Continuous Blowdown w/Heat Recover R Continuous...
2
HS Series Up to 350,000 #/hr Low Headroom Continuous Blowdown SPECIFICATION Continuous Blowdown w/Heat Recovery 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 CBHR – Continuous Blowdown w/Heat Recovery Principles of Operation 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] CBHR SPECIFICATION Furnish and install as shown on drawings, a Kansas City Deaerator Continuous Blowdown w/Heat Recovery MODEL NO. (CBHR) ___________________ as manufactured by Kansas City Deaerator Company, Inc. The Flash Economizer shall be capable of handling ________________ #/hr. continuous blowdown and ________________ gpm make-up at the boiler operating pressure/pressures of_____________ psig. flashing to low pressure deaerator, feedwater heater or other low pressure user at ______________ psig. The Flash Economizer shall consist of the following components and accessories: 1. Vertical Flash Separator section with threaded connections for tangential inlet with stainless steel wear plate, blowdown drain recovered steam vent, and tank cleanout connections as well as couplings as required for accessories. 2. Vertical coil-type heat exchanger made of (copper or stainless steel) with steel threaded connections for make-up inlet, outlet, and openings for remote thermometer bulbs. 3. Flanged bottom section with drop out coil design for easy cleaning and maintenance. 4. Balanced float trap with all working parts constructed of stainless steel with removable seats, located externally and back vented to maintain a constant level in the flash separator. 5. Thermometer gauge panel showing temperatures of the make-up inlet, make-up outlet, and blowdown water to drain. 6. A safety relief valve set at 150 psig, a Michigan site level gauge, and tank clean out valve. 7. Optional Accessories shall include a high level alarm switch, multi-boiler manifold, flow control or blowdown valves, pressure gauge, and sample cooler with piping. All the above components shall be mounted on a table base with four angle iron floor supports and pads in such a manner that will allow gravity flow of blowdown water through the system. The finished system shall be painted with a blue enamel exterior. The equipment shall be designed and constructed in accordance with the latest ASME Code Sec. VIII, Div. 1. requirements for a unfired pressure vessel for 150 psig MAWP. 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 Copyright © January 2004 MEMBER 1. TANGENTIAL INLET imparts high velocity spinning action to liquid 2. STAINLESS STEEL wear Plate at point of impingement prevents erosion of separator wall 3. FLOAT TRAP for continuous discharge of cooled water to drain 4. COOLED BLOWDOWN to drain (100 - 110°) 5. BOILER MAKE-UP exits heated by continuous blowndown at no extra cost 6. COLD WATER boiler make-up enters system 7. SLUDGE AREA no pockets or baffles in heat exchanger area for sludge to deposit and reduce heat recovery efficiency or to clop the flow area 8. SPIRAL COIL HEAT EXCHANGER designed to provide maximum heat transfer 9. HIGH VELOCITY CENTRIFUGAL ACTION drives liquid and solids to outside – only clean dry steam releases into central vortex area and up into steam outlet 10. LOW PRESSURE VORTEX AREA expedites instant flashing of all steam to outlet 11. STEAM OUTLET clean dry steam 97% quality to deaerator
Transcript of Continuous Blowdown w/Heat Recover R Continuous...
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
