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HS
Serie
s U
p to
350
,000
#/h
r Lo
w H
eadr
oom
VS D
eaer
ator
SP
ECIFI
CATIO
N
P
erfo
rman
ce –
Fi
ll in
and
sen
d to
Kan
sas
City
Dea
erat
or o
r req
uest
a d
etai
led
spec
ifica
tion
shee
t. A
dd a
dditi
onal
ther
mal
cas
es a
s ne
eded
.
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
Spra
y - 0
.005
cc/
l –7P
PB
Stan
dard
D
eaer
atin
g U
nits
KK AA
NN SSAA SS
CCII TT
YY DDEE AA
EE RRAA TT
OO RR
Ka
nsas
City
Dea
erat
or S
pray
dea
erat
ors
prov
ide
an e
cono
mic
al a
ltern
ativ
e to
tra
y ty
pe
units
. Th
e un
its fe
atur
e a
sim
ple,
trou
ble-
free,
qui
et d
esig
n an
d ar
e de
sign
ed fo
r con
stan
t loa
ds.
Inco
min
g un
deae
rate
d w
ater
ent
ers
the
Dea
erat
or t
hrou
gh s
prin
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
pat
tern
from
5%
to
200%
of d
esig
n.
Th
e fin
e dr
ople
ts o
f w
ater
max
imiz
e th
e su
rface
are
a in
con
tact
with
ste
am,
rais
ing
the
tem
pera
ture
tow
ithin
a fe
w d
egre
es o
f sat
urat
ion
tem
pera
t ure
and
inst
antly
rel
easi
ng th
e m
ajor
ity
of t
he c
orro
sive
, no
n-co
nden
sabl
e ga
ses.
Th
e pr
ehea
ted
and
parti
ally
dea
erat
ed w
ater
is
chan
nele
d th
roug
h a
colle
ctio
n ba
sin
dow
ncom
er,
thro
ugh
a to
rtuou
s pa
th
seco
nd
stag
e de
oxyg
enat
or.
Her
e th
e ho
ttest
, pu
rest
ste
am v
igor
ousl
y sc
rubs
the
wat
er t
o he
at i
t to
the
sa
tura
tion
tem
pera
ture
and
stri
ps th
e la
st tr
aces
of d
isso
lved
gas
es.
The
stea
m a
nd n
on-c
onde
nsab
les
flow
upw
ard
into
the
sta
inle
ss s
teel
ven
t co
nden
sing
ar
eaw
here
the
stea
m is
con
dens
ed w
ith th
e in
let w
ater
and
the
gase
s ar
e re
leas
ed to
atm
osph
ere
thro
ugh
the
vent
out
let.
The
dea
erat
ed w
ater
then
falls
to th
e st
orag
e ar
ea.
VS –
Verti
cal S
pray
Deae
rato
r
St
anda
rd V
ertic
al S
pray
Dea
erat
or
Prin
cipl
es o
f Ope
ratio
n
Spr
ay M
odel
(VS
) Dea
erat
or
Lo
w C
ost
S
mal
l foo
tprin
t / P
lan
area
Cap
aciti
es u
p to
260
,000
#/h
r with
pr
e-en
gine
ered
eco
nom
y, c
usto
m
units
up
to 8
00,0
00 #
/hr
O
xyge
n re
mov
al to
0.0
05 c
c/lit
er
(7pp
b) p
er H
EI
C
ertif
ied
ASM
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
(HE
I) D
esig
n
FEA
TUR
ES
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
FEED
WAT
ER IN
LET
%
Mak
eup
M
U Te
mper
ature
%Co
nden
sate
C
ond.
Temp
eratu
re
ST
ORAG
E CA
PACI
TY
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
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
SPEC
IAL
REQU
IREM
ENTS
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
PROJ
ECT
DE
AERA
TOR
Q
uanti
ty
Cap
acity
DESI
GN
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
DS
Serie
s U
p to
800
,000
#/h
r Tr
ay U
nit
Mee
ts H
EI
VS=
Vert
ical
Spr
ay
(See
fron
t cov
er fo
r add
ition
al se
ries)
3
508=
20,
000
#/H
R
020
=20,
000
#/H
R
(Use
actu
al ca
paci
ty, c
harts
show
max
imum
capa
city)
M
=Mec
hani
cal
or P
=Pne
umat
ic
(Lea
ve bl
ank f
or no
ne)
P=P
ipin
g In
clud
ed
O=P
ipin
g N
ot In
clud
ed
PK
G=P
acka
ge
(Lea
ve bl
ank f
or no
ne)
2 =
# o
f Pum
ps
042
= F
low
(GPM
) 1
50 =
Hea
d(PS
I)
VS De
aera
tor
MOD
ELS
S
ERIES
-
SIZE
CAPA
CITY
TY
PE
PI
PED
#/P
UMPS
FL
OW
HE
AD
SELE
CTIO
N CHA
RT
10 M
inut
es S
tora
ge
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)
VS-
3006
-020
58
0 20
,000
21
0 5
3’0”
x2’7
” x
7’9”
1.
5 6
1,40
0 3,
000
4,00
0 6’
3”x5
’9”
x9’3
” 7’
0”x2
’11”
x2
’10”
VS-
3508
-040
1,
159
40,0
00
420
5 3’
6”x2
’11”
x
9’11
” 2
6 2,
000
6,00
0 7,
000
6’3”
x8’7
” x1
1’11
” 8’
6”x3
’3”
x3’1
0”
VS-
4008
-050
1,
449
50,0
00
525
5 4’
0”x3
’4”
x 10
’1”
2.5
8 2,
400
7,00
0 10
,000
6’
2”x9
’5”
x11’
7”
8’6”
x3’8
” x4
’0”
VS-
4508
-060
1,
739
60,0
00
630
5 4’
6”x3
’8”
x 10
’4”
2.5
8 2,
700
8,00
0 12
,000
6’
3”x9
’9”
x11’
10”
8’6”
x4’0
” x4
’0”
VS-
5008
-080
2,
319
80,0
00
840
5 5’
0”x4
’1”
x 10
’10”
3
10
3,20
0 11
,000
15
,000
6’
11”x
10’8
”x1
2’4”
9’
0”x4
’5”
x4’0
”
VS-
5508
-100
2,
899
100,
000
1,05
0 5
5’6”
x4’5
” x
11’0
” 4
10
3,40
0 12
,000
18
,000
6’
6”x1
2’4”
x12’
10”
10’0
”x4’
9”
x5’6
”
VS-
6008
-120
3,
478
120,
000
1,26
0 5
6’0”
x5’2
” x
11’3
” 4
12
3,90
0 15
,000
21
,000
6’
10”x
12’7
”x1
3’0”
10
’0”x
5’4”
x5
’6”
VS-
6009
-140
4,
058
140,
000
1,47
0 5
6’0”
x5’2
” x
12’3
” 4
12
4,30
0 17
,000
23
,000
6’
10”x
12’7
”x1
4’0”
C
onsu
lt Fa
ctor
y
VS-
6010
-160
4,
638
160,
000
1,68
0 5
6’0”
x5’2
” x
13’3
” 4
12
4,70
0 19
,000
26
,000
6’
10”x
12’7
”x1
5’0”
C
onsu
lt Fa
ctor
y
VS-
6510
-180
5,
217
180,
000
1,89
0 5
6’6”
x5’7
” x
13’5
” 6
14
5,50
0 22
,000
30
,000
10
’8”x
12’6
”x1
6’8”
C
onsu
lt Fa
ctor
y
VS-
6512
-220
6,
377
220,
000
2,31
0 5
6’6”
x5’7
” x
15’5
” 6
14
6,20
0 26
,000
35
,000
10
’8”x
13’5
”x1
8’8”
C
onsu
lt Fa
ctor
y
VS-
7012
-260
7,
536
260,
000
2,73
0 5
7’0”
x5’1
1”
x 15
’7”
6 16
6,
900
30,0
00
41,0
00
11’1
”x13
’8”
x18’
10”
Con
sult
Fact
ory
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)
VS-
3006
-010
29
0 10
,000
21
0 10
3’
0”x2
’7”
x 7’
9”
1 3
1,30
0 3,
000
4,00
0 6’
6”x5
’9”
x9’3
” 7’
0”x2
’11”
x2
’10”
VS-
3508
-020
58
0 20
,000
42
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”
VS-
4008
-025
72
5 25
,000
52
5 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”
VS-
4508
-030
87
0 30
,000
63
0 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”x4
’0”
x3’0
”
VS-
5008
-040
1,
159
40,0
00
840
10
5’0”
x4’1
” x
10’1
0”
2 6
2,70
0 10
,000
14
,000
6’
9”x9
’4”
x12’
9”
9’0”
x4’5
” x4
’0”
VS-
5508
-050
1,
449
50,0
00
1,05
0 10
5’
6”x4
’5”
x 11
’0”
2.5
8 3,
100
12,0
00
17,0
00
6’9”
x10’
2”x1
2’6”
9’
6”x4
’9”
x3’6
”
VS-
6008
-060
1,
739
60,0
00
1,26
0 10
6’
0”x5
’2”
x 11
’3”
2.5
8 3,
300
14,0
00
20,0
00
6’10
”x10
’6”
x12’
9”
10’6
”x5’
4”
x3’6
”
VS-
6009
-070
2,
029
70,0
00
1,47
0 10
6’
0”x5
’2”
x 12
’3”
3 8
3,60
0 16
,000
23
,000
7’
3”x1
1’2”
x13’
9”
10’6
”x5’
4”
x3’6
”
VS-
6010
-080
2,
319
80,0
00
1,68
0 10
6’
0”x5
’2”
x 13
’3”
3 10
4,
000
18,0
00
25,0
00
7’3”
x11’
2”x1
4’9”
10
’6”x
5’4”
x3
’6”
VS-
6510
-090
2,
609
90,0
00
1,89
0 10
6’
6”x5
’7”
x 13
’5”
3 10
4,
400
20,0
00
29,0
00
7’10
”11’
5”x1
4’11
” 12
’0”x
5’9”
x4
’5”
VS-
6512
-110
3,
188
110,
000
2,31
0 10
6’
6”x5
’7”
x 15
’5”
4 10
5,
100
24,0
00
34,0
00
7’6”
x12’
10”
x18’
8”
11’7
”x5’
9”
x4’5
”
VS-
7012
-130
3,
768
130,
000
2,73
0 10
7’
0”x5
’11”
x
15’7
” 4
12
5,90
0 29
,000
40
,000
8’
2”x1
3’1”
x18’
10”
11’7
”x6’
1”
x4’1
1”
VS De
aera
tor
CH
ART
Mode
l Num
ber S
elec
tion
Ser
ies
Size
C
a pac
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
EXAM
PLE:
V
S
3 5
0 8
-- 0
2 0
--
M
O
--
P
K G
--
2 -
- 0
4 2
--
1 5
0
_
_
_ _
_ _
_
_ _
_
_
_ _
_
_
_
_ _
_ _
_
5 M
inut
es S
tora
ge
Typi
cal A
rrang
emen
t