copy of material balance 2012

7/24/2019 Copy of Material Balance 2012

1/24

PLANT LOAD: 100 %

NG: 44297 Nm3/hr FEED GAS: 34551.66

PROCESS AIR: 45000 Nm3/hr FEL GAS: 9745.34

S/C: 3.3

NG/AIR: 0.73

!2 R"#$#": 1&00 Nm3/hr

Pr'()#*+',: m*/(-$

C

!2 r"#$#"

!2 1332N2 37&

CO 54

CO2 1&

C!4 1&

T'*- 1&00

NG FEED

N2 120.930&1

CO2 276.4132&

C!4 33369.993

C2!6 701.39&7

C3!& 62.1929&&

C4!10 13.&20664

C5!12 6.910332

T'*-: 34551.66Nm3/hr

R1102


2/24


3/24

Nm3/hr

Nm3/hr

G- ",*

N2

CO2

O2

!2O

CO

T'*-

S*"-m: 11391&.4 Nm3/hr

!2 1332 1: 26741.&1

N2 49&.930& 2: 25&25.32

CO 54 3: 7&4.3227

CO2 294.4133 4: &2.9239&

C!4 333&7.99 5: 20.731

C2!6 701.39&7 6: 6.910332

C3!& 62.19299

C4!10 13.&2066

C5!12 6.910332

T'*-: 36351.66 Nm3/hr

FEL GAS

!1301Pr+m-r$ R"'rm"r


4/24

N2 34.10&69

CO2 77.96272

C!4 9412.049

C2!6 197.&304

C3!& 17.54161

C4!10 3.&9&136C5!12 1.94906&

T'*-: 9745.34


5/24

Pr'#" A+r

N2 35100

O2 9450

CO2 45

Ar 405

T'*-: 45000 Nm3/hr

!2 &0576.13 1: 3150

N2 49&.930&

CO 26795.&1

CO2 272.&133

C!4 &346.99&

!2O &7219.&

T'*-: 203710.5Nm3/hr

AIR

R1301S"#',(-r$ R"'rm"r

C'm)*+',


6/24

N2

O2

CO2

Ar

T'*-:


7/24

!2 &0576.13 1: 4417.449 !2 &4993.5&

N2 3559&.93 N2 3559&.93

CO 20495.&1 CO 20495.&1

CO2 9722.&13 CO2 14140.26

C!4 5196.99& C!4 779.5497

!2O 93519.& !2O &9102.35

Ar 405 Ar 405

T'*-: 245515.5Nm3/hr T'*-: 245515.5

R1301S"#',(-r$ R"'rm"r


8/24


9/24

1: 15371.&5 !2 100365.4 1:

N2 3559&.93

CO 5123.951

CO2 29512.12

C!4 779.5497

!2O 73730.5

Ar 405

Nm3/hr T'*-: 245515.5 Nm3/hr

R1401!TS

R


10/24


11/24

T' REA P

!2

N2

CO2

!2O

T'*-:

1024.79 !2 101390.2

N2 3559&.93

CO 4099.161

CO2 30536.91

C!4 779.5497

!2O 72705.71

Ar 405

T'*-: 245515.5Nm3/hr

-*"r R"m'": 0.9&

402TS

8ENFIELD


12/24


13/24

ANT: 0.94

202.7&04

35.59&93

2&704.69

21&1.171

31124.24Nm3/hr

-*"r R"m'": 0.7&

!2 1011&7.4 !2 1011&7.4 1:

N2 35563.33 N2 35563.33 2:

CO 4099.161 CO 4099.161

CO2 1&32.214 CO2 1&32.214

C!4 779.5497 C!4 779.5497

!2O 1410.491 !2O 310.30&

Ar 405 Ar 405

T'*-: 145277.2Nm3/hr T'*-: 144177 Nm3/hr

1504 R25


14/24


15/24

&24.4965 !2 &6416.47 1: &06.1743

3074.371 N2 35563.33 2: 717.3532

CO 1024.79

CO2 1007.71&

C!4 779.5497

!2O 1134.&04

Ar 405

C!3O! 3&9&.&67

T'*-: 130230.5Nm3/hr

1 R2502


16/24


17/24

"*h-,' r"m'": 0.99

-*"r r"m'": 0.94

!2 &112&.53 C!3O! 536&.171

N2 35563.33 !2O 1&24.52

CO 307.4371

CO2 201.5436 T'*- 7192.691 Nm3/hr

C!4 779.5497

!2O 1940.979

Ar 405

C!3O! 5422.395

T'*-: 12574&.&Nm3/hr

"*h-,' S"-r-*'r


18/24


19/24

!2 &112&.53 1: 307.4371 !2 79345.&2

N2 35563.33 2: 201.5436 N2 35563.33

CO 307.4371 3: 54.22395 C!4 1342.754

CO2 201.5436 !2O &&1.2069

C!4 779.5497 Ar 405

!2O 116.45&7

Ar 405 T'*-: 11753&.1

C!3O! 54.22395

T'*-: 11&556.1Nm3/hr

R1701


20/24


21/24

Nm3/hr


22/24


23/24

Primary reformer

CO2 ; !2 < CO ; !2O CO2: 0.4

C!4 ; 2!2O =< CO2 ; 4!2 C!4: 0.75

C2!6 ; 2!2O =< C!4 ; CO2 ; 3!2 C2!6: 1

C3!& ; 2!2O =< C2!6 ; CO2 ; 3!2 C3!&: 1

C4!10 ; 2!2O =< C3!& ; CO2 ; 3!2 C4!10: 1

C5!12 ; 2!2O =< C4!10 ; CO2 ; 3!2 C5!12: 1

Burner in H-13-01

C!4 ; 2O2 < CO2 ; 2!2O C!4: 1

C2!6 ; 5/2O2 < 2CO ; 3!2O C2!6: 1

C3!& ; 7/2O2 < 3CO ; 4!2O C3!&: 1

C4!10 ; 9/2O2 < 4CO ; 5!2O C4!10: 1

C5!12 ; 11/2O2 < 5CO ; 6!2O C5!12: 1

Combustion Top of Secondary Reformer

C!4 ; 2CO ; 3O2 < 3CO2 ; 2!2O O2: 1

Reaction in Secondary Reformer

C!4 ; !2O =< CO2 ; !2 C!4: 0.&5

HTS

CO ; !2O =< CO2 ; !2 CO: 0.75

LTS

CO ; !2O =< CO2 ; !2 CO: 0.2

Methano 1

CO2 ; 3!2 =< C!3O! ; !2O CO2: 0.45

CO ; 4!2 =< C!3O! CO: 0.75

Methano !

CO2 ; 3!2 =< C!3O! ; !2O CO2: 0.&

CO ; 4!2 =< C!3O! CO: 0.7

Methanator

CO ; 3!2 =< C!4 ;!2O CO: 1

CO2 ; 4!2 =< C!4 ; 2!2O CO2: 1

C!3O! ; !2 =< C!4 ; !2O C!3O!: 1


24/24

1: 26741.&1

2: 25&25.32

3: 7&4.3227

4: &2.9239&

5: 20.731

6: 6.910332

1:

2:

3:

4:

5:

1: 3150

1: 4417.449

1: 15371.&5

1: 1024.79

1: &24.4965

2: 3074.371

1: &06.1743

2: 717.3532

1: 307.4371

2: 201.5436

3: 54.22395

copy of material balance 2012

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