside the pump
Explosion hazard!
The pump internals in contact with the fluid to be handled, including the seal
chamber and auxiliary systems must be filled with the fluid to be handled at all times.
Provide sufficient inlet pressure.Provide an appropriate monitoring system.
DANGER
Incorrectly serviced shaft seal
Explosion hazard! Hot, toxic fluid escaping! Damage to the pump set! Risk of burns! Fire hazard!
Regularly service the shaft seal.
DANGER
Excessive temperatures as a result of bearings running hot or defective bearing seals
Explosion hazard! Fire hazard! Damage to the pump set!
Regularly check the rolling element bearings for running noises.
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CAUTION
Increased wear due to dry running
Damage to the pump set!
Never operate the pump set without liquid fill.Never close the shut-off element in the suction line and/or supply line during
pump operation.
CAUTION
Impermissibly high temperature of fluid handled
Damage to the pump!
Prolonged operation against a closed shut-off element is not permitted
(heating up of the fluid).
Observe the temperature limits in the data sheet and in the section on
operating limits. (ðSection6.2,Page33)
While the system is in operation, observe or check the following:
The pump must run quietly and free from vibrations at all times.Check the shaft seal. (ðSection6.1.5,Page29) In case of oil lubrication, ensure the oil level is correct.Check the static sealing elements for leakage.Check the rolling element bearings for running noises.
Vibrations, noise and an increase in current input occurring during unchanged operating conditions indicate wear.
Monitor the correct functioning of any auxiliary connections.Monitor the stand-by pump.
To make sure that stand-by pumps are ready for operation, start them up once a week.
Monitor the bearing temperature.
– The bearing temperature must not exceed 90°C (measured at the motor
housing).
CAUTION
Operation outside the permissible bearing temperature
Damage to the pump!
The bearing temperature of the pump (set) must never exceed 90 °C (measured
on the outside of the motor housing).
NOTE
After commissioning, increased temperatures may occur at grease-lubricated rolling element bearings due to the running-in process. The final bearing temperature is only reached after a certain period of operation (up to 48 hours depending on the conditions).
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7.2.2 Inspection work
DANGER
Excessive temperatures caused by friction, impact or frictional sparks
Explosion hazard! Fire hazard! Damage to the pump set!
Regularly check the cover plates, plastic components and other guards of
rotating parts for deformation and sufficient distance from rotating parts.
DANGER
Static charging due to insufficient potential equalisation
Explosion hazard!
Make sure that the connection between pump and baseplate is electrically
conductive.
7.2.2.1 Checking the clearances
1. Remove pump casing 101.
2. Examine pump casing 101 and impeller vanes for signs of seizure or rubbing contact.
3. Smoothen any signs of seizure or rubbing contact using a polishing cloth.
4. Remove any burrs from the impeller vane.
5. Re-adjust the axial clearance / distance between pump casing 101 and impeller
230. (ðSection7.5.2,Page50)
6. Mount pump casing 101. (ðSection7.5,Page49)
7.2.2.2 Cleaning filters
CAUTION
Insufficient inlet pressure due to clogged filter in the suction line
Damage to the pump!
Monitor contamination of filter with suitable means (e.g. differential pressure
gauge).
Clean filter at appropriate intervals.
7.2.2.3 Checking the flushing liquid
Periodically check the flushing liquid for contamination. If necessary, drain the flushing liquid. Clean the flushing system and fill it with new flushing liquid.
7.2.2.4 Checking the bearing seals
DANGER
Excessive temperatures caused by mechanical contact
Risk of explosion! Damage to the pump set!
Check correct seating of axial seal rings mounted on the shaft.
Only gentle contact of the sealing lip shall be established.
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7.2.3 Lubrication and lubricant change of rolling element bearings
DANGER
Excessive temperatures as a result of bearings running hot or defective bearing seals
Explosion hazard! Fire hazard! Damage to the pump set!
Regularly check the condition of the lubricant.
7.2.3.1 Grease lubrication
The bearings are supplied packed with high-quality lithium-soap grease.
7.2.3.1.1 Intervals
NOTE
On some pump designs (motor ≤ 132) the rolling element bearings are lubricated for life. These pumps are not provided with a lubricating nipple on the bearing bracket.
The rolling element bearings of the pump must be re-lubricated or the grease in the bearings replaced at regular intervals.
The re-lubrication interval is 4000 hours for all sizes. For correct re-lubrication the bearings must be removed, carefully cleaned and
packed with new grease (up to half the volume).
7.2.3.1.2 Grease quality
Optimum grease properties for rolling element bearings
Table16: Grease quality to DIN 51825
Soap basis NLGI grade Worked penetration at
25° C in mm/10
Drop point
Lithium 2 to 3 220-295 ≥ 175°C
Free of resin and acidNot liable to crumbleRust-preventive characteristics
If required, the bearings may be lubricated with greases of other soap bases. Make sure to remove any old grease and rinse the bearings thoroughly.
7.2.3.1.3 Changing the grease
CAUTION
Mixing greases of differing soap bases
Changed lubricating qualities!
Thoroughly clean the bearings.Adjust the re-lubrication intervals to the grease used.
ü The pump has been dismantled for changing the grease.
1. Only half-fill the bearing cavities with grease.
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7.3 Drainage/cleaning
WARNING
Fluids handled, consumables and supplies which are hot and/or pose a health hazard
Hazard to persons and the environment!
Collect and properly dispose of flushing fluid and any fluid residues.Wear safety clothing and a protective mask if required.Observe all legal regulations on the disposal of fluids posing a health hazard.
1. For draining the fluid handled use the pump connections or a valve for residual drainage, if fitted.
2. Always flush the pump if it has been used for handling harmful, explosive and hot fluids or other fluids posing a risk. Always flush and clean the pump before transporting it to the workshop. Provide a certificate of decontamination for the pump.
7.4 Dismantling the pump set
7.4.1 General information/Safety regulations
WARNING
Unqualified personnel performing work on the pump (set)
Risk of injury!
Always have repair work and maintenance work performed by specially trained,
qualified personnel.
WARNING
Hot surface
Risk of injury!
Allow the pump set to cool down to ambient temperature.
WARNING
Improper lifting/moving of heavy assemblies or components
Personal injury and damage to property!
Use suitable transport devices, lifting equipment and lifting tackle to move
heavy assemblies or components.
Always observe the safety instructions and information. (ðSection7.1,Page38) For any work on the motor, observe the instructions of the relevant motor
manufacturer. For dismantling and reassembly observe the exploded views and the general
assembly drawing.
NOTE
All maintenance work, service work and installation work can be carried out by KSB Service or authorised workshops. For contact details please refer to the enclosed "Addresses" booklet or visit "www.ksb.com/contact" on the Internet.
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DANGER
Insufficient preparation of work on the pump (set)
Risk of injury!
Properly shut down the pump set. (ðSection6.1.6,Page30)Close the shut-off elements in the suction line and discharge line.Drain the pump and release the pump pressure.Shut off any auxiliary feed lines.Allow the pump set to cool down to ambient temperature.
NOTE
After a prolonged period of operation the individual components may be hard to pull off the shaft. If this is the case, use an appropriate pull-off device, if possible.
7.4.2 Preparing the pump set
1. De-energise the pump set and secure it against unintentional start-up.
2. Reduce pressure in the piping by opening a consumer installation.
3. Disconnect and remove all auxiliary pipework.
7.4.3 Removing the complete pump set from the piping
1. Disconnect the discharge nozzle and suction nozzle from the piping.
2. Depending on the pump size and motor size, unscrew the bolts that fix the support foot or motor foot to the foundation.
3. Remove the complete pump set from the piping. Alternative: Leave pump casing 101 installed in the piping. Undo clamping piece 81-44. Pull the remaining back pull-out unit out towards the back (back pull-out design).
7.4.4 Removing the pump casing and impeller
7.4.4.1 Sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15
1. For mechanical seal designT with operating modeBQ, or mechanical seal designQ with operating modeDB: Remove quench connections 710.
2. Undo screws 900.1 and remove shroud 683 if fitted.
3. Undo hexagon head bolts 901.1 to remove motor 801.
4. Carefully pull motor 801 out of bearing housing 350/shaft 210.
NOTE
Remove the foot base if necessary. Ball feet: Motors <IEC112: Undo nuts 920.1 and hexagon socket head cap screws 914.1. Remove the foot base. Motors >IEC112: Undo nuts 920.1 and hexagon socket head cap screws 914.1. Remove the front foot base. Remove foot 182.2. Motor feet: Undo nuts (82) and bolts (81). Remove the feet.
5. Undo and remove clamping piece 81-44.
6. Remove pump casing 101.2 and O-ring 412.2.
7. Unscrew impeller nut 922 in anti-clockwise direction. Remove it together with O-ring 412.1.
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8. Remove impeller 230 and key 940.
9. Remove spacer discs 551.
7.4.4.2 Sizes 42-146 and 52-164
1. For mechanical seal designT with operating modeBQ, or mechanical seal designQ with operating modeDB: Remove quench connections 710.
2. Undo screws 900.1 and remove shroud 683 if fitted.
3. Undo hexagon head bolts 901.1 to remove motor 801.
4. Carefully pull motor 801 out of bearing housing 350/shaft 210.
NOTE
Remove the foot base if necessary. Ball feet: Motors <IEC112: Undo nuts 920.1 and hexagon socket head cap screws 914.1. Remove the foot base. Motors >IEC112: Undo nuts 920.1 and hexagon socket head cap screws 914.1. Remove the front foot base. Remove foot 182.2. Motor feet: Undo nuts (82) and bolts (81). Remove the feet.
5. Undo screw 900.
6. Remove pump casing 101.2.
7. Remove first impeller 230 and key 940.
8. Remove the interstage plate with guide vanes 172 and O-ring 412.2.
9. Remove second impeller 230 and key 940.
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7.4.5 Removing the mechanical seal
7.4.5.1 Mechanical seal designT, operating modeB
a) b)
101.1
101.1
433
433
101.2 412.1
210
210
551 230 940 922
554 940 172
932 230 172
Fig.5: Mechanical seal designT, operating modeB a) Sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15 b) Sizes 42-146 and 52-164
1. Slide back the ring retainer 8). Remove circlip 932 from shaft 210.
2. Remove the primary ring of mechanical seal 433. To do so, rotate the primary ring and the spring in clockwise direction while pulling them off the end of the shaft.
3. Undo hexagon socket head cap screws 914.2. Take pump casing 101.1 carefully off bearing housing 350.
4. Take the mating ring of mechanical seal 433 out of its seat in pump casing
101.1.
5. Pull thrower 507 off shaft 210.
8) Sizes 42-146 and 52-164 only
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7.4.5.2 Mechanical seal designT, operating modeBQ
a) b)
101.1
101.1
412.3
210
210
902
421.2 710 471.2
421.2 710 412.3
471.2 902
Fig.6: Mechanical seal designT, operating modeBQ a) Sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15 b) Sizes 42-146 and 52-164
1. Slide back the ring retainer9). Remove circlip 932 from shaft 210.
2. Remove the primary ring of mechanical seal 433. To do so, rotate the primary ring and the spring in clockwise direction while pulling them off the end of the shaft.
3. Undo hexagon socket head cap screws 914.2. Take pump casing 101.1 carefully off bearing housing 350.
4. Undo nuts 920.4 and studs 902.
5. Carefully remove seal cover 471.2 from pump casing 101.1.
6. Remove lip seal 421.2 from seal cover 471.2.
7. Take the mating ring of mechanical seal 433 out of its seat in pump casing
101.1.
9) Sizes 42-146 and 52-164 only
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7.4.5.3 Mechanical seal designQ, operating modeDB
a) b)
101.1 412.1
210 433
471.1
412.5
922
101.2
902
230
940
433
A
471.1
210 940
Fig.7: Mechanical seal designQ, operating modeDB a) Sectional drawing b) Installation dimensionA
1. On sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15: Undo nuts (69) and studs 902. On sizes 42-146 and 52-164: Undo grub screws 904.4.
2. Move back seal cover 471.1 to separate it from pump casing 101.1.
3. Undo hexagon socket head cap screws 914.2. Take pump casing 101.1 carefully off bearing housing 350.
4. Remove the mating ring of mechanical seal 433 from the rear section of pump casing 101.1.
NOTE
Observe distance "A" when re-installing the mechanical seal. Note down this distance to be able to re-install the mechanical seal accurately.
5. Undo the grub screws at the primary ring and pull the primary ring off shaft
210.
6. Remove seal cover 471.1.
7. Press the mating ring of mechanical seal 433 out of seal cover 471.1. Remove O­ring 412.5.
8. Pull thrower 507 off shaft 210.
7.4.6 Dismantling the bearing assembly
1. If applicable, undo screws 900.2 and remove holder 732.
2. Undo hexagon head bolts 901.2.
3. Remove bearing cover 360.
4. Press the assembly consisting of shaft 210 and rolling element bearing 320 and – for motor sizes IEC160 and above – lip seal 421.1 out of bearing housing 350.
5. Undo and remove nut 920.3.
6. Guide shaft 210 out of rolling element bearing 320. Remove lip seal 421.1 if fitted.
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7.5 Reassembling the pump set
7.5.1 General information/Safety regulations
DANGER
Wrong selection of motor
Explosion hazard!
Use an original motor or a motor of identical design from the same
manufacturer.
The permissible temperature limits at the motor flange and motor shaft must
be higher than the temperatures generated by the pump. (Contact KSB for temperatures).
WARNING
Improper lifting/moving of heavy assemblies or components
Personal injury and damage to property!
Use suitable transport devices, lifting equipment and lifting tackle to move
heavy assemblies or components.
CAUTION
Improper reassembly
Damage to the pump!
Reassemble the pump (set) in accordance with the general rules of sound
engineering practice.
Use original spare parts only.
Sequence Always reassemble the pump in accordance with the corresponding general assembly
drawing or exploded view.
Sealing elements Always use new O-rings.
Never use O-rings that have been made by cutting an O-ring cord to size and gluing the ends together.
Always use new gaskets, making sure that they have the same thickness as the old ones.
Always fit gaskets of asbestos-free materials or graphite without using lubricants (e.g. copper grease, graphite paste).
Assembly adhesives Avoid the use of assembly adhesives, if possible.
Match the lubricants to the fluid handled (e.g. water for foodstuff applications).
Tightening torques For reassembly, tighten all screws and bolts as specified in this manual.
Tightening torque of the impeller nut: 70-80 Nm
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7.5.2 Adjusting the clearances
C B
A
Fig.8: Pump clearances
A Rear side of impeller,
distance between impeller and pump casing
B Distance between pump casing and
pump inlet casing
C Distance between front side of
impeller and pump inlet casing
Explanation: Distance C is set at the factory; distance B is achieved by using spacer discs which are
fitted to adjust distance A (on the rear side of the impeller). Should any problems occur, particularly verify distance A as this is the most
significant value. The only distance for which a deviation is permissible is distance B.
Table17: Impeller and casing clearances
Size A B C
40-146 0,15 0,15 -­50-164 0,15 0,15 2,85 60-200 0,20 0,20 2,80 65-200 0,20 0,20 2,80 80-240-11 0,30 0,30 4,20 80-240-11 0,30 0,30 4,20
7.5.3 Fitting the bearing assembly
1. Check shaft 210 for any wear. Clean it thoroughly.
2. Fit rolling element bearing 320 on shaft 210.
3. Fit and tighten nut 920.3.
4. Insert the assembly consisting of shaft 210 and rolling element bearing 320 into bearing housing 350. For motor size IEC160 and above: Fit lip seal 421.1.
5. Fit bearing cover 360. Fasten it with hexagon head bolts 901.2.
6. Slide thrower 507 onto shaft 210.
7. Fit holder 732 (if applicable). Fasten screws 900.2.
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7.5.4 Installing the mechanical seal
7.5.4.1 Mechanical seal designT, operating modeB
CAUTION
The keyway could damage the seal faces and O-rings
Damage to the mechanical seal!
Always handle seal faces with utmost care.
a) b)
101.1
101.1
433
433
101.2 412.1
210
210
551 230 940 922
554 940 172
932 230 172
Fig.9: Mechanical seal designT, operating modeB a) Sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15 b) Sizes 42-146 and 52-164
1. Carefully insert the mating ring of mechanical seal 433 into pump casing 101.1.
2. Place pump casing 101.1 on bearing housing 350. Slide the seal carefully over shaft 210.
3. Fasten pump casing 101.1 with hexagon socket head cap screws 914.2 to bearing housing 350 .
4. Slide the primary ring of mechanical seal 433 onto shaft 210.
5. Fit the ring retainer
10)
on shaft 210. Use the ring retainer to compress the spring
of mechanical seal 433. Lock the spring with circlip 932.
7.5.4.2 Mechanical seal designT, operating modeBQ
CAUTION
The keyway could damage the seal faces and O-rings
Damage to the mechanical seal!
Always handle seal faces with utmost care.
10) For sizes 42-146 and 52-164 only.
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a) b)
101.1
101.1
412.3
210
210
902
421.2 710 471.2
421.2 710 412.3
471.2 902
Fig.10: Mechanical seal designT, operating modeBQ a) Sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15 b) Sizes 42-146 and 52-164
1. Fit lip seal 421.2 in seal cover 471.2.
2. Fit studs 902 in pump casing 101.1. Tighten the studs.
3. Place seal cover 471.2 on studs 902. Fasten the studs with nuts (69).
4. Carefully insert the mating ring of mechanical seal 433 into pump casing 101.1.
5. Place pump casing 101.1 on bearing housing 350. Make sure not to damage lip seal 421.2 and mating ring.
6. Fit and tighten hexagon socket head cap screws 914.2.
7. Slide the primary ring of mechanical seal 433 onto shaft 210.
8. Fit the ring retainer
11)
on shaft 210. Use the ring retainer to compress the spring
of mechanical seal 433. Lock the spring with circlip 932.
7.5.4.3 Mechanical seal designQ, operating modeDB
CAUTION
The keyway could damage the seal faces and O-rings
Damage to the mechanical seal!
Always handle seal faces with utmost care.
11) For sizes 42-146 and 52-164 only.
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a) b)
101.1 412.1
210 433
471.1
412.5
922
101.2
902
230
940
433
A
471.1
210 940
Fig.11: Mechanical seal designQ, operating modeDB a) Sectional drawing b) Installation dimensionA
1. Fit O-ring 412.5 in seal cover 471.1.
2. Insert the mating ring (motor end) of mechanical seal 433 into seal cover 471.1.
3. On sizes 42-146 and 52-164: Fit hexagon head bolts 901.4 in seal cover 471.1. On sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15: Fit and tighten studs 902 in pump casing 101.1.
4. Fit seal cover 471.1 on shaft 210. Slide it right to the end of the shaft.
5. Slide the primary rings of mechanical seal 433 onto shaft 210.
6. Check distance A: This value must be observed to make sure the load on the mechanical seal is evenly distributed. Correct values: Size 40-146: A = 16mm Size 50-164: A = 17.5mm Size 60-200: A = 15.5mm Size 65-200: A = 15.5mm Size 80 240-11: A = 19.5mm Size 80 240-15: A = 19.5mm
7. If value A is correct, tighten the grub screws of the primary ring.
8. Fit the mating ring (pump end) into the rear end of pump casing 101.1.
9. Carefully place pump casing 101.1 on bearing housing 350. Make sure not to damage the seal.
10. Fasten pump casing 101.1 to bearing housing 350 with hexagon socket head cap screws 914.2.
11. Slide seal cover 471.1 right against pump casing 101.1. Fasten the seal cover.
12. On sizes 42-146 and 52-164: Fasten it with hexagon head bolts 901.4. On sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15: Fasten it with nuts (69).
7.5.5 Fitting the impeller and the pump casing
7.5.5.1 Sizes 40-146, 50-164, 60-200, 65-200, 80-240-11 and 80-240-15
1. Slide a suitable spacer disc 551 onto shaft 210.
2. Insert key 940 into the keyway of shaft 210. Fit impeller 230.
3. Fit O-ring 412.1 in impeller nut 922. Secure impeller 230 with the nut.
4. Fit O-ring 412.2 in the groove of pump casing 101.1.
5. Fit pump casing 101.2. Secure it with clamping piece 81-44.
Page 54
7 Servicing/Maintenance
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Vitaprime
NOTE
Fit the foot base if applicable. Ball feet: Motors <IEC112: Fasten the foot base to pump casing 101.1 with hexagon socket head cap screws 914.1 and nuts 920.1. Motors >IEC112: Fasten the front foot base to pump casing 101.1 with hexagon socket head cap screws 914.1 and nuts 920.1. Fasten foot 182.2 to motor 801. Motor feet: Fasten the feet to motor 801 with bolts (81) and nuts (82).
6. Mount motor 801. To do so, insert the motor shaft into shaft 210. Fasten motor 801 with hexagon head bolts 901.1.
7. If applicable, place shroud 683 onto the motor. Fasten it to holder 732 with screws 900.1.
8. For mechanical seal designT with operating modeBQ and mechanical seal designQ with operating modeDB: Fit quench connections 710 in seal cover
471.1/.2.
7.5.5.2 Sizes 42-146 and 52-164
1. Insert the first key 940. Slide the first impeller 230 onto shaft 210.
2. Insert O-ring 412.2 into the groove in the pump casing. Then fit interstage plate with guide vane 172.
3. Insert O-ring 412 in interstage plate with guide vane 172. Fit the second interstage plate with guide vane 172.
4. Insert the second key 940. Slide the second impeller 230 onto shaft 210.
5. Insert O-ring 412 in interstage plate with guide vane 172. Fasten pump casing
101.2 with screws 900.
NOTE
Fit the foot base if applicable. Ball feet: Motors <IEC112: Fasten the foot base to pump casing 101.1 with hexagon socket head cap screws 914.1 and nuts 920.1. Motors >IEC112: Fasten the front foot base to pump casing 101.1 with hexagon socket head cap screws 914.1 and nuts 920.1. Fasten foot 182.2 to motor 801. Motor feet: Fasten the feet to motor 801 with bolts (81) and nuts (82).
6. Mount motor 801. To do so, insert the motor shaft into shaft 210. Fasten motor 801 with hexagon head bolts 901.1.
7. If applicable, place shroud 683 onto the motor. Fasten it to holder 732 with screws 900.1.
8. For mechanical seal designT with operating modeBQ and mechanical seal designQ with operating modeDB: Fit quench connections 710 in seal cover
471.1/.2.
Page 55
7 Servicing/Maintenance
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Vitaprime
7.6 Spare parts stock
7.6.1 Ordering spare parts
Always quote the following data when ordering replacement or spare parts:
Order numberOrder item numberConsecutive numberType seriesSizeMaterial variantSeal codeYear of construction
Refer to the name plate for all data. (ðSection4.3,Page16) Also specify the following data:
Part number and description (ðSection9.1,Page57)Quantity of spare partsShipping addressMode of dispatch (freight, mail, express freight, air freight)
7.6.2 Recommended spare parts stock for 2 years' operation to DIN24296
Table18: Quantity of spare parts for recommended spare parts stock
Part No. Description Number of pumps (including stand-by pumps)
2 3 4 5 6 and 7 8 and 9 10 and
more
230 Impeller 1 1 1 2 2 2 20% 210 + 940 Shaft with key 1 1 1 2 2 2 20% 433 Mechanical seal set 2 3 4 5 6 7 90% 320 Rolling element bearing set 1 1 2 2 2 3 25%
412.1 O-ring (impeller nut) 4 6 8 8 9 10 100%
412.2 O-ring (casing) 4 6 8 8 9 12 150%
412.5 O-ring (seal housing) 4 6 8 8 9 10 100%
421.1 Lip seal set 4 6 8 8 9 10 100%
421.2 Lip seal set 4 6 8 8 9 10 100%
Page 56
8 Trouble-shooting
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Vitaprime
8 Trouble-shooting
WARNING
Improper work to remedy faults
Risk of injury!
For any work performed to remedy faults, observe the relevant information
given in this operating manual and/or in the product literature provided by the accessories manufacturer.
If problems occur that are not described in the following table, consultation with the KSB customer service is required.
A Pump is running, but does not deliver
B Insufficient flow rate C Discharge pressure below specified value
D Excessive power consumption
E Excessive current consumption
Table19: Trouble-shooting
A B C D E Possible cause Remedy
✘ ✘ - - - Air ingress into the suction line Check integrity of all pipe connections and re-
seal if necessary.
✘ - - - - Suction line not submerged in fluid Check fill level. ✘ ✘ ✘ - - Clearance tolerances between impeller and
casing exceeded
Re-adjust impeller or replace if worn.
✘ - - - - No fluid inside the pump casing Fill in fluid. ✘ - - - - Cavitation caused by excessive suction lift Reduce suction lift. ✘ - - - - Air pocket in discharge line Fit a vent valve. ✘ - - - - Pump does not prime. Check the points mentioned in section
(ðSection6.1,Page27) .
✘ - - - - Wrong direction of rotation Change electrical connection of motor. ✘ ✘ - - - Suction line clogged Check suction line and clean if necessary. ✘ - - - - The shut-off valves are closed. Open all valves.
- - - - System pressure too high Check discharge-side piping; increase nominal piping diameter if necessary.
- - - - Air intake at the mechanical seal Check mechanical seal arrangement.
- - - - Fluid viscosity is higher than specified for pump
selection.
Consult the manufacturer.
- - - - System pressure lower than specified Throttle the discharge-side valve.
- - - - Power input lower than permitted Check all system conditions.
- - - - Pump speed too high (frequency inverter
operation)
Reduce speed.
- - - - Impeller does not rotate freely. Eliminate clogging, re-adjust impeller.
- - - - Viscosity and/or density of fluid higher than
specified
Consult the manufacturer.
- - - - Bearings run sluggishly. Replace rolling element bearings, replace lubricant.
- - - - Flow rate too high Check items listed above.
- - - - Excessive drop of electrical voltage Check voltage supply (trained specialist personnel only).
- - - - Fault in electrical system Shut down pump.
Page 57
9 Related Documents
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Vitaprime
9 Related Documents
9.1 General assembly drawing with list of components (single-stage pumps)
9.1.1 Pump size 40-146, motor size 90
683 801 920.3
360
914.2
900.1 732
900.2
916
210 101.1
101.2
922940562433
182.1
920.2
909.2
901.2
901.1 350
320
507
914.1
909.1
920.1 551
412.2 81-44
230
412.1
Fig.12: Size 40-146, motor 90
Table20: List of components for pump size 40-146, motor size 90
Part No. Description Part No. Description
81-44 Clamping piece 562 Parallel pin
101.1/.2 Pump casing 683 Shroud
182.1 Foot 732 Holder 210 Shaft 801 Flanged motor 230 Impeller 900.1/.2 Bolt/screw 320 Rolling element bearing 901.1/.2 Hexagon head bolt 350 Bearing housing 909.1/.2 Adjusting screw 360 Bearing cover 914.1/.2 Hexagon socket head cap
screw
412.1/.2 O-ring 916 Plug 433 Mechanical seal 920.1/.2/.3 Nut 507 Thrower 922 Impeller nut 551 Spacer disc 940 Key
Page 58
9 Related Documents
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Vitaprime
9.1.2 Pump size 50-164, motor size 132
683
801
920.3
360
914.2 900.1
732900.2
916
210
101.1 101.2
922
940
562
433
182.2
920.2
909.2 901.2
901.1
350
320 507
914.1 909.1
920.1
551
412.2
81-44230
412.1
182.1
Fig.13: Pump size 50-164 / motor size 132
Table21: List of components for pump size 50-164, motor size 132
Part No. Description Part No. Description
81-44 Clamping piece 562 Parallel pin
101.1/.2 Pump casing 683 Shroud
182.1/.2 Foot 732 Holder 210 Shaft 801 Flanged motor 230 Impeller 900.1/.2 Bolt/screw 320 Rolling element bearing 901.1/.2 Hexagon head bolt 350 Bearing housing 909.1/.2 Adjusting screw 360 Bearing cover 914.1/.2 Hexagon socket head cap
screw
412.1/.2 O-ring 916 Plug 433 Mechanical seal 920.1/.2/.3 Nut 507 Thrower 922 Impeller nut 551 Spacer disc 940 Key
Page 59
9 Related Documents
59 of 68
Vitaprime
9.1.3 Pump size 60/65-200, motor size 160
683
801
920.3
360
914.2
900.1
732900.2
421.1
210
101.1
101.2
922
940
562433
182.1 920.2
909.2 901.2
901.1
350
320
507
914.1 909.1
920.1
551
412.2
81-44
230
412.1
182.2 636
Fig.14: Pump size 60/65-200, motor size 160
Table22: Pump size 60/65-200, motor size 160
Part No. Description Part No. Description
81-44 Clamping piece 562 Parallel pin
101.1/.2 Pump casing 636 Lubricating nipple
182.1/.2 Foot 683 Shroud 210 Shaft 732 Holder 230 Impeller 801 Flanged motor 320 Rolling element bearing 900.1/.2 Bolt/screw 350 Bearing housing 901.1/.2 Hexagon head bolt 360 Bearing cover 909.1/.2 Adjusting screw
412.1/.2 O-ring 914.1/.2 Hexagon socket head cap screw
421.1 Lip seal 920.1/.2/.3 Nut
433 Mechanical seal 922 Impeller nut 507 Thrower 940 Key 551 Spacer disc
Page 60
9 Related Documents
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Vitaprime
9.1.4 Pump size 80-240, motor size 160
683
801
920.3
360
914.2
900.1
732900.2
421.1
210101.1
101.2
922
940
562
433
182.1
920.2
909.2 901.2
901.1
350
320
507
914.1 909.1
81-92
551
412.2
81-44
230
412.1
182.2
636
81-92
901.3
Fig.15: Pump size 80-240, motor size 160
Table23: List of components for pump size 80-240, motor size 160
Part No. Description Part No. Description
81-44 Clamping piece 551 Spacer disc 81-92 Cover plate 562 Parallel pin
101.1/.2 Pump casing 636 Lubricating nipple
182.1/.2 Foot 683 Shroud
210 Shaft 732 Holder 230 Impeller 801 Flanged motor 320 Rolling element bearing 900.1/.2 Bolt/screw 350 Bearing housing 901.1/.2/.3 Hexagon head bolt 360 Bearing cover 909.1/.2 Adjusting screw
412.1/.2 O-ring 914.1/.2 Hexagon socket head cap screw
421.1 Lip seal 920.2/.3 Nut
433 Mechanical seal 922 Impeller nut 507 Thrower 940 Key
Page 61
9 Related Documents
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Vitaprime
9.2 General assembly drawing with list of components (two-stage pumps)
9.2.1 Pump size 42-146, motor size 112
683
801
920.3
360 914.2 900.1
732
900.2
210
101.1
101.2
932
940
562
433
182.1920.2
909.2
901.2
901.1
350
320
507
914.1 909.1
554
412.2
920.1
230
564
182.2 900
916 172
172
412
914
Fig.16: Pump size 42-146, motor size 112
Table24: List of components for pump size 42-146, motor size 112
Part No. Description Part No. Description
101.1/.2 Pump casing 564 Pin
172 Interstage plate with guide
vane
683 Shroud
182.1/.2 Foot 732 Holder
210 Shaft 801 Flanged motor 230 Impeller 900.1/.2 Bolt/screw 320 Rolling element bearing 901.1/.2 Hexagon head bolt 350 Bearing housing 909.1/.2 Adjusting screw 360 Bearing cover 914.1/.2 Hexagon socket head cap
screw
412.2 O-ring 916 Plug
433 Mechanical seal 920.1./2/.3 Nut 507 Thrower 932 Circlip 554 Washer 940 Key 562 Parallel pin
Page 62
9 Related Documents
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Vitaprime
9.2.2 Pump size 52-164, motor size 132
683
801
920.3
360
914.2
900
932
900.1 507
210
101.1
101.2
732
940
564
433
182.1920.1
909.2 901.2
901.1 350
320
914.1 909.1 554
412.2 172
230
172
182.2
916
900.2
412
Fig.17: Pump size 52-164, motor size 132
Table25: List of components for pump size 52-164, motor size 132
Part No. Description Part No. Description
101.1/.2 Pump casing 564 Pin 172 Interstage plate with guide
vane
683 Shroud
182.1/.2 Foot 732 Holder 210 Shaft 801 Flanged motor 230 Impeller 900.1/.2 Bolt/screw 320 Rolling element bearing 901.1/.2 Hexagon head bolt 350 Bearing housing 909.1/.2 Adjusting screw 360 Bearing cover 914.1/.2 Hexagon socket head cap
screw
412.1/.2 O-ring 916 Plug 433 Mechanical seal 920.1/.3 Nut 507 Thrower 932 Circlip 554 Washer 940 Key
Page 63
10 EU Declaration of Conformity
63 of 68
Vitaprime
10 EU Declaration of Conformity
Manufacturer: KSB SE & Co. KGaA
Johann-Klein-Straße 9
67227 Frankenthal (Germany)
The manufacturer herewith declares that the product:
Vitacast, Vitacast-Bloc, Vitaprime, Vitastage
KSB order number: ...................................................................................................
is in conformity with the provisions of the following Directives as amended from time to time:
– Pump (set): EC Machinery Directive 2006/42/EC – Pump (set): Regulation 1935/2004/EG on Materials and Articles Intended to Come into Contact with Food
The manufacturer also declares that
the following harmonised international standards have been applied:
– ISO 12100 – EN 809
Person authorised to compile the technical file:
Name Function Address (company) Address (Street, No.) Address (post or ZIP code, city) (country)
The EU Declaration of Conformity was issued in/on:
Place, date
..............................
12)
.............................
Name
Function
Company
Address
12) A signed, legally binding EU Declaration of Conformity is supplied with the product.
Page 64
11 Certificate of Decontamination
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Vitaprime
11 Certificate of Decontamination
Type: ................................................................................................................................
Order number/ Order item number
13)
: ................................................................................................................................
Delivery date: ................................................................................................................................
Field of application: ................................................................................................................................
Fluid handled
13)
: ................................................................................................................................
Please tick where applicable
13)
:
Radioactive Explosive Corrosive Toxic
Harmful Bio-hazardous Highly flammable Safe
Reason for return
13)
: ................................................................................................................................
Comments: ................................................................................................................................
................................................................................................................................
The product/accessories have been carefully drained, cleaned and decontaminated inside and outside prior to dispatch/ placing at your disposal.
We herewith declare that this product is free from hazardous chemicals, biological and radioactive substances.
For mag-drive pumps, the inner rotor unit (impeller, casing cover, bearing ring carrier, plain bearing, inner rotor) has been removed from the pump and cleaned. In cases of containment shroud leakage, the outer rotor, bearing bracket lantern, leakage barrier and bearing bracket or adapter have also been cleaned.
For canned motor pumps, the rotor and plain bearing have been removed from the pump for cleaning. In cases of leakage at the stator can, the stator space has been examined for fluid leakage; if fluid handled has penetrated the stator space, it has been removed.
No special safety precautions are required for further handling. The following safety precautions are required for flushing fluids, fluid residues and disposal:
...............................................................................................................................................................
...............................................................................................................................................................
We confirm that the above data and information are correct and complete and that dispatch is effected in accordance with the relevant legal provisions.
.................................................................... ....................................................... .......................................................
Place, date and signature Address Company stamp
13) Required fields
Page 65
Index
65 of 68
Vitaprime
Index
A
Abrasive fluids36 Automation18
B
Bearing temperature40 Bearings17
C
Certificate of decontamination64 Cleaning34, 35 Commissioning27 Connections18
D
Design17 Direction of rotation26 Dismantling43 Disposal13 Drive17
E
Electromagnetic compatibility24 Event of damage6
Ordering spare parts55
Explosion protection10, 21, 25, 26, 27, 28, 29, 33, 38, 39, 41, 42
F
Faults
Causes and remedies56 Fields of application8 Filter41
Fluid handled
Density35 Frequency of starts33
G
Grease lubrication
Grease quality42
I
Impeller type17 Installation at site21 Intended use8 Interference immunity24
K
Key to safety symbols/markings7
M
Maintenance39 Mechanical seal29 Monitoring equipment11
N
Name plate16 Noise characteristics19
O
Operating limits33 Operation on a frequency inverter24 Order number6 Other applicable documents6
P
Partly completed machinery6 Permissible forces at the pump nozzles23 Piping22 Preservation13, 36 Product code14 Product description14 Pump casing17
R
Reassembly43, 49 Return to supplier13 Returning to service37
S
Safety8 Safety awareness9 Scope of supply20 Shaft seal17 Shutdown36
Spare part
Ordering spare parts55 Start-up29 Storage13, 36
T
Temperature limits10 Transport12
W
Warnings7 Warranty claims6
Page 66
Page 67
Page 68
KSB SE & Co. KGaA
Johann-Klein-Straße 9 • 67227 Frankenthal (Germany) Tel. +49 6233 86-0 www.ksb.com
1969.84/05-EN
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