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FEED mol% kmol
Methane CH4 0.24 1440
Ethylene C2H4 0.46 2760
Ethane C2H6 0.2 1200
Propylene C3H6 0.08 480
Propane C3H8 0.02 120
1.00 6000
Flow 6000 kmolh-1
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DIRECT SEQUENCE
0.6369
FEED
FEED mol% kmol
Methane CH4 0.24 1440Ethylene C2H4 0.46 2760
Ethane C2H6 0.2 1200
Propylene C3H6 0.08 480
Propane C3H8 0.02 120
1.00 6000
Flow 6000 kmolh-1
10!ar
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BOTTOMS mol% kmol
Methane CH4 0.0033 14.6124
Ethylene C2H4 0."92 2621.376
Ethane C2H6 0.2692 1192.0176
Propylene C3H6 0.1084 479.99"2
Propane C3H8 0.0271 119.9988
1.00 4428
Flow 4428 kmolh-1
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Product 1 mol% kmol
Product 1 Methane CH4 0.907 142".804 #99% $e&
Methane Ethylene C2H4 0.088 138.336 #'"% $e&
Ethane C2H6 0.00" 7.86
Propylene C3H6 0.000 0
Propane C3H8 0.000 0
1.00 1"72
Flow 1"72
Product 2
Ethylene
6000
Pro
MethaneEthylene
Ethane
Propylene
Propane
6001 Flow
kmolh-1
10!ar
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Product 3
Ethane
Product 3
Methane CH4
Ethylene C2H4
Ethane C2H6
Propylene C3H6
Propane C3H8
Flow 1788
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Keys
()*ht CH4 0.0033 #1% o+ ,n)t)al +or 99% $eo/ery&
Hea/y C2H4 0.088 # '"% $eo/ery&
uct 2 mol% kmol
CH4 0.00"" 14."2""C2H4 0.989" 2613.269"
C2H6 0.00" 13.20"
C3H6 0 0
C3H8 0 0
1.00 2641
2641 kmolh-1
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mol% kmol
0 0
0.00" 8.94
0.6"94 1179.0072
0.268" 480.078
0.0671 119.9748
1.00 1788
Keys
()*ht C2H4 0.00"
Hea/y C2H6 0.00"
kmolh-1
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INDIRECT SEQUENCE
TOPS
Methane CH4Ethylene C2H4
Ethane C2H6
Propylene C3H6
Propane C3H8
Flow 4307
FEED
FEED mol% kmol
Methane CH4 0.24 1440Ethylene C2H4 0.46 2760
Ethane C2H6 0.2 1200
Propylene C3H6 0.08 480
Propane C3H8 0.02 120
1.00 6000
Flow 6000 kmolh-1
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)retColmn 1 Colmn 2
Cool)n* ty #Mh& -12260 -101800
Heat)n* ty #Mh& 17020 103400
M)n. $e5 $at)o 0."78 2.299E5ternal $e5 $at)o 0.637 2."19
Methane CH4
Ethylene C2H4
Ethane C2H6
Propylene C3H6
Propane C3H8
Total
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mol% kmol Prod
0.3344 1440.2608 Met0.6378 2747.0046
0.0278 119.7346
0 0
0 0 Prod
1.00 4307 Methane
Ethylene
Ethane
Propylene
Propane
Flow
Keys
()*ht C2H4 0.00769923
Hea/y C2H6 0.0278 Product 2
Ethylene
6000
Product 3
Ethane
6000
kmolh-1
10!ar
10!a
r
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Product 3 mol% kmol
Methane CH4 0 0
Ethylene C2H4 0.0077 13.0361
Ethane C2H6 0.638 1080.134
Propylene C3H6 0.283" 479.96""
Propane C3H8 0.0709 120.0337
1.00 1693.1693
Flow 1693
,n)retColmn 1 Colmn 2
-"9370 -40"70
96780 933"
1.093 2.0231.202 2.22"
Feed Dstllate Product 1 Product 2mol% kmol mol% kmol mol% kmol mol% kmol
0.24 1440.00 0.33 1440.26 0.91 1426.34 0.00" 13.71
0.46 2760.00 0.64 2747.00 0.09 137.72 0.9"2 2609."614
0.20 1200.00 0.03 119.73 0.00 0.94 0.043 118.7286
0.08 480.00 0.00 0.00 0.00 0.00 0.00 0.00
0.02 120.00 0.00 0.00 0.00 0.00 0.00 0.00
1.00 6000 1.00 4307 1.00 1565 1.00 2742
kmolh-1
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ct 1
ane
ct 1 mol% kmol
CH4 0.911 1426.341 #99% $e& ()*ht
C2H4 0.088 137.72 #'"% $e& Hea/y
C2H6 0.001 0.939
C3H6 0.000 0
C3H8 0.000 0
1.00 1"6"
1"6"
Product 2 mol% kmol
Methane CH4 0.00" 13.71
Ethylene C2H4 0.9"2 2609."614
Ethane C2H6 0.043 118.7286Propylene C3H6 0 0
Propane C3H8 0 0
1.00 2742
Flow 2742
kmolh-1
kmolh-1
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Product 3mol% kmol
0.00 0.00
0.01 13.04
0.64 1080.13
0.28 479.97
0.07 120.03
1.00 1693
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Keys
CH4 0.00" )al +or 99% $eo/ery&
C2H4 0.088 '"% $eo/ery&
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)ret ,n)ret
1 2 1 2
Conener ty #h& 12.26 101.8 "9 41-101.9 -"2.93 -62.92 -103.4
$e!o)ler ty #h& 17.02 103.4 97 9
-43.43 -20.37 -19.68 -"2.31M)n. $e5 $at)o 0."78 2.299 1.093 2.023
E5ternal $e5 $at)o 0.637 2."19 1.202 2.22"
)ret ,n)ret
1 2 1 2
Conener ty #h& 12.26 101.8 "9 41-101.9 -"2.93 -62.92 -103.4
$e!o)ler ty #h& 17.02 103.4 97 9
-43.43 -20.37 -19.68 -"2.31
$e5 $at)o
:)eal ;#
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-101.9 -"2.93 -62.92 -103.4
$e>*erant
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co$%&
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Conener ty #h&
$e!o)ler ty #h&
M)n. $e5 $at)o
E5ternal $e5 $at)o
co$%&
Conener ty #h&
$e!o)ler ty #h&
M)n. $e5 $at)o
E5ternal $e5 $at)o
Conener
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1! "ar # "ar
)ret ,n)ret
1 2 1
Conener ty #h& 10."9 99.77 64.7"
-113.4 -72.3 -79.8
$e!o)ler ty #h& 7.93 93.91 97.43
-64.1 -42.9 -42.3
M)n. $e5 $at)o 0."78 1.937 0.919E5ternal $e5 $at)o 0.637 2.131 1.011
)ret ,n)ret
1 2 1
Conener ty #h& 10."9 99.77 64.7"
-113.4 -72.3 -79.8
$e>*erant
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)ret ,n)ret
1 2 1 211.84 99.77 64.67 36."9
-94.4 -39.9 -"1.7 -9".8
20.90 93.91 104.03 7.86
-29.3 -".0 -4.3 -39.20.621 2.782 1.291 2.146
0.683 3.060 1.420 2.361
)ret ,n)ret
1 2 1
Conener ty #h& 11.84 99.77 64.67
-94.4 -39.9 -"1.7$e>*erant
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)ret ,n)ret
1 2 1Conener ty #h& 11.89 111.19 68.8"
-88.7 -29.8 -43.2
$e>*erant
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1
Keys
()*ht CH4
Hea/y C2H4
2
40."7
-103.4
9.34
-"2.3
2.023 Keys2.22" ()*ht C2H4
Hea/y C2H6
2
40."7
-103.4
-108.4
164.6
308
3".34
"8.91
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2
36."9
-9".8-100.79
172.21
308
28.8"
48.09
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237.19
-90.0
-94.97178.03308
27.1"
4".2"
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2
Keys
0.0033 ()*ht C2H4 0.00"
0.088 Hea/y C2H6 0.00"
Keys
0.007699 ()*ht CH4 0.00"
0.0278 Hea/y C2H4 0.088
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B,SE C,SE
)ret ,n)ret
1 2 1 2
Conener ty #h& 12.26 101.8 "9.4 41
-101.9 -"2.93 -62.92 -103.4
$e!o)ler ty #h& 17.02 103.4 96.8 9
-43.43 -20.37 -19.68 -"2.31
M)n. $e5 $at)o 0."78 2.299 1.093 2.023
E5ternal $e5 $at)o 0.637 2."19 1.202 2.22"
)ret ,n)ret
1 2 1 2
Conener ty #h& 12.26 101.8 "9 41-101.9 -"2.93 -62.92 -103.4
$e>*erant
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co$%& 2! "ar 2! "ar 2! "ar
)ret
1 2
Conener ty #h& 11.89 111.19
-88.7 -29.8$e!o)ler ty #h& 24.77 113.04
-18.3 7.0
M)n. $e5 $at)o 0.694 3.297
E5ternal $e5 $at)o 0.763 3.627
)ret
1 2
Conener ty #h& 11.96 114.97
-84.0 -21.4
$e>*erant
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FEED mol%
Methane CH4 0.24
Ethylene C2H4 0.46
Ethane C2H6 0.2
Propylene C3H6 0.08
Propane C3H8 0.02
1.00
-eat I.te/rato. Feas"lty 0 SINE CC
Colmn 1
Cool)n* :ater $etrn
$e>*erant Conener
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Cool)n* :ater 1 ;Cool)n*
1 Cool)n*
E/aporator
:)eal;
@m)n* n0.6 :atal
$eBet *erat)on Conener; ;on
OK
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Product 1
Methane CH4
Ethylene C2H4
Ethane C2H6
Propylene C3H6
Propane C3H8
Prot 1
h
Fro$ R/4
$eo/ery Methane#Fee& 0.99
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$eo/ery Ethylene#Fee& 0.0"
F(( $EF(D
2000 kPa
Fro$ S-4
M)n *erant
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11.96 hCool)n* :ater
2 ;
189.0 A 2 C
184 A E/apo
0.701087 :)e
13.976972 h @m)n* n0.6 :a
28.42 h
$eBet
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mol% kmol
0.908 142".626174
0.088 138.0131643
0.004 6.86"493"13
0 0
0 0
1.00 1"70."06237
GH ;on 11.89
GH
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Prot 2
Fro$ R/4
$eo/ery Ethylene #ott& 0.9698
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ool)n* 114.97 h
ool)n* 2"1.6 A
rator 246.64 A
al; 0.2690"611
al "1."""4"64 h
eat)n* 116.94 h
at)n* 289.9 A
ner 294.9 A
al; 0.19"62926
al 37.48"69"8 h
n 1"2.46 h
t Re5ecto. 6or Re"oler
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Product 2 mol% kmol
Methane CH4 0.006 14.37
Ethylene C2H4 0.990 2"42.91
Ethane C2H6 0.004 11.49
Propylene C3H6 0 0
Propane C3H8 0 0
1.00 2"68.77972
E
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