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Tanques flash para instalaciones de vapor y calderas

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me
Reprinted
Am ri an Soci
Societ
et
is
Heat
Heatin
in
Refr
Refrig
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erat
atin
in
an
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ers, Inc.
Inc.
ms
Low
Associate
me
Member
dv nt ge
mf
o f h av
av in
in g
p ro
ro p
gn
nk
e1
ma
effic
efficie
ient
nt device.
device .
T h a r c l d es
es c b e h o
mp
mp
Amou
Amount
nt of liqu
liquid
id
as
a nk
nk s w o rk
rk , h o
he ca
Amou
Amount
nt ofstea
ofsteam.
m. Ib
Pressu
Pressure,
re, psi
Temperature,
operation.
Liquid
Liquid speci
speciflc
flc
enthal
enthalpy,
py, Btu/lb
Btu/lb
Operation
Steam specific
specific
enthal
enthalpy,
py, Btu/lb
Btu/lb
mp
ms
" f a sh
sh in
in g
ma
me
h a o cc
cc u w h e h o w a e r a t s om
om e h ig
ig he
he r p re
re ss
ss u
we
We
heatthat
we
e n h a p y o f h e q u a t h e h ig
ig he
he r p re
re ss
ss u a n h e n th
th a p y o f
s a u rraa te
te d q u a t h e o w e p rree ss
ss ur
ur e
T h n th
th a p y o f v ap
ap o o n h e h e
qu
h an
an g
he qu
s te
te a a t h e o w e p re
re ss
ss u e ) d e e rm
rm in
in e h o m u c
o f h e q u c a b e c on
on ve
ve r e d
s te
te a b y t h h ea
ea t a va
va i a b e .
o th
th e w o rd
rd s
flas
flas h s team
team
du
c ha
ha ng
ng e
)(
1-
Total enthalpy
enthalpy
of steam, tu
(X) (1.150
(1.150
w e g no
no r h e o ss
ss es
es , h e e n h a p y o f h e h ig
ig h p r s ssuu r
wa
mu
w a e r a n s te
te a e n e r n g h e a nk
nk :
Liquid
Liquid enthal
enthalpy
py
a t h ig
ig h e p re
re ssss uurr e
(1 (309)
h ea
ea t e ne
ne rg
rg y a va
va i a b
1.150
Total enthalpy
enthalpy
of liqu
liquid
id Bt
L iq
iq u i e n th
th a lp
lp y
a t l ow
ow e r p re
re ssss u r
(1
E n th
th a p y o f s te
te a
a t l ow
ow e r p re
re ssss u r
X)
X ) 1 15
15 0
p rree ss
ss ur
ur e
e ne
ne rg
rg y e qu
qu i e d o r c ha
ha ng
ng e o f p ha
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-or-
/0 flash
h ig
ig h p re
re ss
ss u
qu
en ha py
o w p re
re ss
ss u
qu
en ha py
70
e n h a p y o f e va
va po
po rraa t o n a t h e o w e p rree ss
ss ur
ur e
F o e xa
xa mp
m p le
le , o n p ou
ou n
o f b o n g w a e r s a u ra
ra te
te d
00 psig/338
(689 kPal
1 70
70 °C
°C )
o w n g o m p ip
ip e n t
nk
mo ph
pr
s u e . W h a a c o n X , o f h e w a e r w i a s n t s te
te am
am ?
Fr
we
wa
ma mu
qu
n th
th a p y o r o t
n th
th a p y o r
m. Th da
om
h e x am
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nd he
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b e s um
um m a
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in
Ta
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qu
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in oi
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ns titi tu
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ch n ol
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mp
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mp
ms
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mp
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Handbook=Systems,'
A SH
SH R
b /h
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influenced b y o th
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m.
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wh
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Valves
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Temperature Regu
b e m in
in im
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flooding.
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flas tank
tank
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h e h ig
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wi
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Figure 5 . T h
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wi
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mp l
Volume
ft /sec, a s w e
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ul
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Figure 4 , w e d et
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ftl.
in Table
At
me
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wh
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important.
o r h o z on
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a nk
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Si
h e o w p re
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pip ng us ng
nd
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wi
Additional
Additional considerat
considerations
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mo
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mls)
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mo
mo
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Fi ur
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Tabl
Tabl
e qu
qu ip
ip pe
pe d w i r e e f v a v e o f p rroo pe
pe r s iz
iz e a n c ap
ap ac
ac i a s w e l a s
v a u u b re
re ak
ak e
co wa
o u b e n t o du
du ce
ce d n t h e h o
tank.
Flas
Flas tank
tank imen
imensi
si ns
Disengaging
pr
(fts)
(fe)
Horizontal
tank
-12
12
33
39
Vertical
tank
2,3
2,1
2,3
he nt
o w p re
re s u r s t a m d em
em an
a n d If h e p ea
ea k p rroo du
du c o n
me
mi mu
me
ha
he
o nd
nd en
en s o r
mo ph
mu
be provid
provided.
ed.
F iinn a y , h e a r s ev
ev er
er a f ea
ea tu
tu rree s h a s ho
ho u b e n c u de
de d
eeve
very
ry flas
flas h tank
tank insta
install
llat
ation
ion
wh
Ad
v en
en t n g h e e ce
ce iv
iv e a n c oo
oo l n g h e c on
on de
de ns
ns a
provided.
mp
m us
u s t b e m ad
ad e
mu
u r g au
au g
h ou
ou l
P ro
ro p
s uriz
urized
ed tank.
tank.
p ro
ro v d e
p s h ou
ou l
nk
p ro
ro v
pr
Ea
nd ns
br nc
he
ou be
e qu
qu ip
ip pe
pe d w i
c h c k v a v e a vo
vo i b ac
ac k o w T h s te
te a p ip
ip ng ma
so ne
ch ck va ve
c on
on n c t
p r s ssuu r e d
equipment.
Th
v en
en t
g as
as e h a m a y a cc
cc um
um u la
la t
wi
nd
mo
no
d ur
ur in
in g o pe
pe ra
ra t o n
mo
nd ns bl
Conclusions
wi
mo
mp
nc pl
Th
or
he
ni
a pp
pp l
m an
a n y c on
on de
de n a t h an
an d n g s i u a o n
mo yn mi
c os
os t n d e as
as y
equipment.
B y m u a ne
ne ou
ou s
g en
en e a t n g
as
ea
a n c oo
oo l n g h e
by du
oa on he oi
nd
wi
nd ns
r an
an s e r b y u s o f r ea
ea d a va
va i a b p um
um p in
in g e qu
qu ip
ip m en
en t
As ne gy os nc
nk
dd
s te
te a a n c on
on de
de ns
ns a s ys
ys te
te m w i b ec
ec om
om e n cr
cr ea
ea s n g p op
op u a r
Th ar cl wa of ed
h e h op
op e h a
wi se ve he
ms
w a r a n e i h e w r e n o r m p l e d g iv
iv e o r h e f i n es
es s o r
b ilil itit y o f t he
he s i de
de as
as .
b u d in
in g
de nd gu
n s h ou
ou l
checked to n s
ha
n fo
fo rm
rm a o n g r
wi
he
an
g u a t o ns
ns . o c
o nd
nd i o n
e g d in
in g a tm
tm o p h
o th
th e o nd
nd i o n
h ou
ou l b e h e k e
n su
su r
us bi
u ssaa ul
de
an
of
References
Handbook-Systems.
I.
A tltl an
an ta
ta ,
G eo
e o rg
rg ia
ia .
A tltl an
an ta
ta ,
G eo
e o rg
rg ia
ia .
Handbook-Fundamentals.
Ma
R e tu
tu r
TE
8. Ma
3,
i p e S iz
iz in
in g C h ar
ar /s
/s o
8 . Basic Steam P ip
Mo
Gr
Hig
Sys ems
Ch
T e m pe
pe ra
ra tu
tu r
Condensate
Illinois.
D e s g n M a nu
nu a jor H e a ti
ti ng
ng , V e n titi lo
lo titi en
en ,
P lu
l u mb
m b in
in g a n Air Condi
Conditio
tionin
nin Systems. 4 t
Ar
Vi
T ec
ec hn
hn ic
ic a
S ta
ta nd
nd ar
ar d
P ub
u b l c at
at io
io ns
ns .
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