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
