HYSYS tutorial
30
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Reactors and Heat Exchangers
Transcript of HYSYS tutorial
Tuto
rial
2
Rea
ctor
s an
d H
eat
Exch
ange
rs
Prob
lem
1 C
onve
rsio
n R
eact
or
Con
side
r a
stre
am o
f N
2 an
d H
2 at
300
ºF
and
500
psia
with
mol
e fr
actio
n of
0.3
and
0.7
, re
spec
tivel
y, w
ith a
mol
ar f
low
rat
e of
100
lbm
ol/h
r. T
his
stre
am e
nter
s a
reac
tor.
C
onve
rsio
n of
N2
is 3
0 %
and
the
reac
tor
is is
othe
rmal
. C
alcu
late
the
prop
ertie
s of
out
let
stre
ams
usin
g Pe
ng-R
obin
son
equa
tion
of s
tate
. Th
e fo
llow
ing
reac
tion
take
s pl
ace
in t
he
reac
tor:
32
22
3N
HH
N
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
126
Solu
tion:
Follo
w th
e st
ep-b
y-st
ep in
stru
ctio
ns to
solv
e th
e pr
oble
m.
1-O
pen
a ne
w c
ase.
2-A
dd a
new
com
pone
nt li
st.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s12
7
3-Se
lect
the
com
pone
nts
from
the
Com
pone
nts
list
and
then
clo
se t
he a
ctiv
e w
indo
w b
y cl
icki
ng o
n cr
oss b
utto
n (a
ll pr
oces
s com
pone
nts s
houl
d be
ent
ered
in th
is st
ep).
4-Th
e cr
oss
butto
n is
not
see
n on
the
figur
e an
d yo
u co
uld
mov
e th
e ac
tive
win
dow
to s
ee
the
cros
s but
ton
in o
rder
to c
lose
it.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
128
5-Se
lect
the
Flui
d Pa
ckag
e (M
ake
sure
sele
ctin
g C
ompo
nent
Lis
t -1i
n th
e co
mpo
nent
list)
.
6-A
dd a
new
Flu
id P
acka
ge
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s12
9
7-Se
lect
the
Peng
Rob
inso
n or
SRK
equ
atio
n of
stat
e fr
om P
rope
rty
Pack
age.
8-C
lose
the
Flu
id P
acka
ge b
y cl
icki
ng o
n cr
oss
butto
n. A
fter
this
ste
p, i
t is
pos
sibl
e to
im
port/
expo
rt th
e Fl
uid
Pack
age.
G
o to
the
Reac
tion
butto
n.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
130
9-G
o to
the
Add
Rxn
butto
n to
ent
er th
e re
actio
n da
ta.
10-S
elec
t the
Con
vers
ion
Rea
ctio
n an
d th
en c
lick
on th
e ad
d Re
actio
n bu
tton.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s13
1
11-S
elec
t th
e co
mpo
nent
s fr
om t
he d
rop
dow
n m
enu
and
then
ent
er t
he s
toic
hiom
etry
(n
egat
ive
for r
eact
ants
and
posi
tive
for p
rodu
cts)
. Th
e ba
lanc
e er
ror s
houl
d be
zer
o.
12-C
lick
on th
e Ba
sis
butto
n, s
elec
t Bas
e Co
mpo
nent
fro
m d
rop
dow
n m
enu
and
ente
r th
e co
nver
sion
for t
he b
ase
com
pone
nt (3
0 %
).
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
132
13-C
lose
the
act
ive
win
dow
and
ret
urn
to t
he f
ollo
win
g w
indo
w:
The
rea
ctio
n Rx
n-1
is ad
ded.
Add
a re
actio
n se
t by
clic
king
on
the
Add
Set b
utto
n.
14-I
n th
e Ac
tive
List
, sel
ect R
xn-1
from
the
drop
dow
n m
enu.
Che
ck m
ark
the
reac
tion
set
and
clos
e th
e ac
tive
win
dow
.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s13
3
15-C
lick
on th
e Ad
d FP
but
ton
(Thi
s mak
es th
e re
actio
n ac
cess
ible
for s
imul
atio
n).
16-C
lick
on A
dd S
et to
Flu
id P
acka
ge B
utto
n.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
134
17-T
he B
asis
-1 p
rope
rty m
odel
is
now
add
ed t
o th
e Fl
uid
Pack
age.
Th
en E
nter
to
Sim
ulat
ion
Envi
ronm
ent.
18-G
o to
Too
ls/P
refe
renc
e to
cha
nge
the
Uni
t Set
to F
ield
.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s13
5
19-G
o to
the
Vari
able
s but
ton,
sele
ct F
ield
and
clo
se th
e w
indo
w (T
he n
ew u
nit s
et m
ay a
lso
be c
lone
d by
clic
king
on
the
Clo
ne b
utto
n).
20-D
rag
a m
ater
ial s
tream
to th
e PF
D, c
lick
on s
tream
and
ent
er tw
o ou
t of t
hree
pro
perti
es
(tem
pera
ture
, pr
essu
re
and
vapo
r fra
ctio
n)
and
mol
ar
flow
rate
in
th
e W
orks
heet
/Con
ditio
ns P
age.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
136
21-S
ave
the
sim
ulat
ion
wor
k (e
.g.,
pro
blem
-1).
22-E
nter
the
mol
e fr
actio
ns o
f th
e co
mpo
nent
s in
Wor
kshe
et C
ompo
sitio
n pa
ge. C
lick
OK
and
clos
e th
e ac
tive
win
dow
to re
turn
to P
FD.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s13
7
23-T
he s
tream
pro
perti
es c
an n
ow b
e ca
lcul
ated
(se
en i
n th
e W
orks
heet
/Pro
pert
ies
page
).
Item
s in
blue
and
bla
ck in
dica
te u
ser-d
efin
ed a
nd c
alcu
late
d pr
oper
ties,
resp
ectiv
ely.
24-C
lose
the
activ
e w
indo
w a
nd p
ut th
e cu
rser
on
the
stre
am to
vie
w th
e Fl
y-By
win
dow
.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
138
25-S
elec
t a c
onve
rsio
n re
acto
r fro
m o
bjec
t pal
ette
(F4)
and
dra
g it
to th
e PF
D.
26-
Dou
ble
clic
k on
the
reac
tor a
nd e
nter
Inle
t, V
apor
and
Liq
uid
Out
lets
and
Ener
gy s
tream
in
the
Des
ign/
Con
nect
ions
pag
e.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s13
9
27-G
o to
the
Reac
tions
pag
e an
d se
lect
reac
tion
set f
rom
the
Reac
tion
Set d
rop
dow
n m
enu.
28-I
n th
e W
orks
heet
pag
e, e
ither
ent
er te
mpe
ratu
re o
f one
of o
utle
t stre
ams
or d
efin
e du
ty o
f he
at st
ream
. W
ith th
ese
info
rmat
ion
reac
tor w
ill b
e so
lved
imm
edia
tely
.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
140
29-T
he d
uty
of h
eat s
tream
is e
nter
ed in
Des
ign/
Part
amet
ers
sect
ion.
(M
ake
sure
to d
elet
e th
e te
mpe
ratu
re e
nter
ed in
pre
viou
s sec
tion)
.
30-T
he p
rope
rties
of a
ll st
ream
s cou
ld b
e vi
ewed
in th
e W
orks
heet
Pro
pert
ies P
age.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s14
1
Prob
lem
2 C
STR
Pr
oduc
tion
of k
eten
e fro
m a
ceto
ne is
per
form
ed in
a C
STR
. 4
23
3C
HC
OC
HC
OC
HC
HTh
e re
actio
n ra
te c
onsta
nt (i
n SI
uni
t) fo
r thi
s rea
ctio
n is
:
RTk
514
1085.2
exp
10*2.8 w
here
k is
in k
gmol
/m3 s.
Feed
stre
am (p
ure
acet
one)
ent
ers
the
reac
tor a
t 760
ºC a
nd 1
60 k
Pa w
ith m
olar
flow
rate
of
140
kmol
e/hr
. Th
e re
acto
r is
adia
batic
and
its
volu
me
is 2
m3 .
Sim
ulat
e th
e pr
oces
s us
ing
PRSV
equ
atio
n of
stat
e.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
142
Solu
tion:
Follo
w th
e st
ep-b
y-st
ep in
stru
ctio
ns to
solv
e th
e pr
oble
m.
1-O
pen
a ne
w c
ase.
2-A
dd a
new
com
pone
nt li
st.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s14
3
3-Se
lect
the
com
pone
nts
from
the
Com
pone
nts
list
and
then
clo
se t
he a
ctiv
e w
indo
w b
y cl
icki
ng o
n cr
oss b
utto
n (a
ll pr
oces
s com
pone
nts s
houl
d be
ent
ered
in th
is st
ep).
4-Th
e cr
oss
butto
n is
not
see
n on
the
figur
e an
d yo
u co
uld
mov
e th
e ac
tive
win
dow
to s
ee
the
cros
s but
ton
in o
rder
to c
lose
it.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
144
5-Se
lect
the
Flui
d Pa
ckag
e (M
ake
sure
sele
ctin
g C
ompo
nent
Lis
t -1i
n th
e co
mpo
nent
list)
.
6-A
dd a
new
Flu
id P
acka
ge.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s14
5
7-Se
lect
the
PSRV
equ
atio
n of
stat
e fr
om P
rope
rty P
acka
ge.
8-C
lose
the
Flu
id P
acka
ge b
y cl
icki
ng o
n cr
oss
butto
n. A
fter
this
ste
p, i
t is
pos
sibl
e to
im
port/
expo
rt th
e Fl
uid
Pack
age.
G
o to
the
Reac
tion
butto
n.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
146
9-G
o to
the
Add
Rxn
butto
n to
ent
er th
e re
actio
n da
ta.
10-S
elec
t the
Kin
etic
Rea
ctio
n an
d th
en c
lick
on th
e ad
d Re
actio
n bu
tton.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s14
7
11-S
elec
t the
com
pone
nts f
rom
the
drop
dow
n m
enu
and
then
ent
er st
oich
iom
etry
of r
eact
ion
(neg
ativ
e fo
r rea
ctan
ts an
d po
sitiv
e fo
r pro
duct
s).
The
bala
nce
erro
r sho
uld
be z
ero.
12-C
lick
on th
e Ba
sis
butto
n, s
elec
t Bas
e Co
mpo
nent
fro
m d
rop
dow
n m
enu
and
ente
r th
e re
actio
n ph
ase
(Ove
rall)
and
che
ck th
e un
its.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
148
13-G
o to
Par
amet
ers p
age
and
ente
r the
reac
tion
rate
dat
a.
14-G
o to
Clo
se th
e ac
tive
win
dow
and
retu
rn to
the
follo
win
g w
indo
w:
The
reac
tion
Rxn-
1is
add
ed.
Add
a re
actio
n se
t by
clic
king
on
the
Add
Set b
utto
n.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s14
9
15-I
n th
e Ac
tive
List,
sel
ect R
xn-1
from
the
drop
dow
n m
enu.
Che
ck m
ark
the
set a
nd c
lose
th
e ac
tive
win
dow
.
16-C
lick
on th
e Ad
d FP
but
ton
(Thi
s mak
es th
e re
actio
n ac
cess
ible
for s
imul
atio
n).
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
150
17-C
lick
on A
dd S
et to
Flu
id P
acka
ge B
utto
n.
18-T
he B
asis
-1pr
oper
ty m
odel
is
now
add
ed t
o th
e Fl
uid
Pack
age.
Th
en E
nter
to
Sim
ulat
ion
Envi
ronm
ent.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s15
1
19-D
rag
a m
ater
ial s
tream
to th
e PF
D, c
lick
on s
tream
and
ent
er te
mpe
ratu
re, p
ress
ure
and
mol
ar fl
owra
te in
the
Wor
kshe
et/C
ondi
tions
Pag
e.
20-S
ave
the
sim
ulat
ion
wor
k (e
.g.,
pro
blem
-2).
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
152
21-E
nter
1 f
or a
ceto
ne m
ole
frac
tion
and
zero
for
the
rest
in W
orks
heet
/Com
posi
tion
page
. C
lick
OK
and
clo
se th
e ac
tive
win
dow
to re
turn
to P
FD.
22-T
he s
tream
pro
perti
es c
an n
ow b
e ca
lcul
ated
(se
en i
n th
e W
orks
heet
Con
ditio
ns p
age)
. Ite
ms i
n bl
ue a
nd b
lack
indi
cate
use
r-def
ined
and
cal
cula
ted
prop
ertie
s, re
spec
tivel
y.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s15
3
23-C
lose
the
activ
e w
indo
w a
nd p
ut th
e cu
rser
on
the
stre
am to
vie
w th
e Fl
y-By
win
dow
.
24-S
elec
t a C
STR
from
the
obje
ct p
alet
te (F
4) a
nd d
rag
it to
the
PFD
.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
154
25-
Dou
ble
clic
k on
the
reac
tor a
nd e
nter
Inle
t and
out
let s
tream
s in
Des
ign/
Conn
ectio
ns.
26-G
o to
the
Reac
tions
pag
e an
d se
lect
set o
f rea
ctio
n fr
om R
eact
ion
Set d
rop
dow
n m
enu.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s15
5
27-G
o to
the
Ratin
g pa
ge a
nd e
nter
the
volu
me
(2 m
3 ) for
the
reac
tor.
28-I
n th
e Re
actio
n/Re
sults
pag
e W
orks
heet
pag
e, th
e ac
tual
con
vers
ion
(%)
on th
e ba
sis o
f ac
eton
e co
uld
be se
en.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
156
29-T
he p
rope
rties
of a
ll st
ream
s cou
ld b
e vi
ewed
in th
e W
orks
heet
/Pro
pert
ies P
age.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s15
7
Prob
lem
3: E
quili
briu
m R
eact
or
Con
side
r a st
ream
of N
2 with
mol
e fr
actio
n of
0.7
and
H2w
ith a
mol
e fr
actio
n of
0.3
, whi
ch is
fe
d to
an
equi
libriu
m re
acto
r at 2
5°C
and
20
atm
with
a m
olar
flow
rate
of 1
00 k
mol
e/hr
to
prod
uce
amm
onia
. T
he o
pera
ting
tem
pera
ture
of
reac
tor
is 5
0 ºC
. S
imul
ate
the
proc
ess,
usin
g th
e lib
rary
info
rmat
ion
of H
YSY
S fo
r equ
ilibr
ium
reac
tions
.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
158
Solu
tion:
Follo
w th
e st
ep-b
y-st
ep in
stru
ctio
ns to
solv
e th
e pr
oble
m.
1-O
pen
a ne
w c
ase.
2-A
dd a
new
com
pone
nt li
st.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s15
9
3-Se
lect
the
com
pone
nts
from
the
Com
pone
nts
list
and
then
clo
se t
he a
ctiv
e w
indo
w b
y cl
icki
ng o
n cr
oss b
utto
n (a
ll pr
oces
s com
pone
nts s
houl
d be
ent
ered
in th
is st
ep).
4-Th
e cr
oss
butto
n is
not
see
n on
the
figur
e an
d yo
u co
uld
mov
e th
e ac
tive
win
dow
to s
ee
the
cros
s but
ton
in o
rder
to c
lose
it.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
160
5-Se
lect
the
Flui
d Pa
ckag
e (M
ake
sure
sele
ctin
g C
ompo
nent
Lis
t -1i
n th
e co
mpo
nent
list)
.
6-A
dd a
new
Flu
id P
acka
ge
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s16
1
7-Se
lect
the
Peng
Rob
inso
n or
SRK
equ
atio
n of
stat
e fr
om P
rope
rty
Pack
age.
8-C
lose
the
Flu
id P
acka
ge b
y cl
icki
ng o
n cr
oss
butto
n. A
fter
this
ste
p, i
t is
pos
sibl
e to
im
port/
expo
rt th
e Fl
uid
Pack
age.
G
o to
the
Reac
tion
butto
n.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
162
9-G
o to
the
Add
Rxn
butto
n to
ent
er th
e re
actio
n da
ta.
10-S
elec
t the
Equ
ilibr
ium
Rea
ctio
n an
d th
en c
lick
on th
e ad
d Re
actio
n.bu
tton.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s16
3
11-G
o to
Lib
rary
pag
e an
d se
lect
am
mon
ia r
eact
ion
from
libr
ary
and
clic
k on
Add
Lib
rary
Rx
n bu
tton.
12-
The
reac
tion
info
rmat
ion
will
be
auto
mat
ical
ly a
dded
to th
e St
oich
iom
etry
pag
e.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
164
13-I
n K
eq p
age
equi
libriu
m d
ata
for t
he a
mm
onia
reac
tion
coul
d be
seen
.
14-C
lose
the
activ
e w
indo
w.
The
reac
tion
Rxn-
1 is
add
ed.
Add
a re
actio
n se
t by
clic
king
on
the
Add
Set b
utto
n.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s16
5
15-I
n th
e Ac
tive
List,
sel
ect R
xn-1
from
the
drop
dow
n m
enu.
Che
ck m
ark
the
set a
nd c
lose
th
e ac
tive
win
dow
.
16-C
lick
on th
e Ad
d FP
but
ton
(Thi
s mak
es th
e re
actio
n ac
cess
ible
for s
imul
atio
n).
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
166
17-C
lick
on A
dd S
et to
Flu
id P
acka
ge B
utto
n.
18-T
he B
asis
-1 p
rope
rty m
odel
is
now
add
ed t
o th
e Fl
uid
Pack
age.
Th
en E
nter
to
Sim
ulat
ion
Envi
ronm
ent.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s16
7
19-D
rag
a m
ater
ial s
tream
to th
e PF
D, c
lick
on s
tream
and
ent
er th
e te
mpe
ratu
re, p
ress
ure
and
mol
ar fl
owra
te in
the
Wor
kshe
et/C
ondi
tions
Pag
e.
20-S
ave
the
sim
ulat
ion
wor
k (e
.g.,
pro
blem
-3).
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
168
21-E
nter
the
mol
e fra
ctio
ns o
f th
e co
mpo
nent
s in
Wor
kshe
et/C
ompo
sitio
n pa
ge. C
lick
OK
and
clos
e th
e ac
tive
win
dow
to re
turn
to P
FD.
22-T
he s
tream
pro
perti
es c
an n
ow b
e ca
lcul
ated
(se
en i
n th
e W
orks
heet
Pro
pert
ies
page
).
Item
s in
blue
and
bla
ck in
dica
te u
ser-d
efin
ed a
nd c
alcu
late
d pr
oper
ties,
resp
ectiv
ely.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s16
9
23-S
elec
t an
equi
libriu
m re
acto
r fro
m th
e O
bjec
t Pal
ette
and
dra
g it
to th
e PF
D.
24-
Dou
ble
clic
k on
th
e re
acto
r an
d en
ter
inle
t, ou
tlet
and
ener
gy
stre
am
in
the
Des
ign/
Con
nect
ions
pag
e.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
170
25-G
o to
the
Reac
tions
pag
e an
d se
lect
a re
actio
n se
t fro
m th
e Re
actio
n Se
t dro
p do
wn
men
u.
26-I
n th
e W
orks
heet
pag
e, e
ither
ent
er te
mpe
ratu
re o
f one
of o
utle
t stre
ams
or d
efin
e du
ty o
f he
at st
ream
. En
ter t
empe
ratu
re fo
r the
vap
or o
utle
t stre
am.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s17
1
27-I
n Re
actio
n Re
sults
pag
e, th
e co
nver
sion
per
cent
bas
ed o
n ni
troge
n co
uld
be se
en.
28-N
ow, t
he re
acto
r is s
imul
ated
.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
172
Prob
lem
4 H
eat E
xcha
nger
A
sat
urat
ed v
apor
stre
am o
f al
kene
s (3
6% n
-but
ane,
34%
n-h
exan
e, 3
0% n
-oct
ane
in w
t. pe
rcen
t) en
ters
to th
e sh
ell o
f a h
eat e
xcha
nger
at 1
000
kPa
with
mas
s flo
w ra
te o
f 100
kg/
hr.
The
cool
ing
wat
er a
t 20
ºC is
use
d to
rem
ove
the
heat
from
this
stre
am, w
here
its t
empe
ratu
re
shou
ld n
ot b
e hi
gher
than
50
ºC in
the
outle
t of t
he h
eat e
xcha
nger
. C
alcu
late
the
min
imum
m
olar
flow
rate
of c
oolin
g w
ater
so
that
the
tem
pera
ture
of a
lken
es s
tream
to b
e 60
ºC in
the
outle
t of h
eat e
xcha
nger
. C
hoos
e th
e W
eigh
ted
mod
el fo
r the
hea
t exc
hang
er s
imul
atio
n w
ith
no p
ress
ure
drop
s in
both
side
s.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s17
3
Solu
tion:
Follo
w th
e st
ep-b
y-st
ep in
stru
ctio
ns to
solv
e th
e pr
oble
m.
1-O
pen
a ne
w c
ase.
2-A
dd a
new
com
pone
nt li
st.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
174
3-Se
lect
the
com
pone
nts
from
the
Com
pone
nts
list
and
then
clo
se t
he a
ctiv
e w
indo
w b
y cl
icki
ng o
n cr
oss b
utto
n (a
ll pr
oces
s com
pone
nts s
houl
d be
ent
ered
in th
is st
ep).
4-Th
e cr
oss
butto
n is
not
see
n on
the
figur
e an
d yo
u co
uld
mov
e th
e ac
tive
win
dow
to s
ee
the
cros
s but
ton
in o
rder
to c
lose
it.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s17
5
5-Se
lect
the
Flui
d Pa
ckag
e (M
ake
sure
sele
ctin
g C
ompo
nent
Lis
t -1i
n th
e co
mpo
nent
list)
.
6-A
dd a
new
Flu
id P
acka
ge.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
176
7-Se
lect
the
Peng
Rob
inso
n or
SRK
equ
atio
n of
stat
e fr
om P
rope
rty
Pack
age.
8-C
lose
the
Flu
id P
acka
ge b
y cl
icki
ng o
n cr
oss
butto
n. A
fter
this
ste
p, i
t is
pos
sibl
e to
im
port/
expo
rt th
e Fl
uid
Pack
age.
Th
en e
nter
to S
imul
atio
n En
viro
nmen
t.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s17
7
9-D
rag
a m
ater
ial s
tream
to th
e PF
D a
nd c
hang
e its
nam
e to
Hot
-in, t
hen
ente
r its
vap
or
frac
tion,
pre
ssur
e an
d m
olar
flow
rate
in th
e W
orks
heet
/Con
ditio
ns P
age.
10-S
ave
the
sim
ulat
ion
wor
k (e
.g.,
pro
blem
-4).
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
178
11-I
n th
e W
orks
heet
/Com
posit
ion
page
, ent
er m
ass
fract
ion
of th
e co
mpo
nent
s, cl
ick
OK
and
cl
ose
the
activ
e w
indo
w to
retu
rn to
PFD
.
12-D
rag
anot
her
stre
am to
the
PFD
and
cha
nge
its n
ame
to H
2O-in
, ent
er it
s te
mpe
ratu
re,
pres
sure
in th
e W
orks
heet
/Con
ditio
ns p
age.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s17
9
13-I
n th
e W
orks
heet
Com
posi
tion
page
, ent
er 1
for m
ole
fract
ion
of w
ater
and
0 fo
r the
rest
and
clic
k O
K a
nd c
lose
the
activ
e w
indo
w.
14-S
elec
t a h
eat e
xcha
nger
from
the
Obj
ect P
alet
te (F
4) a
nd d
rag
it to
the
PFD
.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
180
15-
Dou
ble
clic
k on
th
e he
at
exch
ange
r an
d en
ter
inle
t an
d ou
tlet
stre
ams
on
the
Des
ign/
Con
nect
ions
pag
e
16-I
n th
e D
esig
n/Pa
ram
eter
s pag
e en
ter 0
for p
ress
ure
drop
s of b
oth
sides
.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s18
1
17-
In th
e sa
me
page
cha
nge
the
heat
exc
hang
er m
odel
to W
eigh
ted
and
then
incr
ease
the
inte
rval
s to
50 to
impr
ove
accu
racy
.
18-I
n th
e D
esig
n/Sp
ecs p
age,
it is
seen
that
Deg
rees
of F
reed
om is
2.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
182
19-E
nter
60
ºC fo
r the
Hot
-out
tem
pera
ture
in th
e W
orks
heet
/Con
ditio
ns p
age.
20-I
t is s
een
in th
e D
esig
n/Sp
ecs p
age
that
the
Deg
rees
of F
reed
om a
re re
duce
d to
1.
Tuto
rial
2R
eact
ors
&H
eatE
xcha
nger
s18
3
21-I
n th
e W
orks
heet
/Con
ditio
ns p
age,
ent
er 5
0 ºC
for H
2O-o
ut te
mpe
ratu
re.
22-I
t can
be
seen
in th
e D
esig
n/Sp
ecs p
age
that
the
Deg
rees
of F
reed
om a
re re
duce
d to
0.
Pro
cess
Sim
ulat
ion
usin
gH
YSYS
184
23-A
s se
en in
the
Wor
kshe
et/C
ondi
tions
pag
e, th
e m
inim
um fl
ow ra
te o
f the
coo
ling
wat
er is
ca
lcul
ated
to b
e 23
.16
kmol
e/hr
.
24-S
o th
e pr
oces
s is s
imul
ated
.
