HS
Serie
s U
p to
350
,000
#/h
r Lo
w H
eadr
oom
Cont
inuo
us Bl
owdo
wn
S
PECI
FICAT
ION
Con
tinuo
us B
low
dow
n w
/Hea
t Rec
over
y
Stan
dard
D
eaer
atin
g U
nits
KK AA
NN SSAA SS
CCII TT
YY DDEE AA
EE RRAA TT
OO RRCB
HR –
Cont
inuo
us Bl
owdo
wn
w/He
at Re
cove
ry
Prin
cipl
es o
f Ope
ratio
n
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
CB
HR
SPE
CIF
ICA
TIO
N
Furn
ish
and
inst
all a
s sh
own
on d
raw
ings
, a K
ansa
s C
ity D
eaer
ator
Con
tinuo
us B
low
dow
n w
/Hea
t R
ecov
ery
MO
DE
L N
O. (
CB
HR
) ___
____
____
____
____
as
man
ufac
ture
d by
Kan
sas
City
Dea
erat
or C
ompa
ny, I
nc.
The
Flas
h E
cono
miz
er s
hall
be c
apab
le o
f han
dlin
g __
____
____
____
__ #
/hr.
cont
inuo
us b
low
dow
n an
d _
____
____
____
___
gpm
mak
e-up
at
the
boile
r op
erat
ing
pres
sure
/pre
ssur
es o
f___
____
____
__ p
sig.
fla
shin
g to
low
pr
essu
re d
eaer
ator
, fee
dwat
er
heat
er o
r oth
er lo
w p
ress
ure
user
at _
____
____
____
_ ps
ig.
The
Flas
h E
cono
miz
er s
hall
cons
ist o
f the
follo
win
g co
mpo
nent
s an
d ac
cess
orie
s:
1.
V
ertic
al F
lash
Sep
arat
or s
ectio
n w
ith th
read
ed c
onne
ctio
ns fo
r tan
gent
ial i
nlet
with
sta
inle
ss
stee
l wea
r pl
ate,
blo
wdo
wn
drai
n re
cove
red
stea
m v
ent,
and
tank
cle
anou
t con
nect
ions
as
wel
l as
coup
lings
as
requ
ired
for a
cces
sorie
s.
2.
Ver
tical
coi
l-typ
e he
at e
xcha
nger
mad
e of
(cop
per o
r sta
inle
ss s
teel
) with
ste
el th
read
ed
conn
ectio
ns fo
r mak
e-up
inle
t, ou
tlet,
and
open
ings
for r
emot
e th
erm
omet
er b
ulbs
.
3.
Fla
nged
bot
tom
sec
tion
with
dro
p ou
t coi
l des
ign
for e
asy
clea
ning
and
mai
nten
ance
. 4.
B
alan
ced
float
trap
with
all
wor
king
par
ts c
onst
ruct
ed o
f sta
inle
ss s
teel
with
rem
ovab
le s
eats
, lo
cate
d ex
tern
ally
and
bac
k ve
nted
to m
aint
ain
a co
nsta
nt le
vel i
n th
e fla
sh s
epar
ator
.
5.
Ther
mom
eter
gau
ge p
anel
sho
win
g te
mpe
ratu
res
of th
e m
ake-
up in
let,
mak
e-up
out
let,
and
blow
dow
n w
ater
to d
rain
. 6.
A
saf
ety
relie
f val
ve s
et a
t 150
psi
g, a
Mic
higa
n si
te le
vel g
auge
, and
tank
cle
an o
ut v
alve
.
7.
O
ptio
nal A
cces
sorie
s sh
all i
nclu
de a
hig
h le
vel a
larm
sw
itch,
mul
ti-bo
iler m
anifo
ld, f
low
co
ntro
l or b
low
dow
n va
lves
, pre
ssur
e ga
uge,
and
sam
ple
cool
er w
ith p
ipin
g.
All
the
abov
e co
mpo
nent
s sh
all b
e m
ount
ed o
n a
tabl
e ba
se w
ith fo
ur a
ngle
iron
floo
r sup
ports
and
pa
ds i
n su
ch a
man
ner
that
will
allo
w g
ravi
ty f
low
of
blow
dow
n w
ater
thr
ough
the
sys
tem
. Th
e fin
ishe
d sy
stem
sha
ll be
pai
nted
with
a b
lue
enam
el e
xter
ior.
The
equi
pmen
t sha
ll be
des
igne
d an
d co
nstru
cted
in a
ccor
danc
e w
ith th
e la
test
AS
ME
Cod
e Se
c.
VIII
, Div
. 1. r
equi
rem
ents
for a
unf
ired
pres
sure
ves
sel f
or 1
50 p
sig
MA
WP
.
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
Cop
yrig
ht ©
Jan
uary
200
4
ME
MB
ER
1.
TAN
GEN
TIA
L IN
LET
impa
rts h
igh
velo
city
sp
inni
ng a
ctio
n to
liqu
id
2.
STA
INLE
SS S
TEEL
wea
r Pla
te a
t poi
nt o
f im
ping
emen
t pre
vent
s er
osio
n of
se
para
tor w
all
3.
FL
OA
T TR
AP fo
r con
tinuo
us d
isch
arge
of
coo
led
wat
er to
dra
in
4.
C
OO
LED
BLO
WD
OW
N to
dra
in (1
00 -
110°
)
5.
BO
ILER
MAK
E-U
P ex
its h
eate
d by
co
ntin
uous
blo
wnd
own
at n
o ex
tra c
ost
6.
C
OLD
WA
TER
boi
ler m
ake-
up e
nter
s sy
stem
7.
SLU
DG
E A
REA
no
pock
ets
or b
affle
s in
he
at e
xcha
nger
are
a fo
r slu
dge
to
depo
sit a
nd re
duce
hea
t rec
over
y ef
ficie
ncy
or to
clo
p th
e flo
w a
rea
8.
S P
IRA
L C
OIL
HEA
T EX
CH
AN
GER
de
sign
ed to
pro
vide
max
imum
hea
t tra
nsfe
r
9.
HIG
H V
ELO
CIT
Y C
ENTR
IFU
GA
L A
CTI
ON
dr
ives
liqu
id a
nd s
olid
s to
out
side
–
only
cle
an d
ry s
team
rele
ases
into
ce
ntra
l vor
tex
area
and
up
into
ste
am
outle
t
10.
LOW
PR
ESSU
RE
VOR
TEX
AR
EA e
xped
ites
inst
ant f
lash
ing
of a
ll st
eam
to o
utle
t
11.
STEA
M O
UTL
ET c
lean
dry
ste
am 9
7%
qual
ity to
dea
erat
or
CBH
R=Co
ntin
uous
B
lowd
own H
eat
Rec
over
y 14
20 =
Tank
Size
(1
4” x
20” l
ong)
1=
1” Bl
owdo
wn
Inle
t 2
=2” D
rain
2
=2” V
ent
Cont
inuo
us Bl
owdo
wn
M
ODEL
S
SER
IES
T
ANK
IN
LET
DRA
IN
V
ENT
CB
HR
M
OD
EL
BLO
W
DO
WN
M
AK
E U
P A
B
C
D
E
F G
H
I
J K
L
M
CB
HR
3-15
3
15
97
46
40
10.75
1.5
2.5
1
1 37
.25 1
7.75
28.00
8.5
0 9.0
CB
HR
6-30
6
30
111
53
46
12.75
1.5
3
1 1.2
5 35
.00 1
9.00
27.00
11.0
0 9.0
CB
HR
10-5
0 10
50
10
6 51
43
16
.00
1.5
4 2
1.5
41.50
23.5
0 32
.25 1
4.25
9.0
CB
HR
20-1
00
20
100
140
68
60
18.00
1.5
6
2 2
45.00
25.0
0 35
.75 1
5.75
9.0
CB
HR
30-1
50
30
150
132.5
67
51
.25 2
4.00
1.5
6 2
2.5
51.00
33.0
0 41
.75 2
3.75
9.0
Cont
inuo
us Bl
owdo
wn
CHAR
TMo
del N
umbe
r Sel
ectio
n
S
eries
T
ank
Inlet
Dra
in
Ven
t
CO
NTI
NU
OU
S B
LOW
DO
WN
HEA
T R
ECO
VER
Y
EXAM
PLE:
C
B H
R
1
4 2
0
--
1
--
2
--
2
_ _
_ _
_ _
_ _
_
_
_
Typi
cal A
rrang
emen
t
SELE
CTIO
N CHA
RT