Flowserve VTP, VPC User Instructions

USER INSTRUCTIONS

Vertical Turbine Pumps Wet Pit (VTP) Double Casing (VPC)

E, S and A series VTPs in wet pit and suction barrel designs ranging in sizes from 50 mm (6 in.) to 1300 mm (52 in.) with a single or multiple stages. (This manual does not cover VTPs fitted with thrust bearing assemblies and VTPs built for cryogenic service).

PCN=71569224 02-15(F), Based on VTP-QS-0896 Original Instructions

Installation

Operation

Maintenance

These instructions must be read prior to installing,

operating, using and maintaining this equipment

VERTICAL TURBINE PUMPS (VTPS) CENTRIFUGAL PUMPS ENGLISH 71569224 – 02-15

CONTENTS

PAGE

1

 INTRODUCTION AND SAFETY ....................... 4

1.1 General ............................................................ 4

1.2 CE Marking and Approvals .............................. 4

1.3 Disclaimer ........................................................ 4

1.4 Copyright ......................................................... 4

1.5 Duty Conditions ............................................... 4

1.6 Safety .............................................................. 5

1.7 Safety Labels Summary .................................. 8

1.8 Specific Machine Performance ........................ 8

1.9 Noise Level ...................................................... 8

1.10 Specific machine performance ................ 9

2 TRANSPORT AND STORAGE ....................... 10

2.1 Consignment receipt and unpacking ............. 10

2.2 Handling ........................................................ 10

2.3 Lifting ............................................................. 10

2.4 Storage .......................................................... 14

2.5 Recycling and End of Product Life ................ 14

3 DESCRIPTION ................................................ 14

3.1 Configuration ................................................. 14

3.2 Nomenclature ................................................ 16

3.3 Design of Major Parts .................................... 17

3.4 Performance and Operation Limits................ 21

4 INSTALLATION ............................................... 21

4.1 Location ......................................................... 21

4.2 Preparation .................................................... 21

4.3 Foundation ..................................................... 21

4.4 Grouting ......................................................... 23

4.5 Lifting and Assembly ..................................... 24

4.6 Initial Alignment ............................................. 30

4.7 Piping ............................................................. 31

4.8 Electrical Connections ................................... 34

4.9 Final Shaft Alignment Check ......................... 34

4.10 Protection Systems ................................ 34

PAGE

6 MAINTENANCE ............................................... 46

6.1 General .......................................................... 47

6.2 Maintenance Schedule .................................. 47

6.3 Spare Parts .................................................... 49

6.4 Recommended Spares and Consumables .... 49

6.5 Tools Required ............................................... 49

6.6 Fastener Torques ........................................... 50

6.7 Setting Impeller Clearance............................. 51

6.8 Disassembly ................................................... 51

6.9 Examination of Parts ...................................... 51

6.10 Assembly ................................................ 55

7 FAULTS; CAUSES AND REMEDIES ............. 56

8 DRAWINGS AND PARTS LISTS .................... 58

8.1 Cross Section: Product Lubricated VTP ........ 58

8.2 Cross Section: Enclosed Tube VTP ............... 61

8.3 Cross Section: Suction Barrel VTP ................ 64

8.4 General Arrangement Drawing ...................... 67

9 CERTIFICATION .............................................. 67

10 OTHER RELEVANT DOCUMENTATION AND

MANUALS ........................................................ 67

10.1 Supplementary User Instructions ........... 67

10.2 Change Notes ........................................ 67

11 APPENDIX ....................................................... 68

11.1 Bill of Materials Reference Numbers ..... 68



5 COMMISSIONING, STARTUP, OPERATION

AND SHUTDOWN ........................................... 35

5.1 Pre-commissioning Procedure ...................... 35

5.2 Pump Lubricants ........................................... 35

5.3 Impeller Adjustment ....................................... 38

5.4 Direction of Rotation ...................................... 41

5.5 Guarding ........................................................ 41

5.6 Priming and Auxiliary Supplies ...................... 41

5.7 Starting the Pump .......................................... 42

5.8 Operating the Pump ...................................... 45

5.9 Stopping and Shutdown ................................ 46

5.10 Hydraulic, mechanical and electrical duty46

Page 2 of 76 flowserve.com



VERTICAL TURBINE PUMPS (VTPS) CENTRIFUGAL PUMPS ENGLISH 71569224 – 02-15

INDEX

PAGE

Alignment of shafting (see 4.3, 4.6 and 4.9)

Assembly (6.10) ....................................................... 55

ATEX marking (1.6.4.2) ............................................. 7

Bill of materials reference numbers (11.1) …….......68

CE marking and approvals (1.2) ................................ 4

Certification (9) ........................................................ 67

Change notes (10.2) ................................................ 67

Clearances, impeller (6.7) ....................................... 51

Commissioning and operation (5) ........................... 35

Compliance, ATEX (1.6.4.1) ...................................... 6

Configurations (3.1) ................................................. 14

Copyright (1.4) ........................................................... 4

Design of major parts (3.3) ...................................... 17

Direction of rotation (5.4) ......................................... 41

Disassembly (6.8) .................................................... 51

Disclaimer (1.3) ......................................................... 4

Dismantling (6.8, Disassembly) ............................... 51

Drawings (8) ............................................................ 58

Duty conditions (1.5) .................................................. 4

Electrical connections (4.8) ..................................... 34

End of product life (2.5) ........................................... 14

Examination of parts (6.9) ....................................... 52

Fastener torques (6.6) ............................................. 50

Faults; causes and remedies (7) ............................. 56

Foundation (4.3) ...................................................... 21

General arrangement drawing (8.4) ........................ 67

General assembly drawings (8) ............................... 58

Grouting (4.4)........................................................... 23

Guarding (5.5).......................................................... 41

Handling (2.2) .......................................................... 10

Hydraulic, mechanical and electrical duty (5.10) ..... 46

Impeller clearance (6.7) ........................................... 51

Inspection (6.2.1 and 6.2.2) ..................................... 48

Installation (4) .......................................................... 21

Lifting (2.3) ............................................................... 10

Location (4.1) ........................................................... 21

Lubrication (5.2) ....................................................... 35

Maintenance (6) ....................................................... 47

Maintenance schedule (6.2) .................................... 47

Name nomenclature (3.2) ........................................ 16

Nameplate (1.7.1) ...................................................... 8

Nozzle loads (4.7.2) ................................................. 32

Operating limits (3.4.1) ............................................ 21

Ordering spare parts (6.3.1) .................................... 49

Parts lists (8) ............................................................ 58

Performance (3.4) .................................................... 21

Piping (4.7) .............................................................. 31

Pre-commissioning (5.1) .......................................... 35

Priming and auxiliary supplies (5.6) ........................ 41

Protection systems (4.10) ........................................ 34

Reassembly (6.10, Assembly) ................................. 55

Receipt and unpacking (2.1) .................................... 10

Recommended spares (6.4) .................................. 499

PAGE

Recycling (2.5) ......................................................... 14

Replacement parts (6.3 and 6.4) ............................. 49

Running the pump (5.8) ........................................... 45

Safety action (1.6.3) ................................................... 5

Safety labels (1.7.2) ................................................... 8

Safety markings (1.6.1) .............................................. 5

Safety, protection systems (see 1.6 and 4.10)

Sealing arrangements (3.3.7) .................................. 19

Sectional drawings (8) .............................................. 58

Setting impeller clearance (6.7) ............................... 51

Sound pressure level (1.9, Noise level) ..................... 8

Spare parts (6.3) ...................................................... 49

Specific machine performance (1.8) .......................... 8

Starting the pump (5.7) ............................................ 42

Stop/start frequency (5.7.8) ..................................... 45

Stopping and shutdown (5.9) ................................... 46

Storage, pump (2.4) ................................................. 14

Storage, spare parts (6.3.3) ..................................... 49

Supplementary manuals or info. sources (10) ......... 67

Supplementary User Instructions (10.1) .................. 67

Thermal expansion (4.6.1) ....................................... 30

Tools required (6.5) .................................................. 49

Torques for fasteners (6.6) ...................................... 50

Trouble-shooting (7) ................................................. 56

Vibration (5.7.7) ........................................................ 44

Page 3 of 76 flowserve.com

6

O

e

h

e

m

h

s

a

e

o

i

a

c

a

e

o

r

g

e

o

i

m

o

s

h

m

M

e

c

E

u

x

c

A

o

n

VERTIC

A

N

s

o

c

r

o

c

a

o

a

d

p

o

c

o

T

g

w

e

a

s

n

t

u

d

a

e

w

t

c

o

c

E

F

y

c

h

d

u

e

a

s

w

e

o

s

i

a

f

a

n

.

v

t

e

i

w

a

b

i

d

E

y

t

f

T

y

e

a

t

jury

n

d

f

o

I

a

n

a

e

m

c

t

dengine

e

a

t

z

d

c

e

a

e

d

e

o

s

e

m

A

h

m

s

r

w

a

T

a

i

u

c

M

m

r

o

h

r

s

f

e

s

t

u

e

s

e

o

c

u

t

r

o

s

d

e

u

o

u

o

p

t

p

v

s

a

y

g

S

y

r

A

g

b

n

s

r

H

u

c

s

t

a

d

o

w

o

r

a

u

e

m

o

a

o

h

o

y

t

o

d

c

e

h

u

t

o

a

t

F

4

e

o

k

o

b

s

d

w

n

o

e

t

s

e

y

e

a

o

p

o

r

t

e

b

e

o

h

a

u

o

p

t

u

f

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

1 INTR

Gen

1.1

These

close to th directly wit

Flowserve p manufactur modern facil care and co utilizing sop requirement

Flowserve i improvemen information operation or diagnostic s

These instru familiarizati Operating th instructions service and take into ac regulations installing th activity with safety requi laws and re

DUCTIO

ral

instruction

product's

the produ

oducts are d

d with state-

ities. The un

mitment to isticated qu .

committed t

t and being

bout the pro

about its su

rvices.

ctions are int

n with the pr

e product in

s important t

void risks.

ount local re

re observed

product. Al

perations p

ements and

ulations.

AND SA

must alwa

perating lo

t.

esigned, dev

f-the-art tec

it is produce

ontinuous q

lity techniqu

continuous

t service for

uct in its ins

port product

ended to faci

duct and its ompliance

help ensur

he instructi

ulations; en

by all, includ

ays coordin rsonnel, and pplicable sa

ETY

s be kept

ation or

eloped and

nologies in with great ality control, s, and safet

quality

ny further

tallation and

, repair and

litate permitted us

ith these

reliability in

ns may not

ure such

ng those

te repair

follow all pl

ety and heal

nt

h

.

of tech applic releva To co CE m and th

D1.3

Infor to be all of provi

used.

Flows Intern as cer organi been produ and p parts incorr may a featur install acces failure Flows Flows may i

nical docume

ble this docu

t to these Di firm the Appr rked, check t

Certification

isclaime

ation in the

omplete an

he efforts o

e compreh

ering and

rve manufac

tional Quality

ified and audi

ations. Gen esigned, test ts to help en rformance in

nd accessori ct incorporati

versely affe s of the prod

r use authori ories is consi

caused by mi

rve warranty. rve products

pair the safe

nts and safet

ent incorpo

ectives and

vals applyin

e serial num

. (See sectio

e User Inst

d reliable.

Flowserve

nsive instr

afety practi

ures product

Managemen

ted by extern

ine parts an

d and incorp

ure their cont

use. As Flo

s sourced fr

n of such pa

t the perform

cts. The fail zed Flowserv dered to be suse is not c

In addition, or removal of y of these pr

instructions.

ates informati

pprovals.

and if the pr

er plate mar

9, Certificati

uctions is owever, in

Corporation

ctions, goo

e should al

to exacting System Sta

l Quality Ass

accessories

rated into th

inued produc

serve cannot

m other vend

ts and acces nce and saf re to properl

parts and

isuse. Dam

vered by the

ny modificati original com

ducts in their

Where

on

duct is ings

n.)

elieved

pite of to

ays be

dards urance have

quality

test ors the

ories

ty

select,

ge or

n of onents use.

Thes

installing, equipment equipment the conditi instruction and apply t considered product da misuse are warranty.

CE

1.2

It is a legal r put into servi conform with covering Ma Equipment, Pressure Eq Potentially E

Where appli

pprovals c

machinery a

instruction

perating, u n any regio

ust not be ns relating , have been

e present

to be misus

age, delay

not covere

arking an

quirement th

e within cert the applicabl hinery and,

lectromagne ipment Dire plosive Atm

able the Dire ver important

d equipment

must be re

ing and mai

worldwide put into ser o safety no

met. Failur

ser instruct e. Personal or failure ca

by the Flo

Approv

t machinery

in regions of

CE Marking

here applica

ic Compatibil

tive (PED) an

spheres (AT

tives and an

safety aspec

and the satis

d prior to taining the

The

ice until all

ed in the

to follow

ons is

in

,

sed by

serve

ls

nd equipme

the world sha

Directives le, Low Volta

ty (EMC),

Equipment

X).

additional

s relating to

actory provisi

t

ll

ge

or

n

C1.4

ll rig be rep trans permi

D1.5

This p specifi ackno separ with th

the p there prod Flows

If the are go tempe seeks start u

opyright

ts reserved.

roduced, sto

itted in any f

sion of Flow

uty Con

oduct has b

cations of yo

ledgement

tely to the P

ese instructi

he product rameters s s any doub

ct for the a erve for ad

onditions of

ing to be ch rature or dut

the written a

p.

No part of t

ed in a retrie

rm or by an

erve.

itions

en selected

ur purchase

f these con rchaser. A

ns.

must not b ecified for t as to the s plication in

ice, quoting

ervice on y

nged (for ex

) it is reques

reement of

ese instructi

val system o

means with

o meet the

rder. The itions has b opy should

operated b

e applicati

itability of t

ended, cont

the serial n

ur purchase

mple liquid ed that the

lowserve be

ns may

out prior

en sent

e kept

ond

n. If

e

ct mber.

rder umped, ser

ore

Page 4 of 7

flows

rve.com

6

Safe

t

m

e

d

w

y

c

e

w

o

y

w

c

y

o

e

w

c

s

A

e

n

c

n

o

y

p

A

d

r

g

e

u

ju

n

A

e

o

r

f

o

e

f

e

n

b

r

t

o

k

e

d

o

k

a

f

t

n

w

d

n

a

y

o

n

u

E

s

n

f

k

t

e

s

e

s

t

s

t

s

t

s

o

t

d

p

e

c

o

w

f

d

m

r

T

u

y

g

r

e

s

e

t

I

i

o

N

G

P D

R

p

F

C

m

c

H

p

n

u

p

A

s

e

p

A

e

t

v

m

o

e

m

T

m

e

H

o

e

n

M

y

E

S

E

P

T

f

A

e

a

o

C

t

a

e

E

a

d

h

!

a

e

t

H

h

e

k

d

o

n

S

a

T

R

S

P

o

a

(

t

o

a

T

t

p

o

b

a

h

s

v

y

s

e

a

o

4

e

s

W

E

e

)

s

d

e

w

L

a

e

E

z

p

e

v

s

o

h

a

n

m

v

1.6

1.6.1

Su These User I markings wh cause hazar

instructions risk to perso

This s non-complia could result

This s safety instru personal saf

instructions risk to safe damage the

This s zone markin instructions area would

VERTIC

y

mary of saf

nstructions c

re non-obse

s. The speci

This symb here non-c

nal safety or

mbol indicat nce would af in loss of life.

mbol indicat

tions where

ty and could

This sym

here non-co peration and equipment o

mbol indica

g according t

here non-c

ause the ris

L TURBIN

ty marking

ntain specific vance of an i ic safety mar

l indicates el

mpliance wil

he loss of lif

s safety inst

ect personal

s “hazardou

on-complian

result in los

ol indicates s mpliance will personal saf

property.

es explosive o ATEX. It i

mpliance in

of an explo

PUMPS (V

safety

struction wo ings are:

ectrical safet

involve a hi

.

uctions whe

safety and

and toxic flui ce would affe

of life.

afety involve some

ty and would

atmosphere

used in saf he hazardou ion.

PS) CENTR

used secti

WHE

ld

THE

h

BEFO The a

e

where

When

d”

250 º

ct

elasto conditi conta

Many weari is req heavy

ty

appro curren

IFUGAL PU

n potentiall n 1.6.4 also

NEV

THE UNIT I

UARDS MU

UMP IS OP

RAIN THE

RE DISMAN

propriate sa

the pumped

LUORO-EL

a pump has

(482 ºF), p

ers (examp

on these are

t must be av

ANDLING

recision par g of appropri ired when h pieces abov

riate for the

t local regula

PS ENGLI

explosive

applies.

R DO MAIN

S CONNEC

ST NOT BE

RATIONAL

UMP AND I

LING THE

ety precauti

liquids are h

STOMERS

xperienced

rtial decomp

le: Viton) will

extremely d

ided.

OMPONEN

s have shar

ate safety gl

ndling these

25 kg (55 l mass and in tions.

H 7156922

tmosphere

ENANCE

ED TO PO

EMOVED

OLATE PIP UMP

ns should b

zardous.

When fitted. emperature

sition of fluo

occur. In thi

ngerous an

S

corners an

ves and equ components ) use a cran

ccordance

– 02-15

ORK ER

HILE

WORK

taken

over

ro-

skin

the ipment . To lift

ith

This s remind not t cloth; ensur instructions area would

Th

an important

1.6.2

Per

ll personn inspection a qualified to personnel in necessary k and instructi operator ma to provide a

lways coor health and s safety requi laws and re

1.6.3

Saf

This is a s prevent in environme

mbol is used

rub non-m

the cloth is

here non-c

ause the ris

is sign is not

instruction in

onnel quali

l involved in

d maintena

arry out the

question do

owledge an n must be p commissio

plicable trai

inate repair afety person ements and

ulations.

ty action

mmar

ry to perso t and to eq

of c

in safety ins

tallic surface

amp. It is u

mpliance in

of an explo

safety symb

he assembly

ication and

he operation

ce of the uni

ork involve

not already

skill, appro

rovided. If r

the manufa

ing.

activity with

el, and follo pplicable sa

nditions an

nel and da

ipment. Fo

ructions to

with a dry

ed in safety he hazardou ion.

l but indicat

process.

training

, installation,

must be

. If the

ossess the

riate training

quired the

turer/suppli

perations an

all plant

ety and heal

actions to

age to the products

s

d

r

h

PPLYING H

There

may be occ

been

hrunk fit on t

t to remove

difficul

If you be ap

GRE

Befor liquid thorou to pre This positi impell liquid

Rapid the pu in da avoid

If hot suppli perso

lect to use

lied quickly t

T CARE

applying he

rapped betw

ghly drained

ent an explo

ust be carrie

n. On some

r bore so on

ay drain ou

HERMAL S

changes in t

mp can caus

age or brea d.

OT (and col

r freezing c

s can prese

s entering th

AT TO R E M

sions when t

o the pump

ue to produc

eat to remo

o the impelle

t ensure an en the impe

out through t sion or emis d out with th

pump sizes occasions a

.

OCK

e temperatu

e thermal sh

age of comp

) PARTS

mponents or

t a danger t

e immediate

OVE IMPEL

e impeller h

haft or has b

ts of corrosio

e the impelle

r boss. TAK

residual ha

ller and pum

he impeller k

ion of toxic

shaft in the cavity exist

significant v

re of the liqui

ck, which ca

nents and s

auxiliary he

operators a

area action

ER

s either come

n.

r, it must

ardous

shaft is

yway

apour.

ertical

in the

lume of

d within n result hould be

ting

d ust be

Page 5 of 7

flows

rve.com

6

d

e

g

R

e

s

b

n

ki

l

p

n

o

p

n

w

T

e

t

m

P

a

e

h

A

L

b

VERTIC

A

,

e

o

e

r

a

(

e

n

U

g

p

u

a

e

t

T

u

r

i

H

D

m

e

a

o

e

h

L

o

l

R

g

e

E

o

e

r

g

n

h

i

q

y

h

E

n

d

p

T

r

m

e

o

M

F

w

u

W

m

T

t

a

b

o

d

q

g

L

v

r

N

h

o

n

g

e

w

d

I

r

o

m

M

Av

a

b

T

m

a

1

U

p

n

y

c

e

m

r

e

u

a

s

m

c

e

M

e

u

r

e

n

e

u

o

e

g

d

f

n

s

y

r

a

p

o

i

a

F

o

l

S

g

n

e

p

h

m

l

o

e

A

l

o

e

z

h

p

h

y

t

s

l

n

h

T

e

4

e

a

s

m

p

o

u

n

T

h

e

a

o

t

s

t

m

o

t

D

d

o

h

a

s

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

taken to avo protection is be limited to warnings an immediate a insulated an

If the temp below -5 ºC local re

ula

HAZA When the pu must be tak appropriate access and flammable a must be appl

Gland pac hazardous

PIPE LOAD Do not use mount expa in writing, s acts on the

(See sectio

and shutdo

VALVE PAR (Unless oth User Instruc This is reco overloading zero flow. further open cannot occu need to be the run-up p

start-up, op

WHEN PUM Running the recommend damage to t

id accidental

not possible maintenanc

indicators t

rea. Note: b

drive moto

rature is gre

23 ºF) in a r

tions, actio

DOUS LIQ mp is handlin n to avoid ex

iting of the p

y operator tr

d/or explosiv

ied.

ng must no

iquids.

PREVEN

ump as a su

sion joints,

that their fo

ump flange.

ENSURE

5, Commiss

n.)

START T

LY OPENE

rwise instruc

ions.)

mended to and damagin umps may b

only on inst . The pump

djusted to c

ocess. (Se

ration and s

NEVER R

INLET VA

P IS RUNNIN

pump at zer

d minimum f e pump and

contact. If c the machin

staff only, w

those ente

aring housin

s and bearin

ter than 80

stricted zo

as above s

IDS

hazardous l

osure to the l mp, limiting p ining. If the li

, strict safet

be used w

EXCESSIV

port for pipi

nless allowe

ce, due to int

CORRECT L

oning, startu

E PUMP WI

ted at a spec

inimize the

g the pump

started with llations wher outlet contro

mply with th

section 5, C

utdown.)

UN THE PU

VES TO BE

G

flow or belo ow continuo

mechanical s

mplete

access mus ith clear visu ing the gs must not

s may be h

ºC (175 ºF) o

e, or excee

all be taken.

quids care iquid by ersonnel

uid is

procedures

en pumpin

EXTERNA

g. Do not

by Flowser

ernal pressu

UBRICATIO

, operation

H OUTLET

ific point in t

isk of

otor at full o

the valve

this situati

l valve may

duty followi

mmissionin

P DRY

ULLY OPEN

the

sly will caus eal.

t.

s

e,

e

n

g

l

e

the m cause

a reduction in

the pu

1.6.4

  Pr

event build u event the ge

 Pr

event leakag

 Pr  M

The fo

llowing instr

when i

nstalled in p must For A equip Directi

ve 94/9/EC.

Ex req

uirements e EU m IECEx

, UL.

1.6.4.

appro coupli suitabl specifi

Wher

Flowserve h pump, party r

esponsible fo elect the cou

shall s equip Decla

ation of Conf

the ar

The o cause

additional he

pump

sets with a V motor electri requir

ment still app

tor and caus

p, instability

Products atmosphe

easures ar

oid excess t

intain the p

e followed t

EX, both ele

ent must m

y be require

Scope o

se equipme

riate. Alway

g assembly,

rated and/o

atmosphere

the Ex rating

ent, with the

a in which it

tput from a v

ust state tha

al supply is fr

cavitations.

pump/bearin

and cavitatio

sed in pote

es

required to:

mperature

p of explosiv

eration of s

es

mp to avoid

ctions for pu

tentially exp

help ensure

ctrical and n

et the requir

lways obse

Ex electrica

certified to

complianc

t only in the

check that t

eal and pum

certified for t

in which the

s supplied o

applies only

r assembling

ling, driver a

necessary C

rmity establi

s to be instal

riable freque ting affects in

D, the ATEX

t it is covers t

m the VFD.

ies even if th

Low flow rate

life, overhe

/vibration.

tially explo

mixtures

arks

azard

ps and pu osive atmos explosion pr

n-electrical

ments of E

rve the regio

items outsid

ther than A

one for whic e driver, driv

equipment e classificati

are to be ins

nly the bare

o the pump.

the ATEX pu

nd any additi

E Certificate/

hing it is sui

ed.

cy drive (VF the motor an

Certification f

e situation w

his particular

VFD is in a s

s may

ting of

ive

p units

heres

tection.

ropean

al legal

e the

EX eg

it is

re

n of the

alled.

haft

The

p set

nal

able for

) can so, for

r the

ere

fe area.

DO NOT

BNORMA Operating at rate with no

Page 6 of 7

LY H I GH O

a flow rate hi

ack pressur

UN THE PU

LOW FLO

her than nor

on the pump

MP AT

RATES

al or at a flo

may overloa

flows

rve.com

6

a

1.6.4.2

A

a

n

G

g

e

d

c

d

e

u

v

m

R

e

A

t

u

o

e

t

e

-

o

m

A

i

a

G

e

c

N

e

r

e

U

O

a

o

b

u

d

u

C

t

e

w

E

n

e

c

M

A

t

e

º

t

e

u

x

T

s

d

u

T

)

E

o

r

F

l

I

n

p

f

e

t

e

h

s

t

x

a

m

c

e

s

e

A

m

s

y

g

4

E

A

V

e

p

s

m

r

o

x

o

b

M

s

m

p

s

m

v

t

s

p

r

x

o

a

t

a

f

e

h

a

v

m

n

E

D

o

p

e

h

p

d

h

m

a

S

s

o

t

s

o

m

e

m

e

d

t

e

f

r

t

a

u

n

d

e

p

e

m

u

P

T

o

i

h

d

a

o

r

d

a

s

4

e

g

t

n

d

h

t

a

n

p

n

e

r

t

o

c

a

i

F

s

i

s

t

n

s

a

M

n example below. The engraved o

Equipment I = Mining II = Non-min

Category 2 or M2 = hi 3 = normal l

Gas and/or G = Gas D = Dust

c = Constru

(in accor

Gas Group IIA – Propan IIB – Ethylen IIC – Hydrog

Maximum s (see section

1.6.4.3

A

te

ENSU

CLASS IS S

Pumps hav

TEX Ex ra on a maxim Flowserve f

The surface by the temp maximum p the tempera values in th

Temperature c

to EN13463

T6 T5 T4 T3 T2

* The table only

T1

Pump design may further li

VERTIC

rking

of ATEX equ

ctual classif

the namepl

II 2

roup

ing

h level prot

vel of prote

ust

tional safety

ance with E

(typical)

(typical) n (typical)

rface tempe

1.6.4.3.)

oiding exc

peratures

E THE EQ

UITABLE F

a temperatu

ing on the n

m ambient r higher am

temperature

rature of the

rmissible liq ure class an table that fo

lass

Maxim

1

temperat

85 °C 100 ° 135 ° 200 ° 300 °

akes the ATEX t r material, as we

it the maximum

450 °

L TURBIN

pment marki cation of the te.

D c IIC 135

ction tion

13463-5)

ature (Temp

ssive surfa

IPMENT TE

R THE HAZ

re class as s

meplate. Th

f 40 ºC (104

ient tempera

on the pump

liquid handl

id temperat must not e

lows.

m surface

re permitted

(185 °F) (212 °F) (275 °F) (392 °F) (572 °F) (842 °F)

mperature clas

ll as component

orking temperat

PUMPS (V

g is shown

pump will be

ºC (T4)

rature Class

e

PERATUR

RD ZONE

ated in the

se are base F); refer to ures.

is influenced d. The re depends ceed the

emperature limi

liquid handled

Consult Flowse Consult Flowse

115 °C (239 °

180 °C (356 °

275 °C (527 °

400 °C (752 °

into consideratio

esign or materia re of the liquid.

PS) CENTR

The te due to accou

The o speci excee

Temp liquid install case t pump permit

If an e install rotatio run ti conta

Wher again casing surfac

void using power check

In dirt and re bearin

d

1.6.4.

ND Ensur

n

pipelin during atmos make

t of *

syste

ve

prope

ve

)

If the

)

conditi

) )

(for e

n. ,

To av vapor must

IFUGAL PU

mperature ri

the minimu

t in the tem

erator is re

ied maximu

ded

rature classi

emperature

d in differen

e user is re surface tem ted in the pa

plosive atm

tion, do not

n by starting

e may give

t between ro

there is any t a closed v

external sur

temperatur

mechanical,

otor overlo

monitor and

.

or dusty en move dirt fro g housings a

Preventi

mixture

NSURE TH

ENTED AN

the pump a

e system is t

the pump o

here is prev ure that sea

s and any h

ly filled.

peration of t

on, fit an ap

ample liquid

id potential

or gas to at

e well ventil

PS ENGLI

e at the seal

permitted fl

eratures sta

ponsible t

liquid te

fication “Tx” i

aries and th

hazarous at

ponsible for erature does ticular hazar

sphere exis ttempt to ch

the pump un

high tempe

ating and st

risk of the p lve generati

ace tempera

protection

ydraulic or

d trips, tem

make routin

ironments,

areas aro

nd motors.

the build

PUMP IS

DOES NO

nd relevant s

tally filled w

eration, so t

ented. In ad l chambers,

ating and c

e system ca

ropriate dry

etection or

azards from osphere the

ted.

H 7156922

s and bearin

w rate is tak

ed.

ensure tha perature is

s used when

pump coul

ospheres.

nsuring that

not exceed t

ous atmosp

s during the

ck the direc illed. Even ature resulti

tionary com

mp being ru g high liquid

tures, fit an

evice.

lectrical ove erature moni vibration m

ake regular

nd close cle

p of explos

ROPERLY RUN DRY

uction and di

th liquid at al at an explos

ition it is es

uxiliary shaf

oling system

nnot avoid th

un protectio

power moni

fugitive emis

surrounding

– 02-15

s and

en into

the

ot

the be

In this

the

hat

ere.

ion of short g from

onents.

and

xternal

load by

tor or a

nitoring

hecks

rances,

ve

ILLED

charge

l times

ve ential to seal

s are

is

device

tor).

ions of

rea

Page 7 of 7

flows

rve.com

6

re

e

u

h

p

t

n

r

c

l

e

re

u

h

s

A

m

o

c

e

s

y

e

o

f

a

R

A

X

s

t

e

VERTIC

A

a

t

z

k

a

e

C

s

m

y

c

o

t

u

t

u

o

t

o

E

Z

m

p

i

g

E

o

d

a

u

s

n

p

o

d

y

e

a

e

t

T

t

m

e

h

R

t

r

d

p

T

a

i

d

s

d

u

p

e

T

c

I

s

b

c

u

e

r

U

e

i

t

c

s

d

c

A

n

h

s

M

e

t

d

b

e

a

i

e

M

a

r

e

g

c

p

t

S

n

r

e

m

e

r

d

x

c

n

t

4

e

n

a

n

d

e

,

p

e

U

e

w

e

t

a

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

P

1.6.4.5

To pre

contact, the

To avoid th current gen properly gro

Avoid el

surfaces wit

For ATEX a to comply wi must be mai

Additional non-metalli

When metal metallic bas

1.6.4.6

for which it corrosion re

piping due t which could occur if ther the pump is

Bursting of li must be avo and ancillar

Where ther barrier fluid monitored.

If leakage o hazard, inst

1.6.4.7

RISK OF E

The respon instruction

To avoid po maintenanc materials us

P

The p

void entrap

M

COR

VOID POT

venting sp

vent a poten coupling gua

potential ha rating a spar

nded.

ectrostatic ch

a dry cloth;

plications th

h 94/9/EC.

tained.

equirement

base plate

ic componen

plate they

venting lea

mp must onl

as been app

istance.

ent of liquid

closing of su

ause danger

is heat input

tationary or r

quid containi ided by drain

systems.

is the poten

r external fl

liquid to atm ll a liquid de

intenance t

ECT MAINT ENTIAL HA

PLOSION

ibility for co

is with the

ential explos

, the tools, c

d must not

rks

ial hazard fr

d must be n

ard from ran

, the base pl

rge: do not r

nsure cloth is

coupling mu

orrect coupli

for metallic

ts are fitted

ust be indivi

kage

be used to

oved to hav

in the pump

tion and disc

us excessiv

o the liquid.

nning.

g parts due

ing or protec

ial hazard of

sh, the fluid

sphere can

ection devic

avoid the

NANCE IS

ARDS WHIC

pliance wi

lant operato

on hazards eaning and

ive rise to s

m mechanic

n-sparking.

om induced

te must be

b non-metall

damp.

t be selecte

g alignment

umps on

n a non-

ually earthe

handle liquid

the correct

nd associate

harge valves,

pressures to

his can occ

to freezing

ing the pum

a loss of a s

ust be

result in a

.

azard

EQUIRED

H GIVE A

h maintenan

.

uring

ainting

arking or

l

c

.

r if

al

O

e

adver is a ri must

It is re sched

1.7.1 For d

Confo

these

1.7.2

Oil lub

For p

condit

these are in been shoul Instru

ttenti to the guida and w This i

ely affect th

k from such

e conducted

ommended le is adopte

S1.7

afety La

Nameplat

tails of nam

mity, or sep

User Instruct

Safety lab

ricated units

S1.8

pecific

rformance p

ons. When t

o be incorpo luded here. upplied sep be obtained tions if requi

N1.9

oise Lev

on must be noise, and lo

ce to person

en noise ex

typically 80

ambient co

ools or mate

in a safe are

that a maint

. (See secti

els Sum

plate, see th

rate docum

ons.

ls

only:

achine Pe

rameters se he contract r rated into Us

Where perfo

rately to the and retaine ed.

l

iven to the e

al legislatio

nel on noise

osure reduc

o 85 dBA.

ditions. Wh ials, mainte

a.

nance plan

on 6, Mainte

ary

Declaration

ntation inclu

rformanc

section 1.5 quirement s

er Instruction

mance data

purchaser th

with these

posure of p

will define

limitation is r

ion is mand

re there

ance

nd

ance.)

of

ed with

Duty

ecifies s these has

se

ser

rsonnel

hen

quired,

tory.

Page 8 of 7

flows

rve.com

6

p

n

e

o

d

p

f

a

n

u

c

e

i

v

m

l

e

a

c

n

o

a

e

d

o

e

o

t

e

VERTIC

A

t

f

o

r

t

a

l

t

a

e

p

w

.

c

p

w

s

e

a

s

a

s

y

E

x

y

n

e

n

u

k

f

l

e

o

d

a

d

w

r

e

d

(

u

t

u

e

o

s

r

i

e

r

T

e

n

a

h

s

n

d

s

o

h

e

n

I

r

S

E12

223344455

S

e

i

e

m

e

s

d

e

M

r

s

M

0180

s

0180

s

0180

s

0

s

0180

s

0180

s

0180

s

0180

s

0

s

0180

s

0180

s

0

s

0

s

m

o

a

w

S

u

s

A

P

s

e

a

i

a

p

s

4

e

H

A

n

A

-

s

0

2

4

8

0

2

5

0

8

.

8

.

7

.

8

.

7

e

5

e

d

n

-

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

The usual a the noise or emitted sou limiting nois however if n attention is indication of take the ap

Pump noise operational acoustic ch values give cannot be g

Similarly the motor” noise and high effi the pump. N show an incr

If a pump un your own dri table should obtained fro noise specia the values.

It is recomm the prescrib should be m

The values (3.3 ft) from over a refle

For estimati add 17 dBA

Th extracted fr data/catalog motor noise are not guar depending u The combin could excee adding mot total noise l values listed combined n Actual on-si recommend accordingly.

proach is to

to enclose th

d. You may

level when

noise requi

rawn to the

equipment n

ropriate acti

level is depe

actors, flow

racteristics o are subject

aranteed.

motor noise

is that typical

iency motors

ote that a mo

ased noise

t only has be

er then the “

be combined

the supplier

ist if assistan

ended that w

d limit, then

ade.

re in sound the machine, ting plane”.

g sound po

to the sound

e noise level

m typical mo ue to provid values at no

nteed. The

pon the test

d noise leve

the values

rs with simil

vel. Therefo above is req

ise levels of

e noise mea

d and safet

control the e e machine to

have alread he equipme

ements wer

ollowing tabl

ise level so

n in your pla

dent on a n

ate, pipewor

the building

o a 3 dBA to

ssumed in th

y expected fr when on loa or driven by t some spee

n purchased

ump only” no

ith the level

Consult Flo

e is required

here exposu site noise m

ressure lev

for “free fiel

er level LWA

pressure val

shown in ta

or manufact the average load for refer

values could

nd surround

of the pump

hown. It is t r noise level re, the dB co uired to obta motor and th

urement by

measures a

posure time

reduce

specified a

t was ordere defined, th

to give an

that you can

t.

mber of

design and

, and so the

erance and

“pump and m standard

directly drivi

n inverter m s.

for fitting with ise levels in t for the driver

serve or a

in combining

e approache

asurements

l LpA at 1 m

conditions

re 1pW) the

e.

ble 1.9.1 are

rer’s

expected

nce only an

vary

ing condition

and the mot

be noted th

increases t

rection to th

n the

pump.

xperts is

e to be take

to

d, n

g

y

e

at

e

. r

1.9.1

1.10

For p

condit

requir perfor includ been shoul requir

Typical ve and Solid

M

otor

F

ame

ize.

N

MA

80 36

1200 &

10 36

1200 &

50 36

1200 &

80 36

1200 &

20 36

1200 &

60 36

1200 &

00 36

1200 &

40 36

1200 &

49 18

1200 &

000

1200 &

800 36

6

8

1200 &

800 18

1200 &

000 18

1200 &

pecific

rformance, p

ons. Whene

ment to inc

ance into U

d here. In c upplied sep be retained

d.

rtical motor

hafts)

So

RP

0 70 0 60

lower 55 0 70 0 60

lower 55 0 75 0 70

lower 60 0 75

18

0 70

lower 60 0 75 0 65

lower 65 0 75 0 65

lower 65 0 80 0 70

lower 70 0 85

lower 80

36

0 90 0 85

lower 80 0 90 0 90

lower 80 0 90

lower 85 0 90

lower 85

achine pe

arameters s ver there is

rporate spec

ser Instructio

ses where

rately to the

with these U

noise data (

nd

Pres

ure

(dB

)

(W

- I

enclo

ure)

.0 78. .0 68. .0 63. .0 78. .0 68. .0 63. .0 83. .0 78. .0 68. .0 83. .0 78. .0 68. .0 84. .0 74. .0 74. .0 84. .0 74. .0 74. .0 89. .0 79. .0 74. .0 90. .0 80. .0 80. .0 97. .0 92. .0 102 .0 97. .0 92. .0 103 .0 103 .0 93. .0 103 .0 98. .0 104 .0 99.

rformanc

e section 1. contract fic machine

ns, those ar

erformance

purchaser, th

er Instructio

Sou Pow (dB

(WP

enclo

ollow

d

er

) I

ure

8

7 7

9

7

, Duty

ata has

e same

s, if

Page 9 of 7

flows

rve.com

7

s

a

f

m

c

w

b

c

e

d

e

t

n

m

c

o

g

e

a

Y

VERTIC

A

N

r

v

t

p

r

n

t

m

u

r

p

c

s

n

c

o

n

e

p

t

g

s

D

E

A

d

m

p

h

n

t

m

g

b

n

e

b

d

5

n

t

a

e

T

b

n

h

e

s

b

e

I

d

a

e

o

g

e

t

s

PDL

p

u

d

r

M

n

o

s

y

c

a

e

o

e

d

(

l

f

e

p

S

f

c

e

m

d

p

i

s

5

g

s

o

&

4

e

h

s

v

b

e

b

e

H

A

H

M

)

3(1

3

1

5

6

a

s

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

2 TRAN

Con

2.1

Immediately checked ag documents been no da or damage Flowserve a of receipt of accepted.

Check any accessories separately walls of the

Each produ this number always quot as when ord

Han

2.2

Boxes, crat using fork lif size and co

SPORT A

ignment

after receipt inst the deli

or its comple

age in trans

ust be repo d received i

the equipme

rates, boxes

or spare par ith the equip

ox or equip

t has a uniq

corresponds

this numbe

ering spare

ling

s, pallets or vehicles or struction.

D STOR

eceipt an

of the equip ery and ship

eness and t

ortation. A

ted immedia

writing with

t. Later clai

and wrappin s which may

ent or attac

ent.

e serial num with that adv in correspo arts or furth

artons may lings depen

GE

unpackin

ent it must

ing

at there has

y shortage a

ely to

n one month

s cannot be

s for any

be packed

hed to side

er. Check t

ised and

dence as w

r accessorie

e unloaded

ent on their

g

e

at

ll

.

d

of the disch secur

the c throu

2.3.2

Cast d recom that h are at of the

Do

discharge he

rge heads u

d by slings t

mpletely as

h this flang

Lifting of t pump atta

ischarge he

mended to b

ad size (ref ached as sh sling from th

" L "

ot use the li

ad while liftin

less the dis

prevent ov

embled pu

e.

ype-W cast

hed

ds with pum

lifted by usi

r to the table

wn maintain shaft end a

30

ting pins at t g unassembl harge head i

rturning. Ne

p with eye

ischarge h

attached ar

ng pins suita

shown). Th ng minimum

shown in th

mm (12 in.)

e base

ed cast

er lift

olts

ad with

le with

slings

length

detail.

IN.

Lifti

2.3

Equip lifted by me must carry regulations.

Before liftin manufactur

2.3.1

Lifti

(he

Lift the unas not attached the flange m shaft into pl

g

ent in exce

hanical mea

ut lifting, in a

the driver al r’s instructio

ng of W-typ

d only-pum

sembled cas ) by installin ounting hole

ce.

CAST HEAD UNASSEMBLE

E BOLTS

E

s of 25Kg (5

s. Fully trai

cordance wi

ne, refer to

s.

cast disch

not attach

discharge h eyebolts as

. Lower the

lbs) should ed personn

th local

he

rge head

d)

ads (pump shown using head over

CAST

e

WITH P

l

TTAC

EAD

UMP

ED

“L”

2.3.3

If the head in the metho with o

Cast hea

100

(4) 25

in

ia.

(1)

1220

L

(48)

is approximate

Lifting of or without

ump is suppl se 2 point or

etails provid

is applicabl

without the

s with dischar

150

(6)

32

1.25)

1370

(54)

ength

200

(8) 32

(1.25)

1370

(54)

abricated di

the pump

ied with a fab

3 point meth

d in 2.3.3.1 to the lifting

ump.

e size mm (in.

250 (10)

32

(1.25)

1520

(60)

charge hea

ricated disch

d of lifting a

2.3.3.2. Th

of discharge

00

2) 8

(

.5)

1

20

(

0)

ds with

rge

shown

is

heads

Page 10 of

6

flows

rve.com

7

w

e

0

2

0

h

s

VERTIC

A

n

,

a

d

<

t

d

F

T

E

t

(

m

c

L

R

T

F

m

W

N

T

g

0

I

p

n

s

o

x

p

u

n

e

ohe

s

As

M

b

s

i

t

p

i

e

y

h

m

S

b

e

m

n

d

f

b

e

w

4

e

n

p

b

h

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

2.3.3.1

T

h wi

"L"

Fabric

Pin Dia.

Weight <23

2.3.3.2

T

di wi

o point lifti

ad types TF

hout pump

ted heads with

1

0-200

(4-8)

3

(1.25)

0 (5000)

ree point lif

charge hea

hout pump

of fabrica

UF & HFH

attached)

FABRICATED 2 POINT LIFTI

ischarge size m

250-600

(10-24)

38 (1.50)

4500 (10000)

ing of fabri

of type HF

attached)

ed dischar

with or

ITH

G

50

m (2in.) HOLE

(in.)

<6800 (1500

ated

(with or

700-900

(28-36)

44 (1.75)

e

2.3.4 Clam for lifti sump/

Lifting of

the bowl as

g and lower uction barre

owl assem

embly and c

ng the asse

l.

ly only

nter the lifti

bly into the

g hook

a) L

e a

b) B

a n

c) C

d) In e)

wer the bowl tensions res propriate su

ild the very f d lower the xt column se

ntinue to bui ad assembl

tall the disc

semble the

assembly u on the foun

ports). rst section o ntire assem

ction. ld until it is r .

arge head.

otor.

til the clamp

ation (use

the column ly to assem

ady for disc

iping,

le the

arge

Example:

Lifting of bo

l assembly

)

Page 11 of

6

H

L STYLE FAB

WI

H 3 POINT LI

ICATED

TING

flows

rve.com

7

Lifti

e

p

e

b

s

f

s

r

t

m

o

A

n

r

h

t

r

o

l

s

m

t

a

E

a

g

r

.

u

o

s

e

o

T

e

I

M

4

e

2.3.5 Suction barr supplied se sump first. I suction barr the suction barrel for in prevent the movement.

Example: Li

VERTIC

ng of suctio

l (also refer

arately and

nstall eyebol

l and attach

arrel to a ve

tallation. Pr

uction barre

ting of suctio

L TURBIN

barrel

ed as ‘Can’)

as to be inst

s on the flan

slings and st

tical position

vide hand s

from swayin

barrel

PUMPS (V

is always

lled into the e of the

aps to bring Move the pport to

g during

PS) CENTR

IFUGAL PU

PS ENGLISH 7156922

– 02-15

SUCTION BARREL (CAN)

Lifti

2.3.6 If the pump i adequately places befo and moved shown. Sa pulled out fr

ng of fully a

s fully asse

trapped and e it can be lif o the installa

e rules are m the sump

sembled p

bled, it has t supported at ed from the

ion site. Se pplicable wh and moved t

location.

Page 12 of

6

mps

be least two hipping crat details

n the pump

another

is

flows

rve.com

VERTICAL TURBINE PUMPS (VTPS) CENTRIFUGAL PUMPS ENGLISH 71569224 – 02-15

Pump must be supported at least two places when lifted. Do not use chains to wrap around.

Two (2) cranes are required

Examples shown here are for illustration only. See section 2.3 1~2.3.6 for specific lifting instructions based on design variations. The pumps vary in weight, length and physical appearances from the types shown here.

Therefore, before lifting is attempted, exercise caution to prevent any injuries or loss of life.

Pump must be supported at least two places when lifted.

Do not use chains to wrap around.

Page 13 of 76 flowserve.com

7

a

c

e

n

d

p

t

a

s

d

"

e

w

s

o

t

c

s

m

g

h

r

y

A

f

l

d

m

t

a

t

a

VERTIC

A

p

i

c

m

e

r

v

t

a

n

R

a

l

s

a

s

e

s

u

t

o

w

l

a

s

o

c

r

o

h

o

E

e

i

t

T

n

a

o

t

h

s

t

r

p

m

b

n

d

e

t

a

r

t

o

d

o

e

d

e

T

p

s

n

t

e

t

a

o

h

e

m

e

I

n

t

D

d

e

n

m

a

s

h

e

c

a

s

a

n

d

M

m

v

e

s

e

t

a

r

t

r

c

s

p

y

S

s

q

e

d

i

d

s

m

u

p

s

n

a

4

e

,

p

h

v

p

y

o

e

c

e

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

Stor

2.4

location aw connection foreign mat at frequent i bearings an

2.4.1

Ins

a) Inspect

on the v necessa

b) Inspect

connecti covers deposits

c) If neces

as note shipped securely

d) Exercis

Contain coated coating, element

2.4.2

Sh Follow the s storage spa excess moi corrosive fu

Driver stora manufacture

2.4.3

Lon If a situation than 6 mont storage inst

ge

Store the y from vibrat overs in pla rial out of pu

tervals to pr the seal fac

ection befo

he preservati

rious parts.

ry.

ll covers ove ons. If found nd inspect in

of foreign m

ary, clean a above to res condition.

.

caution with

rs are not le

ith a residua

which will wa

.

rt term stor

eps given in

e so that the

ture, extrem

es, or other

e instruction

r’s User Instr

g term or ex

arises for a l

s) please c

uctions and

ump in a cl

on. Leave p

e to keep dir

p casing.

vent brinelli

es, if fitted, fr

e storage

e coating/p

Touch up the

r pump openi

damaged, re

eriors of the

terials or wa

d preserve t

tore the part

eplace cover

pumps expo

k proof. Par

amount of p

h away if ex

ge (up to 6

ection 2.4.1.

unit will not

weather co

harmful con

: Check driv

ctions

ended stor

ng-term sto

ntact Flowse

arranty rela

an, dry ping and other urn the pum

g of the

om sticking.

inted surface

areas, If

ngs and pipi

ove the

pening for a

er.

e interior par

to the "as

and fasten

ed to weath s may be otective

osed to

onths)

Select a

e subjected

ditions, itions.

r

ge

age, ( more

ve for speci

ed informati

g

y

s

r.

o

l

n.

perso specifi regula

3

Shoul Flows serial is sta disch separ reque both t numb

VTPs, (b) su built w applic wells, applic and le shaft

al protective cations must tions at all ti

ESCRIPTI

questions a rve pump di

umber to b

ped on a m

rge head as

te nameplat

ting informa

e driver seri

r for Flowse

C3.1

onfigura

are enginee

tion barrel ( ith customer

tions such a

storm water

tions. The

gth, whethe

esigns and t

equipment i be in accord

es.

ON

rise concerni

ision will re

of assistanc

tal nameplat embly. The

attached to

ion on the dr

l number an

ve represent

ion

ed pumps a

an) type pu specific feat s water pum

ervice, indu

umps vary i

r it is an ope

pe of disch

used. The s

ance with th

ng the pump

uire the com

. The serial e affixed to t driver will ha

it. If you are ver, please

the pump s ative.

:(a) Wet pit t

ps. Most pu

res and for

ing stations, trial and cry size, impell

shaft or en rge head us

afety

current

lete number e e a

rovide

erial

pe and

mps are

deep genic r types

losed

d.

Rec

2.5

t the end o parts, the re recycled or acceptable product con environmen of in accord includes the or other utili

toxic fluids

Page 14 of

cling and

the service

evant materi

isposed of u

ains substan , these shoul

nce with cur

liquids and

ies.

Ma

ke sure that re disposed

6

ethod and l

End of Pr

ife of the pro

ls and parts ing an envir

cal regulatio

es which ar

d be remove

ent regulatio

r gases in th

azardous su

f safely and

duct Life

uct or its

should be

nmentally

s. If the

harmful to t

and dispos

ns. This also

"seal syste

bstances or that the corr

e

d

ct

"

flows

rve.com

7

m

3.1.1

A

E

R

A

B

A

T

I

T

p

m

N

m

n

s

t

o

s

m

c

e

M

a

A

m

t

c

m

5

o

t

c

o

S

T

o

n

t

G

S

i

l

5

s

w

g

o

4

e

A

n

K

&

o

1

e

s

n

w

i

r

a

Su

VERTIC

p and deep

L TURBIN

well VTP

PUMPS (V

PS) CENTR

3.1.2

IFUGAL PU

Suction b

PS ENGLI

rrel (Can) V

H 7156922

P

– 02-15

DRIVER

DISCHA HEAD

SSEM

COLUMN

SSEMBLY

BOWL

SSEMBLY

GE

DRIVER

LY

DISCHARGE HEAD

SSEMBLY

COLUMN

SSEMBLY

BOWL

SSEMBLY

SUCTION BARREL (CAN)

3.1.3 The V are ty asse

EM, E

The i desig detail (6 in) terms inche

Most com

P configura

ical for varie

bly types su

, EP, EQ, S

peller model

ated separat

) and the pu o 1300 mm ( of nominal b

.

on VTP m

ions shown i

y of VTP mo h as EB, E

K, SL, SN,

s in each of t ely (see sect

p sizes cou

2 in.). The

wl diameter

dels

sec 3.1.1 a

dels with the

, EH, EJ, E P, SR, ST,

hese pumps

on 3.2 for m d vary from

ize express

and is alway

d 3.1.2

bowl

, EL,

AV.

are

re

50mm

d is in in

ts will not req

ases, the bo the dischar

have single

uire a colum

l assembly

e head. Ve

r multiple st

s

tical

ges.

asse conne turbin

Some uni

bly. In such

ted directly t

pumps can

Page 15 of

6

flows

rve.com

7

e

a

t

w

p

A

E

,

d

e

n

c

a

c

a

8

m

g

c

-

d

r

d

e

s

a

VERTIC

A

m

s

e

n

S

o

d

c

2

a

e

b

e

t

w

v

E

e

r

E

o

a

o

…

b

c

g

a

s

g

T

s

I

1

a

F(Ty

F

M

h

s

a

y

s

t

S

h

e

p

t

e

4

e

u

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

Nom

3.2

The pump si the namepl attached to

nclature

ze/ serial nu te typically a he discharg

3.2.1

Bo

l assembly

Nominal Bo

l Diameter-i

Impeller Ty

=Axial, E=

e (A or E or

nclosed, S=

Bowl Model B,J,K,H,L,M

Types

N,P,Q,R,T,V

Impeller Mo L, M, H, Y…

el Designati

..

No. of Stag

The typical to the VTP actual pump nameplate. nameplate

s

omenclature

onfiguration

size and ser The driver wi ttached it.

Dis

3.2.2 Consists of Examples:

harge head

lphanumeri W16, 10HF

10 HF 20

No

inal driver b

Dischar

e head type

Nominal dis

harge diam

W = Cast head HF = Fabricate TF & LF = Fab UF = Fabricate HFL = Fabricat HFH = Fabricat

for horizontal a

head for abov

icated heads wi

head for belo d head for abo

ed head for abo

Please see and identific

ection 3.2.2.

tion.

ber will be

below: Th

head assem

omenclatu

12

ches

)

Semi-open

….

n

above is the

escription. I

ial number fr

ll have a sep

nomenclatu

code as foll

0, 6TF16,…

se diameter

(see details

ter in inches

ove the ground the ground dis h base flange

ground dischar

e ground disch

e the ground di

1 for dischar

ngraved on nameplate i bly.

e

J H-3

general guid

dentify the

m the pump

rate

re

ws.

.

in inches

elow)

discharge

harge

e

rge - Low H.P

charge -High H

e head type

e

.P.

3.2.2. Typic

a) W

b) H

c) T

Types of

l discharge

type cast di

type fabric

pically with

type fabrica

discharge

ead types. D

charge head

ted discharg

quare base

ed discharg

eads

etails (a) thr

head

plate)

head

(g).

Page 16 of

6

flows

rve.com

7

f

l

A

a

e

VERTIC

A

f

s

u

s

d

E

e

m

d

a

T

I

F

1

o

u

e

A

e

s

a

o

c

d

o

r

c

a

s

m

s

M

c

h

a

g

d

c

e

s

m

v

e

i

e

t

u

d

s

S

r

s

a

y

a

c

t

d

h

b

v

h

e

c

e

m

e

4

e

t

h

e

u

o

t

a

s

o

n

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

d) LF type

(Typical

lso av

e) UF type

abricated di

y with a circ

ilable with s

fabricated di

charge head

lar base plat

ction barrel

charge hea

- ANSI type. ounting)

g) H

3.2.2. and c config pleas or ord

H type fabri

The disc

(a) thru (g)

upling arran

ration of the

refer to the

r specific se

ated discha

arge heads

re for illustr

ements var

pump that h

rawings sup tionals from

ge head

hown in sec tion only. T . For the act

s been purc

plied with th

Flowserve.

ion e shaft

ual

hased,

pump

f) HFL typ

fabricated

ischarge he

d

D3.3

esign of

Please r

numb

3.3.1

motor manu categ

a) H throug conne of the

b) S and pr type d conne

3.3.2 (See The di asse in mo

r equivalent

vari

ty of drivers are most co l, all types of ries.

llow shaft dri

h a tube in th

ted to the dr

river.

lid shaft driv

ojects below

iver requires

ting to the p

lso section 3.

charge hea bly as well a t cases.

Drivers

Discharge

Major Par

fer to appen

ay be used,

mon. For t

drivers can

ers: where t center of th

ver by a clut

rs: where th he driver-mo

an adjustabl

mp.

Head Asse

2.2.1) supports th supplying a

s

ix for Europ

however, ele e purposes

e grouped in

e head shaf

rotor and is

h assembly

rotor shaft i

unting base.

coupling for

bly

driver and b

discharge co

mp part

ctric

f this

o two

extends

t the top

solid This

wl nection

Page 17 of

6

flows

rve.com

7

A

e

b

e

b

c

u

a

e

h

y

c

d

s

d

u

a

o

VERTIC

A

e

y

b

n

b

u

m

e

f

u

h

o

E

d

e

m

o

d

m

c

s

y

a

0

h

g

e

a

z

i

d

T

t

h

n

e

I

e

c

n

o

e

c

n

e

a

s

e

o

M

m

i

r

m

e

r

i

p

d

s

n

a

r

a

R

S

d

a

e

m

p

s

o

a

h

w

e

4

e

m

d

r

y

c

e

y

o

a

[

a

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

shaft seali discharge h liquid cham

The shaft s seal assem or a tube-pa

Col

3.3.3 The column connects th and carries t Houses and bearings. T

a) flanged

ng arrangem

ad to seal th

er.

al will usuall

ly or stuffing

king box wit

mn assem

ssembly co

bowl assem

e pumped fl

supports the

pical column

olumn asse

nt is locate

e shaft at its

be either a box with an

an enclose

ly

sists of colu

ly to the dis id to the dis

haft and ma

assemblies

bly

in the

xit from the

echanical

pen lineshaf

lineshaft.

n pipe, whic

harge head

harge head.

contain

re:

See s exact size a specifi

ctional draw olumn asse d configurat

c order requi

ings supplie

bly details

on vary dep

rements and

with the pu s per the or nding upon t application c

p for

er. The

he

iteria.

3.3.4 The b mount motor. vanes requir part d

Bowl asse

wl assembly

d on the pu

Impellers ar

and are gen

ments. See tails.

mblies

consists of i

p shaft cou

cast wheel

rally coated t

section 8.0 f

pellers rigidl led to an ele with multipl

o meet the h

r cross secti

tric

diffuser

draulic nal and

3.3.5 VTPs foreig strain applic are fa attach are pr attach

Suction st

an also be f

particles fro

rs and the m

tion. Exam

tened [422]

d using clip

vided with i

it to the mai

rainers

tted with str

m entering t

esh size dep

les are sho

irectly to th

[421]. Con ternal or ext assembly.

iners [316] t e pump. The

ends on the

n below. Str suction bell

shaped str rnal threads

prevent

type of

iners

55] or

iners

to

a)

Slip-on str

iner

b) threade mm (4~14 in

The column

a) Open lin

pumped

b) Enclose

tube aro fluid to l

The shafts stud design

column ass

.) sizes only.

upports sha

eshaft constr

to lubricate t

lineshaft c

und the lines

bricate the li

re threaded

r clamp ring

mbly: from 1

t assembly, t

ction utilizin

e lineshaft b

Or

nstruction h

haft and utili

neshaft bear

r key couple design.

0 mm~355

at is either

the fluid bei

arings.

s an enclosi

es oil or oth

ngs.

with thrust

b)

Clip-on st

SUCTION

CAP SC

STRAIN

ainer

BELL (55)

CLIP (421)

EW (422)

ER (316)

c)

Cone (thre

ded) straine

r

g

r

Page 18 of

6

flows

rve.com

7

s

e

u

e

t

c

i

f

n

s

g

VERTIC

A

e

o

e

t

c

d

o

h

2

i

r

E

s

d

c

a

q

p

n

x

e

g

x

w

T

h

d

e

s

o

s

w

b

I

1

y

a

o

1

s

C

5

C

M

s

g

p

W

S

g

h

r

s

4

e

g

e

a

n

R

G

XSTU

N

)

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

d) Bolt on

3.3.6

Imp VTP’s are s impeller typ capacity typ VTP applica to match ea finish to ach are dynamic shaft by a ta

Stu

3.3.7 Some VTPs cases, stuffi working pre stuffing box

3.3.7.2

Hi

This type of packing with

trainer

llers

pplied with s. Impellers

designed f ions. Impell h order and

eve hydrauli ally balance pered lock c

fing box

are fitted wit

g boxes are

sures up to

ser Instruct

h pressure

packing box two lantern

nclosed, or are low, me r maximum

rs are cast

o provide re

characterist

and held in

llet or split ri

stuffing bo

normally ad

0.7 bar (300

ons for speci

stuffin

bo

s fitted on to ings and allo

emi open

ium and hig overage of a nd machine

uired surfac

ics. Impeller

osition on th g and key.

es. In such

quate for

psi). Refer t

fications.

an open line

s grease lu

3.3.7. This t linesh used

3.2.2.

(17) PA

ll

e

(13) PA

haft for pres

rication.

Low pre

pe of packin

ft for pressu

nly on W-ty

to see for

KING GLAND

(354) STUD

(35

) HEX NUT

KING SET

sures up to 2

sure stuffin

box is fitted

res less than

e discharge

type discha

0 bar (300 p

box

on to an op

6.5 bar (100 eads (see S

ge head det

SLI

HE

O-RI

STUFFIN

PRESSU REDUCIN BUSHING

i) uses six ri

n psi) and

ection

il).

GER (3 46

D (326A

NUT (327A)

NG (347)

BOX (83)

E

(117

gs of

Page 19 of

6

flows

rve.com

7

x

e

c

l

VERTIC

A

s

f

w

E

n

e

n

T

s

h

I

n

M

5

e

S

s

a

4

e

d

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

3.3.7.4

E

In cases wh pressure stu

tra high pre

re the press

ffing box is u

sure stuffi

res are exp

ed.

box

cted to cros

20 bar (300

psi) up to 6

bar (1000 p

i), extra high

-

3.3.8 Me

VTP’s can a the time of c

hanical sha

so be fitted

ontract.

t seal

ith a mecha

ical seal. T

e requireme

t to fit the m

chanical se

l to be provi

ed at

Page 20 of

6

flows

rve.com

7

Acc

A

o

s

g

a

e

d

b

m

w

g

a

A

m

y

p

x

a

m

o

w

o

e

o

u

t

p

F

n

o

A

d

n

e

a

e

d

m

e

a

e

c

d

e

o

n

c

.

o

p

h

n

e

u

o

E

f

i

e

n

y

o

r

+

0

m

o

e

u

o

c

o

e

a

t

o

l

v

h

e

r

a

p

T

a

s

n

r

e

I

u

t

o

t

s

a

o

hup

h

hwil

han

p

s

nagclu

nag

s

c

e

c

p

d

o

M

o

e

t

a

s

k

y

d

a

p

n

a

l

d

t

a

d

A

E

Alwa

e

S

e

t

h

p

y

p

m

w

s

e

s

a

q

l

c

h

k

z

r

m

a

o

e

u

B

m

p

4

e

a

m

h

a

m

u

e

m

l

t

m

o

h

e

d

n

m

a

e

3.3.8 ccessories

customer.

Perf

3.4

This product specification

The followin help with the temperature, data. If requi application c

Op

3.4.1

Pumped liqui limits*

Maximum am temperature*

Maximum pu

*Subject to Special desi pumps oper limits. Cont available for

4 INST

Equip must compl regulations.

otentially e

Loc

4.1

When equip months, a c accordance located to all maintenanc lifting and sh supply of liq arrangemen

4.1.1

Ins Six months Flowserve P employed to and the facili noticed, the may require equipment i some comp

VERTIC

essories

may be fitte

rmance a

has been sel

of the purch

data is includ installation. It

materials and

ed, a definitiv n be obtaine

rating limits

temperature

ient

p speed

ritten agree

ns and mat ting above ct Flowserv

your specifi

LLATION

ent operate

with the rel

See section

plosive atm

tion

ent has bee

mplete inspe

ith section 2

w room for a

and inspecti

uld be as cl

id to be pum

drawing for t

ection prior

rior to the sc

mp Division

conduct an i

ty. If any det

lowserve P

a partial or c

cluding resto nents.

L TURBIN

when speci

d Operat

cted to meet

se order. S

ed as additio

is typical and

seal type ma

statement f

from Flowse

5 ºC (40 ºF) to

Up to +40 ºC (1

refer to the na

ent from Fl

rials may be

nd below th

for upgrade

application.

in hazardo

vant explosi

1.6.4, Produ

spheres.

in storage f

tion should b

4.3. The pum

ccess, ventila

n with ample

se as practic

ed. Refer to

e pump set.

to installati

eduled insta

representati

spection of t

rioration of

mp Division

mplete dism

ration and re

PUMPS (V

ied by the

on Limits

the e section 1.5.

al information factors such

influence thi r your particul ve.

80 ºC (176 ºF)

4 ºF)

eplate

wserve.

available for

se specified

options

s locations

n protection

ts used in

r greater tha

conducted i p should be tion,

headroom fo

ble to the he general

n

lation date, a

e is to be

e equipment

quipment is

epresentativ

ntling of the lacement of

PS) CENTR

The p ventila headr practic

Refer

to

dimen

s

4.2.1

ar

The fo actual

a) M

b) C

c) C d) C

e) C

three should neces

 O

6

male shaft avoid

conne impro to the

pump depen vibrati

IFUGAL PU

P4.2

reparati

mp should b

ion, mainten

om for lifting

able to the su

o the general

ions and det

General in

llowing chec

installation.

ke sure that

p

wer supply s

eck the sum

.

eck the liqui eck the inst

ll safely hand

eck all pum

y shipping a

laces when

be attempte

ary for a suc

hollow shaf

ainst the sh

tch

solid shaft

ainst the cou

haft threads onnection. d.

ting driver to

er motor dire

ump.

F4.3

oundatio

units to their ds on the siz

n limitations

PS ENGLI

n

located to al nce and insp

nd should b

pply of liquid

arrangement

ils.

stallation c

s should be

motor name

stem match

p depth and

level in the

llation equip

le the pump

connection

d handling r

Alw

ys support

ifting or inst

without ade

cessful instal

drivers, che

ft size, whic

rivers, chec

pling bore si

pp

ly thread lub only at the ti

xcess lubric

ys check m pump. Res ction can ca

n/Anchor

The

re are many

foundations.

of the pum . Non-compl

H 7156922

low room for

ection with a

as close as

o be pumped

drawing for t

eck-list

made before

late ratings

correctly.

ump length

sump.

ent to be s

eight and si

(bolts, nuts

lated proble

hafting in at lling. No ins

uate equip

ation.

k the clutch

must go thr

the motor s

e

icant sparing

e of making

nt should b

tor rotation b rve rotation se extensive

olts

ethods of i

The correct

unit, its loc

iance with th

– 02-15

ccess,

ple

.

e pump

starting

nd the

atch-

re that it

ze.

tc) for

s.

east

allation

ent

size

ugh the

aft size

ly to

up

fore ue to damage

stalling

ethod

tion and

Page 21 of

6

flows

rve.com

7

c

r

e

u

l

m

v

a

t

s

m

A

n

f

a

n

t

e

c

A

I

T

VERTIC

A

p

w

s

a

l

e

f

e

s

n

t

u

m

a

m

E

c

t

h

t

d

f

n

v

e

d

s

d

c

u

y

u

A

N

T

r

c

d

h

o

g

I

x

u

d

m

o

m

o

l

y

e

o

d

n

L

i

s

7

h

a

d

c

a

S

D

2

M

y

m

c

d

g

i

a

e

n

3

m

s

c

e

o

b

a

t

h

c

3

e

u

E

S

r

n

w

7

m

e

t

h

0

t

n

p

o

t

e

i

t

e

6

m

o

e

f

m

7

e

4

e

h

p

o

t

u

0

t

b

e

g

n

s

t

n

u

0

o

d

n

e

n

o

0

i

t

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

provision of lead to failu outside the t

The foundati rigid support expected str

Concrete fo installed in s holes in the below. Slee moldable m

When a suc type "TF" di provide per motor.

base, they to grouting.

lways shim the leveling done otherw the structura separation o

recommend industry sta

Detail of a

MOUNTING PL

FOUNDA

NON-BOND

MOLDABLE MA

4.3.1

Lev

dis

orrect found e of the pum erms of the

on must con

to the discha

sses that m

ndations sho eeves that al

ounting plat

e should be

terial after sl

ion barrel is charge head,

anent, rigid

If leveling

ust be backe

near founda

uts. Now tig

se there is a

l natural freq

the base fro

All found

tions should

dards.

ypical found

TE

ION

NG

ERIAL

ling of pu

harge head

ation and ins

and, as su

arranty.

ist of materia

rge head and

y be encoun

uld have anc

ow alignmen

as illustrate

illed with no

eve is set in

upplied as in the suction

upport for th

uts are use

off as far a

ion bolts and

ten the foun

risk of signifi

ency that co

the grout.

tion / anchor

be verified b

tion bolt, gro

ps mounted

flange

tallation may h, would be

that will affo

will absorb

ered in servi

or bolts

and have

in the detail

-bonding

place.

the case of t essel must

pump and

to level the possible pri

then back off

ation bolts.

antly lowerin

ld result in

bolt

prevailing

ted.

NCHOR BOLT

UT

GROUT

on the

If

d

e.

e

r

E

DI

HEA

37

373

The p aligne asse precisi the m flange

0.16 the gr

Check is still torque record

friendl requir

4.3.2

The s aligne by usi level. mount needs using least Reche after t install pit an the sol Check respe in./ft) should

ample of a t

CHARGE FLANGE

CONCRET

mp assembl

with the an

bly is levele

on machinist

tor mountin

mounting su

m/m (0.002

ut to set for

to make sur

evel to withi the nuts [37 ed for future

Directly

for service.

s re-leveling

Leveling o soleplate

leplate [23] i

with the an g a master l evels should

ng surfaces. to be leveled

hims and gr

2~80 hours

ck the solepl

e grout is se tion. Lower t

align the dis eplate bolts[

to make sur

t to the solep nd final torq

be recorded

pical discha

ounting fla

y [101] is lo

hor bolts [3

by using a

's level. Lev

flange. The

rface needs

n./ft) using s

t least 72~8

that the mo

0.16 mm/m ]. The leveli

reference.

ounted pum

Re-installati

and re-grou

f pumps mo

first lowered hor bolts. Th

vel or a prec be taken on The soleplat

to within 0.1

ut. Allow the

efore the pu

te mounting

and then pr

e pump ass

harge head 72]. that the pu

late to within

e the nuts [3

for future ref

ge head wit

ge

ered into the 2]. The pum

aster level

ls should be

discharge he

o be leveled

ims and gro

hours.

or mounting

(0.002 in./ft)

g data is to

s are not us

on of these p

ing.

unted on a

into the pit a

soleplate is

sion machini

he equipme mounting s mm/m (0.0

grout to set f

p is installe

surface level

ceed with th

mbly [101] i

lange bolt h

p is still level

0.16 mm/m ( 3]. The level rence.

the

101

pit and

r a

aken on ad to within

t. Allow

flange

and final

e

r

umps

routed

d

leveled

t's

t rface 2 in./ft)

r at

.

ess pump

to the

les to

with

.002

ng data

Page 22 of

6

flows

rve.com

7

p

e

a

e

(

s

a

h

0

e

a

VERTIC

A

m

s

w

h

e

s

n

u

s

c

e

a

o

t

g

q

o

E

s

d

e

a

r

m

w

e

s

r

T

e

o

e

h

o

p

I

o

i

n

r

a

s

e

u

A

t

e

m

a

c

p

0

i

m

e

A

a

u

d

e

M

o

s

e

u

t

e

a

o

d

e

a

u

o

n

u

a

d

w

g

w

m

u

e

c

S

h

s

d

s

c

o

q

u

t

h

t

o

n

s

u

o

d

v

4

e

a

u

e

i

b

d

s

0

l

s

u

e

v

m

3

e

t

h

o

s

L TURBIN

PUMPS (V

PS) CENTR

IFUGAL PU

PS ENGLI

H 7156922

– 02-15

Exam

4.3.3

Lev

The suction and aligned flange is lev precision m the equipm flange moun

0.16 mm/m the grout to pump is inst surface leve proceed wit assembly [1 discharge h [372].

Check to m respect to th (0.002 in./ft) leveling dat

Example of

le of pump

ling of pu

barrel [315] i

ith the anc

led by using

chinist's lev nt mounting ting surface

0.002 in./ft) et for at lea

lled. Reche

lness after th

the pump in

1] into the b

ad flange b

ke sure that

e barrel flan

and final tor is to be rec

pump install

ounted on a

ps with the

first lowere

or bolts. The

a master lev

l. Levels sho

urfaces. Th eeds to be l

sing shims

t 72~80 hou

k the barrel

grout is set

stallation. Lo

rrel and alig

lt holes to th

he pump is

e to within 0.

ue the nuts [

rded for futu

ed with a suc

soleplate

uction barr

into the pit suction barr

el or a

uld be taken

suction barr

veled to wit nd grout. All s before the

ounting

and then

er the pum

n the

flange bolts

till level with

16 mm/m 373]. The

e reference.

tion barrel.

l

in

w

l

n l

4.3.4

The s and al suctio ancho solepl using Level surfac needs

in./ft)

llow the pu surfac proce asse disch [372].



Che

res

(0.

level

Exa

Leveling o mounted

leplate [23] i

igned with th

barrel [315]

bolts. Torq

te. The suc

master lev

should be t

s. The sucti

to be levele

sing shims

he grout to s

mp is install

levelness

d with the p

bly [101] int

rge head fla

k to make s

ect to the b

02 in./ft) an

ng data is to

ple of pump

f pumps wit

n a soleplat

first lowere anchor bolt

into the pit a

e nuts to se ion barrel fla l or a precisi

ken on the e

n barrel flan to within 0.1

and grout

et for at leas

d. Recheck t fter the grou

mp installati

the barrel a

ge bolt hole

re that the p rrel flange to final torque be recorded

ith a suction

soleplate

suction b

e

onto the fo . Then, low

nd aligned w

ure suction

nge is levele

n machinist'

uipment mo

ge mounting

6 mm/m (0. nder the so

72~80 hour

e barrel mo

is set and th

n. Lower th d align the to the flang

mp is still le

within 0.16 the nuts [37

for future ref

barrel moun

rrel

ndation

r

ith the

arrel to by

level.

unting

surface

02

eplate.

before

nting

en

pump

bolts

el with

m/m

]. The

rence.

ed on a

Page 23 of

6

G4.4

routing

Wher

applicable,

fter

dding pipe the co shoul engin Flows

pling align then be gro ering practic

rve service

rout in the f ork connecti ent, the mou

ted in accor

e. If in any d

enter for ad

undation bol

ns and re-c

nting plate/s

ance with g

oubt, please

ice.

flows

s.

ecking

leplate od

contact

rve.com

Flowserve VTP, VPC User Instructions

Specifications and Main Features

Frequently Asked Questions

User Manual