62449961-ammonia-heat-mat-balance.doc

7/25/2019 62449961-Ammonia-Heat-Mat-Balance.doc

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Project: SPIC AMMONIA REVAMP ****** HEAT AND MATERIAL BALANCE ******

Stream Number

Descritio!

P"ase

#$% #$#&'$( #$( #$) #$ #$+ #$'

Process

Na"t"a to

%)(#

Rec,c-e ",.ro/e!

0rom (%$#

Proc1 Na"t"a 2

rec1 H# at %)(#

out-et

Proc1 Na"t"a 2

rec H# at %%$)

out-et

Process Steam

0rom %('

Primar, re0ormer

%)$$ out-et

Process Air 0rom

%)(( to %%$

LI34ID VAPOR VAPOR VAPOR VAPOR VAPOR VAPOR

Pressure Kg/cm2 a 43.0 42.0 39.4 39.4 43.5 29.9 32.0

Temperature oC 40 40 375 375 471 787 490

Dry gas rate Kg/hr 0 790 27608 27608 0 67164 59941

team rate Kg/hr 0 3 3 3 1111552 72003 282

!"#u"$ rate Kg/hr 26818 0 0 0 0 0 0

Tota% rate Kg/hr 26818 793 27611 27611 1111552 139167 60223

Dry &as '%o( rate )m3/hr 0 2043 8032 8032 0 114864 46391

team to $ry gas mo%e rat"o *.a 0.00 0.00 0.00 *.a 0.78 0

Dry gas compos"t"o*

)2 +o%e , *.a 24.72 6.29 6.29 *.a 0.44 78.11

- +o%e , *.a 0.32 0.08 0.08 *.a 0.01 0.942 +o%e , *.a 0.00 0.00 0.00 *.a 0.00 20.95

C4 +o%e , *.a 0.76 0.19 0.19 *.a 9.98 0.00

C2 +o%e , *.a 0.00 0.00 0.00 *.a 15.65 0.00

C +o%e , *.a 0.00 0.00 0.00 *.a 11.55 0.00

2 +o%e , *.a 74.20 18.87 18.87 *.a 62.37 0.00

)3 +o%e , *.a 0.00 0.00 0.00 *.a 0.00 0.00

)aphtha +o%e , *.a 0.00 74.57 74.57 *.a 0.00 0.00

u%phur Ppm (t 5.0 0 0.5 0.5 *.a 0 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 22.5 22.5 22.5 0.0 22.5 1616.8

- Kgmo%/hr 0.0 0.3 0.3 0.3 0.0 0.3 19.5

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 433.5

C4 Kgmo%/hr 0.0 0.7 0.7 0.7 0.0 511.5 0.0C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 801.8 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 592.0 0.0

2 Kgmo%/hr 0.0 67.6 67.6 67.6 0.0 3196.5 0.0

20 Kgmo%/hr 0.0 0.2 0.2 0.2 6192.2 3996.8 15.6

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 267.2 0.0 267.2 267.2 0.0 0.0 0.0

u%phur Kgmo%/hr 5.0 0 5.0 5.0 0 0 0

Tota% '%o( rate Kgmo%/hr 267.2 91.3 358.5 358.5 6192.2 9121.6 2085.4

+ 100.36 8.69 77.01 77.01 18.02 15.26 28.88

*tha%py &Ca%/hr 0.13 0.09 7.31 7.31 89.94 102.33 4.95


2/29


Stream Number

Descritio!

P"ase

#$5 #$6&($% #%$&5$) #%% #%# #%( #%)

Seco!.ar,

Re0ormer %%$out-et

HT S"i0t 7uar.

Vesse- i!-et

Tai- /as 0ue- 0rom

P7HR4

Na"t"a 0ue- to

%)$$

Pre"eate.

combustio! air

8-ue /as at

re0ormer 0ire bo9e9it

8-ue /as

A0ter %%$

VAPOR VAPOR VAPOR LI34ID VAPOR VAPOR VAPOR

Pressure Kg/cm2 a 29.5 29.1 2.3 9.0 140 mm(c g 12 mm(c g 20.0 mm(c g

Temperature oC 972.5 380 40 40 277 940 871

Dry gas rate Kg/hr 120071 120071 2940 0 179183 177404 177404

team rate Kg/hr 79318 79318 0 0 4435 21906 21906

!"#u"$ rate Kg/hr 0 0 0 9836 0 0 0

Tota% rate Kg/hr 199389 199389 2940 9836 183619 199310 199310

Dry &as '%o( rate )m3/hr 164816 164816 2938 0 138678 131317 131317

team to $ry gas mo%e rat"o 0.60 0.60 0.00 *.a 0.04 0.21 0.21

Dry gas compos"t"o*

)2 +o%e , 22.29 22.29 44.45 *.a 78.11 83.46 83.46- +o%e , 0.27 0.27 12.66 *.a 0.94 1.29 1.29

2 +o%e , 0.00 0.00 0.00 *.a 20.95 2.72 2.72

C4 +o%e , 0.27 28.71 *.a 0.00 0.00 0.00

C2 +o%e , 10.70 10.70 0.00 *.a 0.00 12.53 12.53

C +o%e , 14.94 14.94 0.00 *.a 0.00 0.00 0.00

2 +o%e , 51.53 51.53 13.96 *.a 0.00 0.00 0.00

)3 +o%e , 0.00 0.00 0.21 *.a 0.00 0.00 0.00

)aphtha +o%e , 0.00 0.00 0.00 *.a 0.00 0.00 0.00

u%phur Ppm (t 0 0 0 *.a 0 0 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 1639.3 1639.3 58.3 0.0 4832.8 4889.8 4889.8

- Kgmo%/hr 19.7 19.7 16.6 0.0 58.2 75.8 75.8

2 Kgmo%/hr 0.0 0.0 0.0 0.0 1296.2 159.2 159.2C4 Kgmo%/hr 20.1 20.1 37.6 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 787.0 787.0 0.0 0.0 0.0 734.0 734.0

C Kgmo%/hr 1098.2 1098.2 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 3789.0 3789.0 18.3 0.0 0.0 0.0 0.0

20 Kgmo%/hr 4402.9 4402.9 0.0 0.0 246.2 1216.0 1216.0

)3 Kgmo%/hr 0.0 0.0 0.3 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 98.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 800 0 0 0


+ 16.96 16.96 22.43 100.36 28.54 28.17 28.17

*tha%py &Ca%/hr 136.15 75.42 0.08 0.04 743 62.49 58.12


3/29


Stream Number

Descritio!

P"ase

#% #%+ #%' #%5 #%6 ##$&+$% ##%

8-ue /as

A0ter %(+A

7-ue /as

A0ter %('

8-ue /as

A0ter %(+B

8-ue /as

To stac

Tota- steam

7e!erate. i!

%%$+

HT turbi!e

steam 0rom %(+A

to "ea.er

Process steam

0rom )

;/&cm##a "ea.er

to %('

VAPOR VAPOR VAPOR VAPOR VAPOR VAPOR VAPOR

Pressure Kg/cm2 a 45 mm(c g 66 mm(c g 124 mm(c g 0 mm(c g 112.0 106.0 44.5

Temperature oC 684 569 363 684 318.1 485 365

Dry gas rate Kg/hr 177404 177404 177404 177404 0 0 0

team rate Kg/hr 21906 21906 21906 21906 158600 158600 111552

!"#u"$ rate Kg/hr 0 0 0 0 0 0 0

Tota% rate Kg/hr 199310 199310 199310 199310 158600 158600 111552

Dry &as '%o( rate )m3/hr 131317 131317 131317 131317 0 0 0

team to $ry gas mo%e rat"o 0.21 0.21 0.21 0.21 *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , 83.46 83.46 83.46 83.46 *.a *.a *.a- +o%e , 1.29 1.29 1.29 1.29 *.a *.a *.a

2 +o%e , 2.72 2.72 2.72 2.72 *.a *.a *.a

C4 +o%e , 0.00 0.00 0.00 0.00 *.a *.a *.a

C2 +o%e , 12.53 12.53 12.53 12.53 *.a *.a *.a

C +o%e , 0.00 0.00 0.00 0.00 *.a *.a *.a

2 +o%e , 0.00 0.00 0.00 0.00 *.a *.a *.a

)3 +o%e , 0.00 0.00 0.00 0.00 *.a *.a *.a

)aphtha +o%e , 0.00 0.00 0.00 0.00 *.a *.a *.a

u%phur Ppm (t 0 0 0 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 4889.8 4889.8 4889.8 4889.8 0.0 0.0 0.0

- Kgmo%/hr 75.8 75.8 75.8 75.8 0.0 0.0 0.0

2 Kgmo%/hr 159.2 159.2 159.2 159.2 0.0 0.0 0.0C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 734.0 734.0 734.0 734.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 1216.0 1216.0 1216.0 1216.0 8803.8 8803.8 6192.2

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 28.17 28.17 28.17 28.17 18.02 18.02 18.02

*tha%py &Ca%/hr 46.52 39.82 27.89 16.69 102.63 126.18 83.25


4/29


Stream Number

Descritio!

P"ase

### ##(&(#( ##)&+(+ ##+ #5%

Atomi


5/29


Stream Number

Descritio!

P"ase

($%$6 ($# ($( ($) ($ ($+ ($'

HT S"i0t

7uar. Vesse-

I!-et

HT S"i0t %st

Be. out-et to

%(6

HT S"i0t #!.

Be. i!-et

8rom %(6

HT S"i0t #!.

Be. out-et

To %%)

Process 7as

Out-et 0rom

%%)

3ue!c" =ater

To %%%%

LT S"i0t

I!-et /as

VAPOR VAPOR VAPOR VAPOR VAPOR LI34ID VAPOR

Pressure Kg/cm2 a 29.1 28.7 28.5 28.2 27.9 34.0 27.8

Temperature oC 380 449.2 350 363 302.5 126 205

Dry gas rate Kg/hr 120071 133869 133869 136622 136622 0 136622

team rate Kg/hr 79318 65521 65521 62768 62768 0 80210

!"#u"$ rate Kg/hr 0 0 0 0 0 17440 0

Tota% rate Kg/hr 199389 199390 199390 199390 199390 17440 216832

Dry &as '%o( rate )m3/hr 164816 181982 181982 185408 185408 0 185408

team to $ry gas mo%e rat"o 0.60 0.45 0.45 0.42 0.42 *.a 0.54

Dry gas compos"t"o*

)2 +o%e , 22.29 20.19 20.19 19.82 19.82 *.a 19.82

- +o%e , 0.27 0.24 0.24 0.24 0.24 *.a 0.242 +o%e , 0.00 0.00 0.00 0.00 0.00 *.a 0.00

C4 +o%e , 0.27 0.25 0.25 0.24 0.24 *.a 0.24

C2 +o%e , 10.70 19.13 19.13 20.62 20.62 *.a 20.62

C +o%e , 14.94 4.09 4.09 2.17 2.17 *.a 2.17

2 +o%e , 51.53 56.10 56.10 56.91 56.91 *.a 56.91

)3 +o%e , 0.00 0.00 0.00 0.00 0.00 *.a 0.00

)aphtha +o%e , 0.00 0.00 0.00 0.00 0.00 *.a 0.00

u%phur Ppm (t 0 0 0 0 0 *.a 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 1639.3 1639.3 1639.3 1639.3 1639.3 0.0 1639.3

- Kgmo%/hr 19.7 19.7 19.7 19.7 19.7 0.0 19.7

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 20.1 20.1 20.1 20.1 20.1 0.0 20.1C2 Kgmo%/hr 787.0 1552.9 1552.9 1705.7 1705.7 0.0 1705.7

C Kgmo%/hr 1098.2 332.4 332.4 179.6 179.6 0.0 179.6

2 Kgmo%/hr 3789.0 4554.8 4554.8 4707.7 4707.7 0.0 4707.7

20 Kgmo%/hr 4402.9 3637.0 3637.0 3484.2 3484.2 968.1 4452.4

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 16.96 16.96 16.96 16.96 16.96 18.02 17.04

*tha%py &Ca%/hr 75.42 76.78 66.97 67.14 61.20 2.16 63.36


6/29



7/29

Stream Number

Descritio!

P"ase

($5 ($6 (%$&)$% (%% (#$&)(# (#%&'(% (##&'(#

LT S"i0t

Out-et /as

To %$

Process /as

8rom %$

To %%%)

Process /as

8rom %%%)

To %%' a&B

Process

Co!.e!sate

8rom %%%)

LP B8=

8rom %%(

To %'$(

Deaerate.

B8= to %#(

HP B8= 0rom

%#( to %(

a!. %(6

VAPOR MI>ED VAPOR LI34ID LI34ID LI34ID LI34ID

Pressure Kg/cm2 a 27.5 27.1 26.9 26.9 3.7 127.0 126.5

Temperature oC 217.1 173 173 173 94 109 181

Dry gas rate Kg/hr 139454 139454 139454 0 0 0 0

team rate Kg/hr 77383 71942 71942 0 0 0 0

!"#u"$ rate Kg/hr 0 5441 0 5441 293945 300400 300400

Tota% rate Kg/hr 216837 216837 211396 5441 293945 300400 300400

Dry &as '%o( rate )m3/hr 188687 188687 188687 0 0 0 0

team to $ry gas mo%e rat"o 0.51 0.47 0.47 *.a *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , 19.45 19.45 19.45 *.a *.a *.a *.a

- +o%e , 0.23 0.23 0.23 *.a *.a *.a *.a

2 +o%e , 0.00 0.00 0.00 *.a *.a *.a *.aC4 +o%e , 0.24 0.24 0.24 *.a *.a *.a *.a

C2 +o%e , 22.10 22.10 22.10 *.a *.a *.a *.a

C +o%e , 0.27 0.27 0.27 *.a *.a *.a *.a

2 +o%e , 57.71 57.71 57.71 *.a *.a *.a *.a

)3 +o%e , 0.00 0.00 0.00 *.a *.a *.a *.a

)aphtha +o%e , 0.00 0.00 0.00 *.a *.a *.a *.a

u%phur Ppm (t 0 0 0 *.a *.a *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 1639.3 1639.3 1639.3 0.0 0.0 0.0 0.0

- Kgmo%/hr 19.7 19.7 19.7 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 20.1 20.1 20.1 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 1862.6 1862.6 1862.6 0.0 0.0 0.0 0.0C Kgmo%/hr 22.6 22.6 22.6 0.0 0.0 0.0 0.0

2 Kgmo%/hr 4864.6 4864.6 4864.6 0.0 0.0 0.0 0.0

20 Kgmo%/hr 4295.5 4295.5 3993.5 302.0 16316.7 16674.0 16674.0

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 1704 1704 1702 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 63.56 56.52 55.57 0.95 27.63 32.88 55.49



8/29

Stream Number

Descritio!

P"ase

(#(#( (#)&+)) (#&)(( (#'&+#' (#5 (#6

B8=

8rom %(6

To %%$+

B8= 0rom

%( to

au91 Boi-er

LP steam 0rom

%$ to )

;/&cm#a "ea.er

? %%%'A

LP steam 0rom

#1% ;/&cm#a

"ea.er to %'$(

Deaerate.

B8= 0rom

Deaerator

LP steam

Boi-er %$

[email protected]@!

LI34ID LI34ID VAPOR VAPOR LI34ID LI34ID

Pressure Kg/cm2 a 126.0 126.0 5.0 2.1 1.4 5.0

Temperature oC 238 218 151 243 109 151

Dry gas rate Kg/hr 0 0 0 0 0 0

team rate Kg/hr 0 0 12810 10763 0 0

!"#u"$ rate Kg/hr 161000 139400 0 0 301947 200

Tota% rate Kg/hr 161000 139400 12810 10763 301947 200

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0

team to $ry gas mo%e rat"o *.a *.a *.a *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , *.a *.a *.a *.a *.a *.a

- +o%e , *.a *.a *.a *.a *.a *.a2 +o%e , *.a *.a *.a *.a *.a *.a

C4 +o%e , *.a *.a *.a *.a *.a *.a

C2 +o%e , *.a *.a *.a *.a *.a *.a

C +o%e , *.a *.a *.a *.a *.a *.a

2 +o%e , *.a *.a *.a *.a *.a *.a

)3 +o%e , *.a *.a *.a *.a *.a *.a

)aphtha +o%e , *.a *.a *.a *.a *.a *.a

u%phur Ppm (t *.a *.a *.a *.a *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 8937.0 7737.6 711.1 597.5 16760.9 11.1

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0

Tota% '%o( rate Kgmo%/hr 8937.0 7737.6 711.1 597.5 16760.9 11.1

+ 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 39.55 31.14 8.44 7.60 32.96 0.03



9/29

Stream Number

Descritio!

P"ase

(($ ()$&)$( ()% ()( ()) ()

Co!.e!sate

8rom %()

To %'$(

Co!erte.

7as 0rom %%(%

To %)

Co!erte.

7as 0rom

%) to %%)

Co!1 7as 0rom

%%) to

Met"a!ator

S,!1 7as 0rom

Met"a!ator

To %(

S,!1 7as

8rom %(

To %)

MI>ED VAPOR VAPOR VAPOR VAPOR VAPOR

Pressure Kg/cm2 a 1.4 26.1 25.8 25.4 25.0 24.7

Temperature oC 109 70 179 305 335 220

Dry gas rate Kg/hr 0 57704 57704 57704 57055 57055

team rate Kg/hr 388 1452 1452 1452 2101 2101

!"#u"$ rate Kg/hr 927 0 0 0 0 0

Tota% rate Kg/hr 1315 59156 59156 59156 59156 59156

Dry &as '%o( rate )m3/hr 0 147116 147116 147116 144937 144937

team to $ry gas mo%e rat"o *.a 0.01 0.01 0.01 0.02 0.02

Dry gas compos"t"o*

)2 +o%e , *.a 24.96 24.96 24.96 25.32 25.32

- +o%e , *.a 0.30 0.30 0.30 0.31 0.31

2 +o%e , *.a 0.00 0.00 0.00 0.00 0.00C4 +o%e , *.a 0.31 0.31 0.31 0.76 0.76

C2 +o%e , *.a 0.10 0.10 0.10 0.3 ppm 0.3 ppm

C +o%e , *.a 0.34 0.34 0.34 0.6 ppm 0.6 ppm

2 +o%e , *.a 73.99 73.99 73.99 73.61 73.61

)3 +o%e , *.a 0.00 0.00 0.00 0.00 0.00

)aphtha +o%e , *.a 0.00 0.00 0.00 0.00 0.00

u%phur Ppm (t *.a 0 0 0 0 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 1637.5 1637.5 1637.5 1637.5 1637.5

- Kgmo%/hr 0.0 19.7 19.7 19.7 19.7 19.7

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 20.1 20.1 20.1 49.4 49.4

C2 Kgmo%/hr 0.0 6.7 6.7 6.7 0.0 0.0C Kgmo%/hr 0.0 22.6 22.6 22.6 0.0 0.0

2 Kgmo%/hr 0.0 4854.6 4854.6 4854.6 4759.7 4759.7

20 Kgmo%/hr 73.0 80.6 80.6 80.6 116.6 116.6

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0



+ 18.02 8.91 8.91 8.91 8.99 8.99

*tha%py &Ca%/hr 0.35 4.52 0.60 6.53 8.38 2.98



10/29

Stream Number

Descritio!

P"ase

()' ()5&'$% ()6 (5%

S,!1 7as 0rom

%) to %%+

S,! /as

8rom %%%(

To (%$#

Process

Co!.e!sate

8rom %%%(

Coo-i!/

=ater to

%%+

VAPOR VAPOR LI34ID LI34ID

Pressure Kg/cm2 a 24.5 24.2 24.3 5.0

Temperature oC 111 40 40 32

Dry gas rate Kg/hr 57055 56933 0 0

team rate Kg/hr 2101 359 0 0

!"#u"$ rate Kg/hr 0 0 1742 536600

Tota% rate Kg/hr 59156 57291 1742 536600

Dry &as '%o( rate )m3/hr 144937 144637 0 0

team to $ry gas mo%e rat"o 0.02 0.02 *.a *.a

Dry gas compos"t"o*

)2 +o%e , 25.32 25.32 *.a *.a

- +o%e , 0.31 0.30 *.a *.a

2 +o%e , 0.00 0.00 *.a *.aC4 +o%e , 0.76 0.76 *.a *.a

C2 +o%e , 0.3 ppm 0.3 ppm *.a *.a

C +o%e , 0.6 ppm 0.6 ppm *.a *.a

2 +o%e , 73.61 73.61 *.a *.a

)3 +o%e , 0.00 0.00 *.a *.a

)aphtha +o%e , 0.00 0.00 *.a *.a

u%phur Ppm (t 0 0 *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 1637.5 1634.1 0.0 0.0

- Kgmo%/hr 19.7 19.7 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 49.4 49.3 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0C Kgmo%/hr 0.0 0.0 0.0 0.0

2 Kgmo%/hr 4759.7 4749.9 0.0 0.0

20 Kgmo%/hr 116.6 19.9 96.7 29784.6

)3 Kgmo%/hr 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0

Tota% '%o( rate Kgmo%/hr 6583.1 6473.0 96.7 29784.6

+ 8.99 8.85 18.02 18.02

*tha%py &Ca%/hr 2.13 6.47 0.06 18.32



11/29

Stream Number

Descritio!

P"ase

)$%&(%$ )$# )$(&()$ )$) )$ )$+ )$'

Co!erte.

7as 0rom %%%)

To %%' A&B

Co!erte.

7as 0rom %%%

To %%%+

Co!erte.

7as 0rom %%(%

To %)

Semi -ea!

So-!1 8rom

%%%' A to B

Lea! So-!1

8rom %%%' A

To %%%'B

Semi -ea!

8rom %%%'B

To %#$

Lea! So-utio!

8rom %%'B

To %#%

VAPOR VAPOR VAPOR LI34ID LI34ID LI34ID LI34ID

-T +-T:-! ;-!-)C < CT:) 400 500 ;= &:-++-C >TCK

Pressure Kg/cm2 a 26.9 26.3 26.1 3.6 3.3 4.0 2.0

Temperature oC 173 126 70 124 128 108 111111

Dry gas rate Kg/hr 139454 139454 57704 0 0 0 0

team rate Kg/hr 71942 15502 1452 0 0 0 0

!"#u"$ rate Kg/hr 0 0 0 949072 347656 1631520 339773

Tota% rate Kg/hr 211396 154956 59156 949072 347656 1631520 339773

Dry &as '%o( rate )m3/hr 188687 188687 147116 0 0 0 0

team to $ry gas mo%e rat"o 0.47 0.10 0.01 *.a *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , 19.45 19.45 24.96 *.a *.a *.a *.a

- +o%e , 0.23 0.23 0.30 *.a *.a *.a *.a

2 +o%e , 0.00 0.00 0.00 *.a *.a *.a *.aC4 +o%e , 0.24 0.24 0.31 *.a *.a *.a *.a

C2 +o%e , 22.10 22.10 0.10 *.a *.a *.a *.a

C +o%e , 0.27 0.27 0.34 *.a *.a *.a *.a

2 +o%e , 57.71 57.71 73.99 *.a *.a *.a *.a

)3 +o%e , 0.00 0.00 0.00 *.a *.a *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 1639.3 1639.3 1637.7 *.a *.a *.a *.a

- Kgmo%/hr 19.7 19.7 19.7 *.a *.a *.a *.a

2 Kgmo%/hr 0.0 0.0 0.0 *.a *.a *.a *.a

C4 Kgmo%/hr 20.1 20.1 20.1 *.a *.a *.a *.a

C2 Kgmo%/hr 1862.6 1862.6 6.7 *.a *.a *.a *.a

C Kgmo%/hr 22.6 22.6 22.6 *.a *.a *.a *.a

2 Kgmo%/hr 4864.6 4864.6 4854.6 *.a *.a *.a *.a

20 Kgmo%/hr 3993.5 860.5 80.6 *.a *.a *.a *.a)3 Kgmo%/hr 0.0 0.0 0.0 *.a *.a *.a *.a

Tota% o%ut"o*

Car?o*ate t, 19.7 28.6 20.5 29.3

;"car?o*ate t, 12.7 6.8 12.6 6.9


12/29

Stream Number

Descritio!

P"ase

)$5 )$6 )%$ )%% )%# )%( )%)

%%%'A

oer"ea.

aor to >%$$

%%%'B oer"ea.

aor to

%%

>%$$ out-et

To %%6

%%%5 oer"ea.

to %%%6

=as" @ater

8rom %%%6

To (#%$

CO# 0rom %%#$

To 4rea

P-a!t

Oer"ea. co!.1

8rom %%$

To (##% A&B

VAPOR VAPOR VAPOR VAPOR LI34ID VAPOR LI34ID

-T +-T:-! ;-!-)C < CT:) 400 500 ;= &:-++-C >TCK

Pressure Kg/cm2 a 2.1 1.3 1.4 1.4 1.6 1.3 1.3

Temperature oC 107 99 98 80 45 40 77

Dry gas rate Kg/hr 53885 27860 81745 81745 864 80881 0

team rate Kg/hr 25915 25362 32112 18397 0 2081 0

!"#u"$ rate Kg/hr 0 0 0 0 872851 0 19165

Tota% rate Kg/hr 79800 53222 113857 100142 873715 82962 19165

Dry &as '%o( rate )m3/hr 27401 14170 41571 41571 0 41134 0

team to $ry gas mo%e rat"o 1.17 2.21 0.95 0.55 *.a 0.06 *.a

Dry gas compos"t"o*

)2 +o%e , 0.08 0.09 0.09 0.09 *.a 0.09 *.a

- +o%e , 0.00 0.00 0.00 0.00 *.a 0.00 *.a

2 +o%e , 0.00 0.00 0.00 0.00 *.a 0.00 *.aC4 +o%e , 0.00 0.00 0.00 0.00 *.a 0.00 *.a

C2 +o%e , 99.40 99.38 99.39 99.39 *.a 99.39 *.a

C +o%e , 0.00 0.00 0.00 0.00 *.a 0.00 *.a

2 +o%e , 0.51 0.53 0.52 0.52 *.a 0.53 *.a

)3 +o%e , 0.00 0.00 0.00 0.00 *.a 0.00 *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 1.0 0.6 1.6 1.6 0.0 1.6 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 1223.4 632.5 1855.9 1855.9 19.6 1836.3 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 6.3 3.4 9.7 9.7 0.0 9.7 0.0

20 Kgmo%/hr 1438.5 1407.8 1782.5 1021.2 48451.4 115.5 1063.8

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

Tota% o%ut"o*

Car?o*ate t,

;"car?o*ate t,


13/29


Stream Number

Descritio!

P"ase

)% )%+ )%' )%5 )%6 )#$ )#

E9cess

oer"ea.

Co!.e!sate to

Drai! "ea.er

Co!.e!sate

8rom (##% A&B

To (#$+ A&B

Process

Co!.e!sate

8rom %%%

Co!.e!sate

8rom %%% to

(+$($$%

Co!.e!sate

8rom %%% to

(#%$$%&$$#

Oer"ea. co!.1

8rom %%%5 to

(#%+$$%&$$#

Semi -ea!

So-utio! 0rom

(#$' A&B to %%%+

LI34ID LI34ID LI34ID LI34ID LI34ID LI34ID LI34ID

-T +-T:-! ;-!-)C < CT:) 400 500 ;= &:-++-C >TCK

Pressure Kg/cm2 a 1.3 2.0 26.3 26.3 26.3 1.5 30.1

Temperature oC 77 77 126 126 126 80 102.5

Dry gas rate Kg/hr 0 0 0 0 0 0 0

team rate Kg/hr 0 0 0 0 0 0 0

!"#u"$ rate Kg/hr 4353 14812 56440 39000 17440 13715 1631520

Tota% rate Kg/hr 4353 14812 56440 39000 17440 13715 1631520

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0

team to $ry gas mo%e rat"o *.a *.a *.a *.a *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , *.a *.a *.a *.a *.a *.a *.a- +o%e , *.a *.a *.a *.a *.a *.a *.a

2 +o%e , *.a *.a *.a *.a *.a *.a *.a

C4 +o%e , *.a *.a *.a *.a *.a *.a *.a

C2 +o%e , *.a *.a *.a *.a *.a *.a *.a

C +o%e , *.a *.a *.a *.a *.a *.a *.a

2 +o%e , *.a *.a *.a *.a *.a *.a *.a

)3 +o%e , *.a *.a *.a *.a *.a *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

20 Kgmo%/hr 241.6 822.2 3132.9 2164.9 968.1 761.3 *.a

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 *.a

Tota% o%ut"o*

Car?o*ate t, 20.5

;"car?o*ate t, 12.6


14/29


Stream Number

Descritio!

P"ase

)## )($ )(% )(#&(#$ )((&(# )() )(&+#5

Lea! so-utio!

8rom %#%

To (#$+ A&B

LP B8=

8rom B1L

To %%

LP B8=

8rom %%

To %%(

LP B8=

8rom %%(

To %'$(

LP steam

8rom %$

LP steam

To %%%' A

LP steam to

) ata "ea.er

LI34ID LI34ID LI34ID LI34ID VAPOR VAPOR VAPOR

-T +-T:-! ;-!-)C < CT:) 400 500 ;= &:-++-C >TCK

Pressure Kg/cm2 a 1.8 4.8 4.3 3.7 5.0 5.0 5.0

Temperature oC 70 44 81.5 94 151 151 151

Dry gas rate Kg/hr 0 0 0 0 0 0 0

team rate Kg/hr 0 0 0 0 12810 8700 4110

!"#u"$ rate Kg/hr 339773 293945 293945 293945 0 0 0

Tota% rate Kg/hr 339773 293945 293945 293945 12810 8700 4110

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0

team to $ry gas mo%e rat"o *.a *.a *.a *.a *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , *.a *.a *.a *.a *.a *.a *.a

- +o%e , *.a *.a *.a *.a *.a *.a *.a2 +o%e , *.a *.a *.a *.a *.a *.a *.a

C4 +o%e , *.a *.a *.a *.a *.a *.a *.a

C2 +o%e , *.a *.a *.a *.a *.a *.a *.a

C +o%e , *.a *.a *.a *.a *.a *.a *.a

2 +o%e , *.a *.a *.a *.a *.a *.a *.a

)3 +o%e , *.a *.a *.a *.a *.a *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr *.a 16316.7 16316.7 16316.7 711.1 482.9 228.1

)3 Kgmo%/hr *.a 0.0 0.0 0.0 0.0 0.0 0.0

Tota% o%ut"o*

Car?o*ate t, 29.3

;"car?o*ate t, 6.9


15/29


Stream Number

Descritio!

P"ase

)5% )5( )5)

Coo-i!/

=ater to

%%6

Coo-i!/

=ater to

%#$

Coo-i!/

=ater to

%#%

LI34ID LI34ID LI34ID

-T +-T:-! ;-!-)C < CT:) 400 500 ;= &:-++-C >TCK

Pressure Kg/cm2 a 5.0 5.0 5.0

Temperature oC 33 32 32

Dry gas rate Kg/hr 0 0 0

team rate Kg/hr 0 0 0

!"#u"$ rate Kg/hr 677345 840840 762300

Tota% rate Kg/hr 677345 840840 762300

Dry &as '%o( rate )m3/hr 0 0 0

team to $ry gas mo%e rat"o *.a *.a *.a

Dry gas compos"t"o*

)2 +o%e , *.a *.a *.a

- +o%e , *.a *.a *.a2 +o%e , *.a *.a *.a

C4 +o%e , *.a *.a *.a

C2 +o%e , *.a *.a *.a

C +o%e , *.a *.a *.a

2 +o%e , *.a *.a *.a

)3 +o%e , *.a *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0

20 Kgmo%/hr 37598.9 46674.4 42314.7

)3 Kgmo%/hr 0.0 0.0 0.0

Tota% o%ut"o*

Car?o*ate t,

;"car?o*ate t,


16/29


Stream Number

Descritio!

P"ase

$% $# $( $) $ 5%

Lea! so-utio!

To (+$5

Lea! so-utio!

8rom (+$5

To (+$

Lea! so-utio!

to %#

Air to %#$+ Lea! so-utio!

To (#$+ A&B

Coo-i!/

=ater

To %#

LI34ID LI34ID LI34ID VAPOR LI34ID LI34ID

-T +-T:-! ;-!-)C < CT:) 400 500 ;= &:-++-C >TCK

Pressure Kg/cm2 a 5.7 5.7 1.9 8.0 1.8 5.0

Temperature oC 70 70 70 40 70 32

Dry gas rate Kg/hr 0 0 0 39 0 0

team rate Kg/hr 0 0 0 0 0 0

!"#u"$ rate Kg/hr 76200 40640 19200 0 339773 52550

Tota% rate Kg/hr 76200 40640 19200 39 339773 52550

Dry &as '%o( rate )m3/hr 0 0 0 30 0 0

team to $ry gas mo%e rat"o *.a *.a *.a 0.00 *.a *.a

Dry gas compos"t"o*

)2 +o%e , *.a *.a *.a 78.09 *.a *.a

- +o%e , *.a *.a *.a 0.93 *.a *.a2 +o%e , *.a *.a *.a 20.95 *.a *.a

C4 +o%e , *.a *.a *.a 0.00 *.a *.a

C2 +o%e , *.a *.a *.a 0.03 *.a *.a

C +o%e , *.a *.a *.a 0.00 *.a *.a

2 +o%e , *.a *.a *.a 0.00 *.a *.a

)3 +o%e , *.a *.a *.a 0.00 *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr *.a *.a *.a 1.0 *.a 0.0

- Kgmo%/hr *.a *.a *.a 0.0 *.a 0.0

2 Kgmo%/hr *.a *.a *.a 0.3 *.a 0.0

C4 Kgmo%/hr *.a *.a *.a 0.0 *.a 0.0

C2 Kgmo%/hr *.a *.a *.a 0.0 *.a 0.0

C Kgmo%/hr *.a *.a *.a 0.0 *.a 0.0

2 Kgmo%/hr *.a *.a *.a 0.0 *.a 0.0

20 Kgmo%/hr *.a *.a *.a 0.0 *.a 2917.0

)3 Kgmo%/hr *.a *.a *.a 0.0 *.a 0.0

Tota% o%ut"o*

Car?o*ate t, 27 27 27 29.3

;"car?o*ate t, 6.4 6.4 6.4 6.9


17/29



18/29

Stream Number

Descritio!

P"ase

+$%#$ +$# +$( +$) +$ +$ +$'

Steam 0rom

%(+A to %$+

;/&cm#a

"ea.er

Steam 0rom

%'$# to %$+

;/&cm#a

"ea.er

Steam 0rom S7C

mai! turbi!e to

co!.1 Turbi!e

Steam 0rom S7C

mai! turbi!e to

) ;/&cm#a

"ea.er

Steam 0rom )

;/&cm#a "ea.er

to %%$5%()%('

Steam 0rom )

;/&cm#a "ea.er

to %%$5%()%('

Process Air 0rom

%)(( to %%$

LI34ID VAPOR VAPOR VAPOR VAPOR VAPOR VAPOR

Pressure Kg/cm2 a 106.0 106.0 45.0 45.0 45.0 45.0 45.0

Temperature oC 485 482 365 365 365 365 365

!"#u"$ rate Kg/hr 0 0 0 0 0 0 0

>apor rate Kg/hr 158600 134400 43000 240000 112867 21510 2360

Tota% rate Kg/hr 158600 134400 43000 240000 112867 21510 2360

Dry &as '%o( rate Kg/hr 0 0 0 0 0 0 0

team to $ry gas mo%e rat"o )m3/hr

Dry gas compos"t"o*

)2 +o%e ,

+o%e ,

2 +o%e , C4 +o%e ,

C2 +o%e ,

C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 8803.8 7460.4 2386.9 13322.2 6265.2 1194.0 131.0

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 18.02 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 126.18 106.67 32.08 179.04 84.20 16.05 1.76



19/29

Stream Number

Descritio!

P"ase

+$5 +$6 +%$ +%% +%# +%( +%)

Steam to ('$'

$$% Comb1 Air

0a! turbi!e

Steam to

Semi-ea! um

turbi!e ('$6

$$%&$$#

Let .o@! to

%# ;/&cm#a

"ea.er

Steam to B8=

um turbi!e

('$)$$%&$$#

Steam to -ea!

um turbi!e

('$$$%&$$#

Steam to Au91

Boi-er 0a! .ries

Steam to O7T

%$%A C= um

turbi!e


Pressure Kg/cm2 a 45.0 45.0 45.0 45.0 45.0 45.0 45.0

Temperature oC 365 365 365 365 365 365 365

!"#u"$ rate Kg/hr 0 0 0 0 0 0 0

>apour rate Kg/hr 1360 33200 0 34250 12200 14700 10500

Tota% rate Kg/hr 1360 33200 0 34250 12200 14700 10500

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0

team to $ry gas mo%e rat"o

Dry gas compos"t"o*

)2 +o%e ,

- +o%e ,

2 +o%e , C4 +o%e ,

C2 +o%e ,

C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 75.5 1842.9 0.0 1901.2 677.2 816.0 582.8

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 18.02 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 1.01 24.77 0.00 25.55 9.10 10.97 7.83



20/29

Stream Number

Descritio!

P"ase

+% +%+ +%' +%5 +%6 +#$ +#%

Steam to O7T

%$%B C=

um turbi!e

Steam to rocess

air comressor

turbi!e ('$#

Steam 0or

misce--a!eous

uses

Steam to 0ue- oi-

um turbi!e

('%%

Steam to rocess

!a"t"a um

turbi!e ('%#

Steam to 0ue-

!a"t"a um

turbi!e ('%(

Imort steam to

) ;/&cm# a

"ea.er


Pressure Kg/cm2 a 45.0 12.0 23.0 12.0 12.0 12.0 12.0

Temperature oC 365 278 278 278 278 278 365

!"#u"$ rate Kg/hr 0 0 0 0 0 0 0

>apour rate Kg/hr 21500 56300 14100 1750 3650 1100 17400

Tota% rate Kg/hr 21500 56300 14100 1750 3650 1100 17400

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0


Dry gas compos"t"o*

)2 +o%e ,

- +o%e ,

2 +o%e ,

C4 +o%e , C2 +o%e ,

C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 75.5 1842.9 0.0 1901.2 677.2 816.0 582.8

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 18.02 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 1.01 24.77 0.00 25.55 9.10 10.97 7.83


Stream Number +## +#( +#) +# +#+ +#'&(#' +#5&)(


21/29

Descritio!

P"ase

Desuer"eate.

-et .o@! steam to

%# ;/&cm#a

"ea.er

Let .o@! 0rom

%# ;/ &Cm#a to

#1% ;/ &cm#a

Let.o@! 0rom

%#;/&cm#a

"ea.er

to (+$$$%

Atomiapor rate Kg/hr 0 0 8320 9100 0 10763 4110

Tota% rate Kg/hr 0 0 8320 9100 0 10763 4110

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0


Dry gas compos"t"o*

)2 +o%e ,

- +o%e ,

2 +o%e ,

C4 +o%e , C2 +o%e ,

C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 0.0 0.0 461.8 505.1 0.0 597.4 228.1

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 18.02 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 0.00 0.00 5.96 6.05 0.00 7.60 2.70


Stream Number +#6 +($ +(% +(# +(( +() +(


22/29

Descritio!

P"ase

E9ort steam

0rom ) ata

"ea.er

Ve!t 0rom

%# ;/&Cm# a

"ea.er

Steam to ('$+

$$# 8-ue 7as 0a!

turbi!e

Steam to ('$'$$#

Comb1 Air 0a!

turbi!e

Lea steam 0rom

BP turbi!es to #1%

;/&cm# a "ea.er

Ve!t 0rom #1%

;/&cm# a "ea.er

B,ass o0 ('$%

turbi!e


Pressure Kg/cm2 a 4.0 12.0 45.0 45.0 2.1 2.1 106.0Temperature oC 193 278 365 365 243 243 482

!"#u"$ rate Kg/hr 0 0 0 0 0 0 0

>apor rate Kg/hr 25610 6130 2360 1360 3000 1845 10000

Tota% rate Kg/hr 25610 6130 2360 1360 3000 1845 10000

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0


Dry gas compos"t"o*

)2 +o%e ,

- +o%e ,

2 +o%e ,

C4 +o%e ,

C2 +o%e , C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 1421.8 340.3 131.0 75.50 166.5 102.4 555.1

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 18.02 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 17.37 4.39 1.76 1.01 2.12 1.30 7.94


Stream Number +(+#) +)$ +)% +)# +)( +))&(#) +)


23/29

Descritio!

P"ase

8-as" steam

0rom %%($

=ater to

.esuer"eater

(+$$$(

=ater to

.esuer"eater

(+$$$#

=ater to

.esuer"eater

(+$$$%

Steam co!.e!sate

to o-is"i!/ u!it

HP B8= 0rom

%( Ne@ B8=

re"eaterF

[email protected]@! 0rom

%'$#

VAPOR LI34ID LI34ID LI34ID LI34ID LI34ID LI34ID

Pressure Kg/cm2 a 2.5 55.0 55.0 55.0 5.0 126.0 106.0Temperature oC 127 109 109 109 57 218 314

!"#u"$ rate Kg/hr 0 767 0 780 152850 139400 5000

>apor rate Kg/hr 3108 0 0 0 0 0 0

Tota% rate Kg/hr 3108 767 0 780 152850 139400 5000

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0 0


Dry gas compos"t"o*

)2 +o%e ,

- +o%e ,

2 +o%e ,

C4 +o%e ,

C2 +o%e , C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 172.5 42.6 0.0 43.3 8484.6 7737.6 277.5

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 18.02 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 2.02 0.09 0.00 0.09 8.72 31.14 1.70


Stream Number +5% +5# +5( +5) +5 +5+


24/29

Descritio!

P"ase

C= to

Co!.e!ser o0

('$%

C= to

Co!.e!ser o0

('$#

C= to

Co!.e!ser o0

('$(

C= to

Co!.e!ser o0

('$+&('$'$$%

C= to

Co!.e!ser o0

('$+&('$'$$#

C= to

Co!.e!ser o0

O7T%$%A

LI34ID LI34ID LI34ID LI34ID LI34ID LI34ID

Pressure Kg/cm2 a 5.0 5.0 5.0 5.0 5.0 5.0Temperature oC 32 32 32 32 32 32

!"#u"$ rate Kg/hr 3700000 3219000 1230000 212700 212700 600000

>apor rate Kg/hr 0 0 0 0 0 0

Tota% rate Kg/hr 3700000 3219000 123000 212700 212700 600000

Dry &as '%o( rate )m3/hr 0 0 0 0 0 0


Dry gas compos"t"o*

)2 +o%e ,

- +o%e ,

2 +o%e ,

C4 +o%e ,

C2 +o%e , C +o%e ,

2 +o%e ,

)3 +o%e ,

)aphtha +o%e ,

u%phur Ppm (t

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

- Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

20 Kgmo%/hr 205384.4 178684.4 68276.4 11806.8 11806.8 33305.6

)3 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0

)aphtha Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0



+ 18.02 18.02 18.02 18.02 18.02 18.02

*tha%py &Ca%/hr 118.40 103.01 39.36 6.81 6.81 19.20


Stream Number '$%&()5 '$#&5$# '$($# '$) '$ '$+ '$'


25/29

Descritio!

P"ase

Maeu S,!1

7as 0rom %%)(

Recoere. H#

0rom P7IHR4 to

(%$#

Rec,c-e H# to

!a"t"a

aori


26/29

Descritio!

P"ase

Recirc1 7as

0rom %%## to

%#

8ee. to

circu-ator (%$(

Circu-ator

.isc"ar/e to %%#%

S,!1 7as 0rom

%%#% to %#(

S,!1 7as 0rom

%#( to %#)

S,!1 7as 0rom

%#) to %#

S,!1 7as 0rom

%# to %#+

VAPOR VAPOR VAPOR VAPOR VAPOR MI>ED MI>ED

-T +-T:-! ;-!-)C < CT:) 700 800 - ;= -++):- C--! .-

Pressure Kg/cm2 a 199.2 197.8 208.7 206.0 204.7 203.4 202.2

Temperature oC 2.5 30 40 257.3 123.4 35.5 20.3

Dry gas rate Kg/hr 259815 259815 249950 249952 249952 219655 201478


!"#u"$ rate Kg/hr 0 0 0 0 0 30297 44346

Tota% rate Kg/hr 259815 259815 249950 249952 249952 249952 245824

Dry &as '%o( rate )m3/hr 546271 546271 525530 456441 456441 416372 389855

team to $ry gas mo%e rat"o 0.00 0.00 0.00 0.00 0.00 0.00 0.00

Compos"t"o* Dry ;as"s

)2 +o%e , 21.01 21.01 21.01 16.62 16.62 16.62 16.58

- +o%e , 3.78 3.78 3.78 4.35 4.35 4.35 4.342 +o%e , 0.00 0.00 0.00 0.00 0.00 0.00 0.00

C4 +o%e , 8.22 8.22 8.22 9.46 9.46 9.46 9.44

C2 +o%e , 0.00 0.00 0.00 0.00 0.00 0.00 0.00

C +o%e , 0.00 0.00 0.00 0.00 0.00 0.00 0.00

2 +o%e , 63.03 63.03 63.03 49.86 49.86 49.86 49.73

)3 +o%e , 3.96 3.96 3.96 19.70 19.70 19.70 19.91

u%phur Ppm (t 0 0 0 0 0 0 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 5120.4 5120.4 4926.0 3384.8 3384.8 3384.8 3317.0

- Kgmo%/hr 921.8 921.8 886.8 886.8 886.8 886.8 869.1

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 2002.9 2002.9 1926.8 1926.8 1926.8 1926.8 1888.4

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 15361.2 15361.2 14777.9 10154.3 10154.3 10154.3 9950.9

20 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

)3 Kgmo%/hr 966.1 966.1 929.4 4011.8 4011.8 4011.8 3982.7

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 10.66 10.66 10.66 12.27 12.27 12.27 12.29

*tha%py &Ca%/hr 6.03 0.06 1.74 35.42 12.60 8.89 14.82


Stream Number '%&5$% '%+&5$( '%' '%5 '%6 '(%&(#% '(#&(##


27/29

Descritio!

P"ase

Pur/e /as to

P7HR4

LiGui. NH( 0rom

P7HR4 to %%#(

LiGui. NH( 0rom

%%## to %%#(

LiGui. NH(

ro.uct 0rom

%%#(

Vaor 0rom %%#(

to NH( absorber

Deaerate. B8=

0rom HP B8=

um to %#(

B8= 0rom %#(

to %% 2 %(6

VAPOR LI34ID LI34ID LI34ID LI34ID LI34ID LI34ID

-T +-T:-! ;-!-)C < CT:) 700 800 - ;= -++):- C--! .-

Pressure Kg/cm2 a 202.2 21.1 199.2 21.1 21.1 127.0 126.5

Temperature oC 20.3 3.3 2.5 3.3 3.3 109 181

Dry gas rate Kg/hr 4128 0 0 0 616 0 0


!"#u"$ rate Kg/hr 0 491 52516 52390 0 300400 300400

Tota% rate Kg/hr 4128 491 52516 52390 616 300400 300400

Dry &as '%o( rate )m3/hr 7987 0 0 0 1129 0 0

team to $ry gas mo%e rat"o 0.00 *.a *.a *.a 0.00 *.a *.a

Compos"t"o* Dry ?as"s

)2 +o%e , 19.01 0.03 0.22 0.02 12.13 *.a *.a

- +o%e , 4.98 0.00 0.09 0.01 4.62 *.a *.a2 +o%e , 0.00 0.00 0.00 0.00 0.00 *.a *.a

C4 +o%e , 10.78 0.03 0.34 0.01 20.23 *.a *.a

C2 +o%e , 0.00 0.00 0.00 0.00 0.00 *.a *.a

C +o%e , 0.00 0.00 0.00 0.00 0.00 *.a *.a

2 +o%e , 57.08 0.03 0.78 0.02 46.53 *.a *.a

)3 +o%e , 8.15 99.90 98.58 99.93 16.49 *.a *.a

u%phur Ppm (t 0 0 0 0.00 0 *.a *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 67.8 0.0 6.7 0.6 6.1 0.0 0.0

- Kgmo%/hr 17.7 0.0 2.6 0.3 2.3 0.0 0.0

2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 38.4 0.0 10.6 0.5 10.2 0.0 0.0

C2 Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

C Kgmo%/hr 0.0 0.0 0.0 0.0 0.0 0.0 0.0

2 Kgmo%/hr 203.4 0.0 24.0 0.6 23.4 0.0 0.0

20 Kgmo%/hr 0.0 0.0 2.8 2.8 0.0 16674.1 16674.1

)3 Kgmo%/hr 29.1 28.8 3050.5 3071.0 8.3 0.0 0.0

u%phur Kgmo%/hr 0 0 0 0 0 0 0


+ 11.58 17.03 16.96 17.03 12.24 18.02 18.02

*tha%py &Ca%/hr 0.05 0.02 16.16 16.22 0.01 32.66 55.49


Stream Number '5%


28/29

Descritio!

P"ase

Coo-i!/ =ater

to %#)

LI34ID

-T +-T:-! ;-!-)C < CT:) 700 800 - ;= -++):- C--! .-

Pressure Kg/cm2 a 5.0

Temperature oC 32

Dry gas rate Kg/hr 0

team rate Kg/hr 0

!"#u"$ rate Kg/hr 1791200

Tota% rate Kg/hr 1791200

Dry &as '%o( rate )m3/hr 0

team to $ry gas mo%e rat"o *.a


)2 +o%e , *.a

- +o%e , *.a

2 +o%e , *.a

C4 +o%e , *.a

C2 +o%e , *.a

C +o%e , *.a

2 +o%e , *.a

)3 +o%e , *.a

u%phur Ppm (t *.a

Compo*e*t '%o( rate

)2 Kgmo%/hr 0.0

- Kgmo%/hr 0.0

2 Kgmo%/hr 0.0

C4 Kgmo%/hr 0.0

C2 Kgmo%/hr 0.0

C Kgmo%/hr 0.02 Kgmo%/hr 99422.7

20 Kgmo%/hr 0.0

)3 Kgmo%/hr 0.0

u%phur Kgmo%/hr 0

Tota% '%o( rate Kgmo%/hr 99422.7

+ 18.02

*tha%py &Ca%/hr 57.3


Stream Number 5$%&'% 5$#&'$# 5$(&'%+ 5$)%$


29/29

Descritio!

P"ase

Pur/e /as

0rom S,!1

Loo

Recoere. H#

0rom P7HR4 to

(%$#

LiGui. NH( 0rom

P7HR4 to %%#(

Tai- /as to

Primar, re0ormer

0ue- s,stem

VAPOR VAPOR LI34ID VAPOR

-T +-T:-! ;-!-)C < CT:) 700 800 - ;= -++):- C--! .-

Pressure Kg/cm2 a 202.2 48.5 21.1 2.3

Temperature oC 20.3 40 3.3 40

Dry gas rate Kg/hr 4128 697 0 2940

team rate Kg/hr 0 0 0 0

!"#u"$ rate Kg/hr 0 0 491 0

Tota% rate Kg/hr 4128 697 491 2940

Dry &as '%o( rate )m3/hr 7987 4404 0 2938

team to $ry gas mo%e rat"o 0.0 0.0 0.0 0.0


)2 +o%e , 19.01 4.82 0.03 44.45- +o%e , 4.98 0.59 0.00 12.66

2 +o%e , 0.00 0.00 0.00 0.00

C4 +o%e , 10.78 0.39 0.03 28.71

C2 +o%e , 0.00 0.00 0.00 0.00

C +o%e , 0.00 0.00 0.00 0.00

2 +o%e , 57.08 94.20 0.03 13.96

)3 +o%e , 8.15 0.00 99.90 0.21

u%phur Ppm (t 0 0 0 0

Compo*e*t '%o( rate

)2 Kgmo%/hr 67.8 9.5 0.0 58.3

- Kgmo%/hr 17.7 1.2 0.0 16.6

2 Kgmo%/hr 0.0 0.0 0.0 0.0

C4 Kgmo%/hr 38.4 0.8 0.0 37.6

C2 Kgmo%/hr 0.0 0.0 0.0 0.0C Kgmo%/hr 0.0 0.0 0.0 0.0

2 Kgmo%/hr 203.4 185.1 0.0 18.3

20 Kgmo%/hr 0.0 0.0 0.0 0.0

)3 Kgmo%/hr 29.1 0.0 28.8 0.3

u%phur Kgmo%/hr 0 0 0 0

Tota% '%o( rate Kgmo%/hr 356.4 196.5 28.8 131.1

+ 11.58 3.55 17.03 22.43

*tha%py &Ca%/hr 0.05 0.02 0.02 0.01

62449961-ammonia-heat-mat-balance.doc

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