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Model lsb, Description, 8 use acc. to regulations – Xylem LSB User Manual

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Installation, Operation and Maintenance Instruction

Model LSB

LSB 100-english

page 76

Revision 02

Artikel Nr. 771076129

Ausgabe 01/2010

2.7.7 Electric switches and control device,
Instrumentation and accessories

Electric

switches

and

control

devices,

instrumentation

and

accessories

must

correspond with the valid safety requirements

and regulations for explosion protection.

2.8 Use acc. to Regulations

2.8.1 Speed, Pressure, Temperature

Suitable safety measures must be taken at the

plant to ensure that the speed, pressure and

temperature of the pump and the shaft sealing

do not exceed the limit values given in the data

sheet and / or order confirmation. The given

admission pressures (system pressures) must

also be sufficiently high.

Further, pressure shocks, as can occur on too fast

shut down of the facility, must be kept away from the

pump (e.g. by non-return valve at pressure side,

airtanks). Quick temperature changes must be

avoided. They could cause a temperature shock and

lead to damage or impair the function of single

components.

2.8.2 Permitted Nozzle Loads and Torques

Basically the suction and discharge piping must

be designed in such way, that as little forces as

possible are effective to the pump. If that is not

possible, the values shown in chapter 3.5 must

not be exceeded under any circumstances. This

is valid for the operation as well as for the

standstill of the pump and therefore for all

possible pressures and temperatures of the

unit.

2.8.3 NPSH

The pumped liquid must have a min. pressure

NPSH at the impeller inlet, so that cavitation

free work is secured resp. a "break off" of the

pump flow is prevented. This condition is

fulfilled, when NPSH-value of the system

(NPSHA) lies above NPSH-value of the pump

(NPSHR) under all operating conditions.

Attentention must especially be piad to the NPSH-

value on pumping liquids near the vapour pressure. If

the NPSH-value of the pump remains under, this can

lead from damage of the material due to cavitation to

destruction by overheating.

The NPSH-value of the pump (NPSHR) is shown in

the curves of every pump type.

2.8.4 Sealing, Flushing, Cooling

Suitable provisions for the regulation and monitoring of

sealing, flushing or cooling are to be provided.

When handling dangerous liquids or if temperatures

are high, care should be taken to ensure that the

pump ceases operating if the sealing, flushing or

cooling system fails.

Sealing, flushing and cooling systems must always be

operational before the pump is started up. They

should not be taken out of operation until the pump

has stopped, provided that the nature of the operation

allows this at all.

2.8.5 Back Flow

In systems where pumps are operating in closed

circuits under pressure (gas cushions, steam

pressure), the pressure of the gas cushion must not

be reduced via the pump, since the back flow speed

may be much higher than the operating speed, which

would destroy the unit.

3. Description

3.1 Design

LSB-pumps are single-stage volute casing pumps in

block design. Hydraulic design and dimensions comply

with ISO 2858/ EN 22858, the technical design

complies with ISO 5199/EN 25199.

The motors comply with DIN 42677-IM B5. Motor and

pump shaft are coupled rigidly.

The permitted application conditions and design

details of the delivered pump are shown in the

attached data sheet and / or the order confirmation

(see Design Coding System in chapter 3.2).

Installation position: LSB-pump are intended for use

with horizontal shaft, discharge up. Installation

positions deviating therefrom must be approved by the

manufacturer.

3.1.1 Design Coding System

Due to the coding on data sheet and / or order

confirmation all information regarding the delivered

pump can be found in this Installation, Operation and

Maintenance Instruction, e.g.:

LSB 100 - 65 - 250 S1 V L 2 - 132

(0) (1) (2) (3) (4)

(5) (6) (7) (8)

Position (0) - Name of Model

LSB - ISO block pump

Position (1) - Suction Nozzle in mm

Position (2) - Discharge Nozzle in mm

Position (3) - Nominal diameter of impeller in mm

Position (4) - Shaft sealing

S1 - Single-mech. seal acc. DIN 24960 l1k /

EN 12756 form U

S4 - Single-mech. seal acc. DIN 24960 l1k /

EN 12756 form U

with Quench (throttle bush)

Position (5) - Material Impeller

N = Cast Iron (0.6025)

L = Ductile Iron (0.7043)

V = Carbon Steel (1.4408)

W = Duplex (1.4517)

Position (6) - Material pump casing (same coding as

impeller, cast iron not available)