vt – vertical tray deaerator · vt=vertical tray (see front cover for additional series) 93-6009...

2
V V V T T T D D D e e e a a a e e e r r r a a a t t t o o o r r r SPECIFICATION SHEET HS Series Up to 350,000 #/hr Low Headroom Performance Fill in and send to Kansas City Deaerator or request a detailed specification sheet. Add additional thermal cases as needed. 80 ITEM DESCRIPTION ACC PKG PUMP PKG SELECT M BFP RECIRC M1 BFP Recirc Shutoff NA OPT M2 BFP Recirc Check NA OPT M3 BFP Recirc Orifice NA OPT BFP Recirc ARC Valve NA OPT M4 BFP Recirc Piping NA OPT M5 BFP Recirc Pressure Gauge NA OPT N BFP SUCTION N1 BF Pumps (2) 100% Capacity NA STD (3) 50% Capacity NA OPT Motors ODP NA STD TEFC NA OPT N2 BFP Suction Isolation Valve NA STD N3 BFP Suction Strainer NA STD N4 BFP Suction Piping NA STD N5 BFP Suction Expansion Joint NA STD N6 BFP Discharge Pressure Gauge NA OPT N7 BFP Discharge Check Valve NA OPT N8 BFP Discharge Isolation Valve NA OPT O CHEMICAL FEED O Chemical Feed Quill OPT OPT Q OVERFLOW Q1 Overflow Valve/Trap STD STD Q3 Overflow Piping OPT STD R LEVEL SWITCH R1 Level Switches High & Low (TWO) STD STD High High (ADDITIONAL) OPT OPT R2 Level Switch Bridle Piping OPT STD S GAUGE GLASS S1 Gauge Glass Red Line Pyrex STD STD Reflex OPT OPT Magnetic OPT OPT S2 Gauge Glass Bridle OPT STD ITEM DESCRIPTION ACC PKG PUMP PKG SELECT A WATER INLET A1 Inlet Valve Mechanical STD STD Pneumatic OPT OPT A2 Level Controller STD STD Level Transmitter OPT OPT A3 Inlet Valve Bypass Valves OPT STD A4 Inlet Valve Bypass Piping OPT STD A5 Inlet Valve Bypass Strainer OPT STD B STEAM CONTROL B1 Steam PRV OPT Self Contained OPT OPT Pneumatic OPT OPT B2 Steam PRV Controller OPT OPT B3 Steam PRV Bypass Valves OPT OPT B4 Steam PRV Bypass Piping OPT OPT B5 Steam PRV Bypass Strainer OPT OPT C RELIEF VALVE C1 Relief Valve Sentinel STD STD Full OPT OPT C2 Relief Valve Exhaust Piping OPT OPT D THERMOMETER D1 (2) 5" Thermometer w/ss wells STD STD E PRESSURE GUAGE E1 (1) 4 1/2" Pressure Gauge STD STD E2 Siphon & Cock STD STD E3 Pressure Transmitter OPT OPT F VENT F1 Vent Valve STD STD F2 Vent Orifice w/Flange OPT OPT F3 Vent Bypass Valves OPT OPT F4 Vent Bypass Piping OPT OPT H VACUUM BREAKER H1 Vacuum Breaker STD STD Tray - .005 cc/l – 7PPB Standard Deaerating Units K K A A N N S S A A S S C C I I T T Y Y D D E E A A E E R R A A T T O O R R Corrosion in boiler cycles is caused by the presence of non-condensable gases such as oxygen and carbon dioxide in the boiler feed water. In order to remove the non- condensable gases, the feedwater is heated and vigorously scrubbed by a counter current flow of steam. The incoming undeaerated water enters the deaerator through spring-loaded, stainless steel, spray valves. These variable orifice valves produce a fine spray in a uniform pattern from 5% to 200% of design. The fine droplets of water maximize the surface area in contact with steam, raising the temperature to within a few degrees of saturation temperature and instantly releasing the majority of the corrosive, non-condensable gases. The preheated and partially deaerated water flows through the tray stack where the hottest, purest steam vigorously scrubs the water to heat it to saturation temperature and strip the last traces of dissolved gases. The entire deaeration process takes place in a stainless steel enclosure that eliminates any need for vessel lining or cladding and ensures a long life with little maintenance. VT – Vertical Tray Deaerator Standard Vertical Tray Deaerator Principles of Operation Vertical Tray Model (VT) Deaerator Guaranteed performance over wide load swings Rugged design with “Central Station” durability Quiet operation Capacities up to 200,000 #/hr with 100% makeup, 250,000 #/hr with condensate Oxygen removal to 0.005 cc/liter (7ppb) Per HEI Certified ASME construction Options: a. Accessory Package b. Accessory Piping c. BF Pump Package d. Heat Exchange Institute (HEI) Design FEATURES Kansas City Deaerator Company 6731 West 121 st Street, Overland Park, KS 66209 Tel (913) 338-2111 Fax (913) 338-2144 Website: www.deaerator.com Email: [email protected] OPERATING CONDITIONS Operating Pressure FEEDWATER INLET % Makeup MU Temperature %Condensate Cond. Temperature STORAGE CAPACITY Minutes at Overflow Gallon at Overflow Accessories Select package or individual items TC Series Up to 250,000 #/hr Tray Unit Meets HEI BDS Series Up to 250,000 #/hr Tray Unit Meets HEI DS Series Up to 800,000 #/hr Tray Unit Meets HEI VS & VT Series Up to 800,000 #/hr Tray Unit Minimal Plan Area Meets HEI HH Series Up to 16,000,000 #/hr Tray Unit-Meets HEI SPECIAL REQUIREMENTS HEI Post Weld Heat Treatment Minimum Radiography WFMP Testing BF PUMPS Quantity Capacity TDH PROJECT DEAERATOR Quantity Capacity DESIGN ASME SEC. VIII, DIV.1 Design Pressure Full Vacuum Design Design Temperature Corrosion Allowance Copyright © January 2004

Upload: vuongxuyen

Post on 12-May-2018

214 views

Category:

Documents


0 download

TRANSCRIPT

VV V TT T DD D

ee e aa aee e rr r

aa a tt too o rr r

S

PECI

FICAT

ION S

HEET

HS

Serie

s U

p to

350

,000

#/h

r Lo

w H

eadr

oom

Per

form

ance

Fill

in a

nd s

end

to K

ansa

s C

ity D

eaer

ator

or r

eque

st a

det

aile

d sp

ecifi

catio

n sh

eet.

Add

add

ition

al th

erm

al c

ases

as

need

ed.

80

ITEM

D

ESC

RIP

TIO

N

ACC

PKG

PUMP

PK

G √

SE

LECT

M

B

FP R

ECIR

C

M

1 B

FP R

ecirc

Shu

toff

NA

O

PT

M

2 B

FP R

ecirc

Che

ck

NA

O

PT

M

3 B

FP R

ecirc

Orif

ice

NA

O

PT

BFP

Rec

irc A

RC

Val

ve

NA

O

PT

M

4 B

FP R

ecirc

Pip

ing

NA

O

PT

M

5 B

FP R

ecirc

Pre

ssur

e G

auge

N

A

OP

T

N

BFP

SU

CTI

ON

N1

BF

Pum

ps

(2

) 100

% C

apac

ity

NA

S

TD

(3

) 50%

Cap

acity

N

A

OP

T

M

otor

s

OD

P N

A

STD

TEFC

N

A

OP

T

N2

BFP

Suc

tion

Isol

atio

n Va

lve

NA

S

TD

N

3 B

FP S

uctio

n St

rain

er

NA

S

TD

N

4 B

FP S

uctio

n Pi

ping

N

A

STD

N5

BFP

Suc

tion

Expa

nsio

n Jo

int

NA

S

TD

N6

BFP

Dis

char

ge P

ress

ure

Gau

ge

NA

O

PT

N

7 B

FP D

isch

arge

Che

ck V

alve

N

A

OP

T

N8

BFP

Dis

char

ge Is

olat

ion

Valv

e N

A

OP

T

O

CH

EMIC

AL

FEED

O

Che

mic

al F

eed

Qui

ll O

PT

O

PT

Q

O

VER

FLO

W

Q

1 O

verf

low

Val

ve/T

rap

STD

S

TD

Q

3 O

verf

low

Pip

ing

OP

T S

TD

R

LEVE

L SW

ITC

H

R

1 Le

vel S

witc

hes

H

igh

& L

ow (T

WO

) S

TD

STD

Hig

h H

igh

(AD

DIT

ION

AL)

O

PT

OP

T

R2

Leve

l Sw

itch

Brid

le P

ipin

g O

PT

STD

S G

AU

GE

GLA

SS

S1

G

auge

Gla

ss

R

ed L

ine

Pyre

x S

TD

STD

Ref

lex

OP

T O

PT

M

agne

tic

OP

T O

PT

S2

G

auge

Gla

ss B

ridle

O

PT

STD

ITEM

D

ESC

RIP

TIO

N

ACC

PKG

PUMP

PK

G √

SE

LECT

A

W

ATE

R IN

LET

A1

Inle

t Val

ve

M

echa

nica

l S

TD

STD

Pneu

mat

ic

OP

T O

PT

A

2 Le

vel C

ontr

olle

r S

TD

STD

Le

vel T

rans

mitt

er

OP

T O

PT

A

3 In

let V

alve

Byp

ass

Valv

es

OP

T S

TD

A

4 In

let V

alve

Byp

ass

Pipi

ng

OP

T S

TD

A

5 In

let V

alve

Byp

ass

Stra

iner

O

PT

STD

B

STEA

M C

ON

TRO

L

B1

Stea

m P

RV

O

PT

Se

lf C

onta

ined

O

PT

OP

T

Pneu

mat

ic

OP

T O

PT

B

2 St

eam

PR

V C

ontr

olle

r O

PT

OP

T

B3

Stea

m P

RV

Byp

ass

Valv

es

OP

T O

PT

B

4 St

eam

PR

V B

ypas

s Pi

ping

O

PT

OP

T

B5

Stea

m P

RV

Byp

ass

Stra

iner

O

PT

OP

T

C

REL

IEF

VALV

E

C1

Rel

ief V

alve

Sent

inel

S

TD

STD

Full

OP

T O

PT

C

2 R

elie

f Val

ve E

xhau

st P

ipin

g O

PT

OP

T

D

THER

MO

MET

ER

D

1 (2

) 5"

Ther

mom

eter

w/s

s w

ells

S

TD

STD

E PR

ESSU

RE

GU

AG

E

E1

(1) 4

1/2

" Pr

essu

re G

auge

S

TD

STD

E2

Siph

on &

Coc

k S

TD

STD

E3

Pres

sure

Tra

nsm

itter

O

PT

OP

T

F VE

NT

F1

Ve

nt V

alve

S

TD

STD

F2

Vent

Orif

ice

w/F

lang

e O

PT

OP

T

F3

Vent

Byp

ass

Valv

es

OP

T O

PT

F4

Ve

nt B

ypas

s Pi

ping

O

PT

OP

T

H

VAC

UU

M B

REA

KER

H1

Vacu

um B

reak

er

STD

S

TD

Tray

-.0

05 c

c/l –

7PPB

Stan

dard

D

eaer

atin

g U

nits

KK AA

NN SSAA SS

CCII TT

YY DDEE AA

EE RRAA TT

OO RR

Cor

rosi

on in

boi

ler c

ycle

s is

cau

sed

by th

e pr

esen

ce o

f non

-con

dens

able

gas

es s

uch

as o

xyge

n an

d ca

rbon

dio

xide

in

the

boile

r fe

ed w

ater

. I

n or

der

to r

emov

e th

e no

n-co

nden

sabl

e ga

ses,

the

fee

dwat

er is

hea

ted

and

vigo

rous

ly s

crub

bed

by a

cou

nter

cur

rent

flo

w o

f ste

am.

The

inco

min

g un

deae

rate

d w

ater

en

ters

th

e de

aera

tor

thro

ugh

sprin

g-lo

aded

, st

ainl

ess

stee

l, sp

ray

valv

es.

Thes

e va

riabl

e or

ifice

val

ves

prod

uce

a fin

e sp

ray

in a

uni

form

pa

ttern

from

5%

to 2

00%

of d

esig

n.

The

fine

drop

lets

of w

ater

max

imiz

e th

e su

rface

are

a in

co

ntac

t with

ste

am, r

aisi

ng th

e te

mpe

ratu

re to

with

in a

few

deg

rees

of s

atur

atio

n te

mpe

ratu

re

and

inst

antly

rele

asin

g th

e m

ajor

ity o

f the

cor

rosi

ve, n

on-c

onde

nsab

le g

ases

.

The

preh

eate

d an

d pa

rtial

ly d

eaer

ated

wat

er fl

ows

thro

ugh

the

tray

stac

k w

here

the

hotte

st, p

ures

t ste

am v

igor

ousl

y sc

rubs

the

wat

er to

hea

t it t

o sa

tura

tion

tem

pera

ture

and

stri

p th

e la

st tr

aces

of d

isso

lved

gas

es.

The

entir

e de

aera

tion

proc

ess

take

s pl

ace

in a

sta

inle

ss s

teel

enc

losu

re t

hat

elim

inat

es

any

need

fo

r ve

ssel

lin

ing

or

clad

ding

an

d en

sure

s a

long

lif

e w

ith

little

m

aint

enan

ce. VT

– Ve

rtica

l Tra

y Dea

erat

or St

anda

rd V

ertic

al T

ray

Dea

erat

or

Prin

cipl

es o

f Ope

ratio

n

Ver

tical

Tra

y M

odel

(VT)

Dea

erat

or

G

uara

ntee

d pe

rform

ance

ove

r wid

e

l

oad

swin

gs

R

ugge

d de

sign

with

“Cen

tral S

tatio

n”

dura

bilit

y

Qui

et o

pera

tion

C

apac

ities

up

to 2

00,0

00 #

/hr w

ith 1

00%

m

akeu

p, 2

50,0

00 #

/hr w

ith c

onde

nsat

e

Oxy

gen

rem

oval

to 0

.005

c

c/lit

er (7

ppb)

Per

HE

I

Cer

tifie

d A

SM

E c

onst

ruct

ion

O

ptio

ns:

a.

Acc

esso

ry P

acka

ge

b.

Acc

esso

ry P

ipin

g c.

B

F P

ump

Pac

kage

d.

H

eat E

xcha

nge

Inst

itute

(H

EI)

Des

ign

FEA

TUR

ES

1

Kan

sas

City

Dea

erat

or C

ompa

ny

6

731

Wes

t 121

st S

treet

, Ove

rland

Par

k, K

S 6

6209

Tel

(913

) 338

-211

1 F

ax (9

13) 3

38-2

144

W

ebsi

te: w

ww

.dea

erat

or.c

om E

mai

l: in

fo@

deae

rato

r.com

OPE

RATI

NG C

ONDI

TION

S

Ope

ratin

g Pre

ssur

e

FEE

DWAT

ER IN

LET

%

Mak

eup

M

U Te

mper

ature

%Co

nden

sate

C

ond.

Temp

eratu

re

S

TORA

GE C

APAC

ITY

M

inutes

at O

verflo

w

Gall

on at

Ove

rflow

Acc

esso

ries

– S

elec

t pac

kage

or i

ndiv

idua

l ite

ms

TC S

erie

s

Up

to 2

50,0

00 #

/hr

Tray

Uni

t M

eets

HE

I

BD

S Se

ries

Up

to 2

50,0

00 #

/hr

Tray

Uni

t M

eets

HE

I

DS

Serie

s U

p to

800

,000

#/h

r Tr

ay U

nit

Mee

ts H

EI

VS &

VT

Serie

s U

p to

800

,000

#/h

r Tr

ay U

nit

Min

imal

Pla

n A

rea

Mee

ts H

EI

HH

Ser

ies

Up

to 1

6,00

0,00

0 #/

hr

Tray

Uni

t-Mee

ts H

EI

SPE

CIAL

REQ

UIRE

MENT

S

HEI

Pos

t Weld

Hea

t Tre

atmen

t

Mini

mum

Radio

grap

hy

W

FMP

Testi

ng

BF

PUM

PS

Q

uanti

ty

Cap

acity

TDH

PRO

JECT

DEA

ERAT

OR

Q

uanti

ty

Cap

acity

DES

IGN

A

SME

SEC.

VIII,

DIV

.1

Des

ign P

ress

ure

F

ull V

acuu

m De

sign

D

esign

Tem

pera

ture

C

orro

sion A

llowa

nce

Cop

yrig

ht ©

Jan

uary

200

4

VT=

Vert

ical

Tra

y (S

ee fr

ont c

over

for a

dditi

onal

serie

s)

93-

6009

(1

0 Min

utes

Stor

age)

0

45=4

5,00

0 #/

HR

(U

se ac

tual

capa

city

, cha

rts sh

ow m

axim

um ca

paci

ty)

M=M

echa

nica

l o

r P=P

neum

atic

(L

eave

blan

k for

none

) P

=Pip

ing

Incl

uded

O

=Pip

ing

Not

Incl

uded

P

KG

=Pac

kage

(L

eave

blan

k for

none

) 2

= #

of P

umps

0

94 =

Flo

w(G

PM)

150

= H

ead(

PSI)

VV V TT T DD D

ee e aa aee e rr r

aa a tt too o rr r

MOD

ELS

SS EE

RR IIEE SS

-- -

SS S

II I ZZ ZEE E

CC

AA PPAA CC

II TTYY

TY

PE

PI

PED

#

/PUM

PS

FLOW

HEAD

SELE

CTIO

N CHA

RT

10 M

inut

es St

orag

e

SE

LECT

ION C

HART

10

Min

utes

Stor

age

5 M

inut

es St

orag

e

DA

M

OD

EL

Boi

ler

Cap

acity

(HP)

Rat

ed

Cap

acity

(#

/HR

)

Stor

age

to

Ove

rflo

w

(Gal

lons

)

Stor

age

Cap

acity

(M

inut

es)

Vess

el

Dim

ensi

on

(L1

x W

1x H

1)

Wat

er

Inle

t “A”

(in

)

Stea

m

Inle

t “B

” (in

)

Empt

y W

eigh

t(lb

s)

Ope

rate

Wei

ght

(lbs)

Floo

ded

Wei

ght

(lbs)

T

otal

A

cces

sory

(L2

x W

2x H

2)

Pum

p Pa

ckag

e (L

3 x

W3x

H3)

VT3

2-30

06-1

0 29

0 4,

000

93

10

3’0”

x2’7

” x

7’9”

1

3 1,

300

3,00

0 4,

000

6’6”

x5’9

” x9

’3”

6’9”

x2’1

1”

x2’1

0”

VT3

2-35

08-1

0 58

0 10

,000

27

0 10

3’

6”x2

’11”

x

9’11

” 1.

5 6

1,70

0 5,

000

7,00

0 6’

10”x

7’7”

x11’

11”

7’6”

x3’3

” x2

’10”

VT3

2-40

08-1

0 72

5 15

,000

35

3 10

4’

0”x3

’4”

x 10

’1”

2 6

2,10

0 7,

000

9,00

0 7’

1”x8

’3”

x12’

1”

8’0”

x3’8

” x3

’0”

VT3

2-45

08-1

0 87

0 20

,000

44

6 10

4’

6”x3

’8”

x 10

’4”

2 6

2,40

0 8,

000

12,0

00

7’4”

x8’6

” x1

2’3”

8’

0”4’

0”

x3’0

VT3

2-50

08-1

0 1,

159

25,0

00

539

10

5’0”

x4’1

” x

10’1

0”

2 6

2,70

0 10

,000

14

,000

7’

7”x9

’4”

x12’

9”

8’4”

x4’5

” x4

’0”

VT5

0-55

08-1

0 1,

449

30,0

00

681

10

5’6”

x4’5

” x

11’0

” 2.

5 8

3,10

0 12

,000

17

,000

7’

7”x1

0’2”

x12’

6”

9’3”

x4’9

” x3

’6”

VT5

0-60

08-1

0 1,

739

40,0

00

811

10

6’0”

x5’2

” x

11’3

” 2.

5 8

3,30

0 14

,000

20

,000

7’

10”x

10’6

”x1

2’9”

10

’6”x

5’4”

x3

’6”

VT9

3-60

09-1

0 2,

029

50,0

00

1,02

2 10

6’

0”x5

’2”

x 12

’3”

3 8

3,60

0 16

,000

23

,000

8’

3”x1

1’2”

x13’

9”

10’6

”x5’

4”

x3’6

VT9

3-60

10-1

0 2,

319

60,0

00

1,23

4 10

6’

0”x5

’2”

x 13

’3”

3 10

4,

000

18,0

00

25,0

00

8’3”

x11’

2”x1

4’9”

10

’6”x

5’4”

x3

’6”

VT9

3-65

10-1

0 2,

609

70,0

00

1,44

7 10

6’

6”x5

’7”

x 13

’5”

3 10

4,

400

20,0

00

29,0

00

8’3”

x11’

5”x1

4’11

” 11

’5”x

5’9”

x3

’6”

VT1

22-6

512-

103,

188

90,0

00

1,94

3 10

6’

6”x5

’7”

x 15

’5”

4 10

5,

100

24,0

00

34,0

00

8’3”

x12’

10”

x18’

8”

12’0

”x5’

9”

x4’5

VT1

22-7

012-

103,

768

100,

000

2,25

5 10

7’

0”x5

’11”

x

15’7

” 4

12

5,90

0 29

,000

40

,000

8’

6”x1

3’1”

x18’

10”

11’7

”x6’

1”

x4’1

1”

DA

M

OD

EL

Boi

ler

Cap

acity

(HP)

Rat

ed

Cap

acity

(#

/HR

)

Stor

age

to

Ove

rflo

w

(Gal

lons

)

Stor

age

Cap

acity

(M

inut

es)

Vess

el

Dim

ensi

on

(L1

x W

1x H

1)

Wat

er

Inle

t “A”

(in

)

Stea

m

Inle

t “B

” (in

)

Empt

y W

eigh

t(lb

s)

Ope

rate

Wei

ght

(lbs)

Floo

ded

Wei

ght

(lbs)

T

otal

A

cces

sory

(L2

x W

2x H

2)

Pum

p Pa

ckag

e (L

3 x

W3x

H3)

VT3

2-30

06-0

5 58

0 8,

000

93

5 3’

0”x2

’7”

x 7’

9”

1.5

6 1,

400

3,00

0 4,

000

6’6”

x5’9

” x9

’3”

7’0”

x2’1

1”

x2’1

0”

VT3

2-35

08-0

5 1,

159

25,0

00

270

5 3’

6”x2

’11”

x

9’11

” 2

6 2,

000

6,00

0 7,

000

6’10

”x8’

7”x1

1’11

” 8’

6”x3

’3”

x3’1

0”

VT5

0-40

08-0

5 1,

449

30,0

00

353

5 4’

0”x3

’4”

x 10

’1”

2.5

8 2,

400

7,00

0 10

,000

6’

10”x

9’5”

x11’

7”

8’6”

x3’8

” x4

’0”

VT5

0-45

08-0

5 1,

739

40,0

00

446

5 4’

6”x3

’8” x

10

’4”

2.5

8 2,

700

8,00

0 12

,000

7’

1”x9

’9”

x11’

10”

8’6”

x4’0

” x4

’0”

VT9

3-50

08-0

5 2,

319

50,0

00

539

5 5’

0”x4

’1”

x 10

’10”

3

10

3,20

0 11

,000

15

,000

7’

9”x1

0’8”

x12’

4”

9’0”

x4’4

” x4

’0”

VT9

3-55

08-0

5 2,

899

60,0

00

681

5 5’

6”x4

’5”

x 11

’0”

4 10

3,

400

12,0

00

18,0

00

7’4”

x12’

4”x1

2’10

” 9’

6”x4

’9”

x5’6

VT9

3-60

08-0

5 3,

478

75,0

00

811

5 6’

0”x5

’2”

x 11

’3”

4 12

3,

900

15,0

00

21,0

00

7’7”

x12’

7”x1

3’0”

9’

6”x5

’4”

x5’6

VT1

22-6

009-

054,

058

100,

000

1,04

0 5

6’0”

x5’2

” x

12’3

” 4

12

4,30

0 17

,000

23

,000

7’

7”x1

2’7”

x14’

0”

10’9

”x5’

4”

x3’6

VT1

49-6

010-

054,

638

120,

000

1,23

4 5

6’0”

x5’2

” x

13’3

” 4

12

4,70

0 19

,000

26

,000

7’

7”x1

2’7”

x15’

0”

11’1

”x5’

4”

x3’6

VT1

84-6

510-

055,

217

140,

000

1,44

7 5

6’6”

x5’7

” x

13’5

” 6

14

5,50

0 22

,000

30

,000

9’

8”x1

2’6”

x16’

8”

Con

sult

Fact

ory

VT2

09-6

512-

056,

377

170,

000

1,94

3 5

6’6”

x5’7

” x

15’5

” 6

14

6,20

0 26

,000

35

,000

9’

8”x1

3’5”

x18’

8”

Con

sult

Fact

ory

VT2

46-7

012-

057,

536

200,

000

2,25

5 5

7’0”

x5’1

1”

x 15

’7”

6 16

6,

900

30,0

00

41,0

00

9’11

”x13

’8”

x18’

10”

Con

sult

Fact

ory

VV V TT TDD D ee e

aa a ee err r aa a

tt t oo orr r

CH

ART

Mode

l Num

ber S

elec

tion

Ser

ies

Size

C

apac

ity

Typ

e P

ipin

g

PK

G

#/ Pu

mps

Flo

w

Hea

d

DEA

ERA

TOR

A

CC

ESSO

RIE

S

STA

ND

& P

UM

P/PA

CK

AG

E

EE E XX XAA A

MM MPP P LL L

EE E :: :

V

T

9 3

6 0

0 9

-- 0

4 5

--

M

O

--

P

K G

--

2

--

0 9

4 -

- 1

5 0

_

_

_ _

_ _

_ _

_ _

_

_

_

_

_ _

_

_ _

_

_

_ _

Typi

cal A

rrang

emen

t