Mod_060_Planta Recuperacion de Licuables Calculo_GLP

8/16/2019 Mod_060_Planta Recuperacion de Licuables Calculo_GLP

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Presion (Psig) 1000.0

Temp. (°F) 78.0

Fecha 15/JUN/2004

Componentes San Alberto

N2 0.45000

Factor bCO2 1.52000 PESOC1 89.96000

!O"E#$"%&

C2 5.0'000 Btu/Pc r*rmo

C3 1.84000 C6 100.00 4756.0 2.75!0 0.072 !6.17500

"C4 0.48000 C7 0.00 0.0 0.00000 0.0000 0.00000

NC4 0.40000 C! 0.00 0.0 0.00000 0.0000 0.00000

"C5 0.16000 C# 0.00 0.0 0.00000 0.0000 0.00000

NC5 0.0+000 C6+ 100.00 4,756.0 2.97580 0.0792 86.17500

C6 0.09000

C7 0.00000 0.09000

C! 0.00000

C# 0.00000

$ota% 100.00000 %C6 1.000000 100.00

C7 0.000000 0.00

C! 0.000000 0.00

C# 0.000000 0.00

$ota% 1.000000 100.00

NOTA.- PROPI!A!S ! AC"R!O CON #A NOR$A %PA 2145 &RSI'N 200( ) AST$ ! (588 - 98

PO,E&

#%"O&-F-#OS$PE&-O&SE#O

&%/E,%,ESPE#-F-#%


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3/32

(,262.(

4,000.9

4,008.9

4,756.0

Componentes San Alberto -

-

992.4

1,7(8.9

2,472.(

(,195.(

(,205.5

(,9(1.(

(,9(9.1

4,67(.2

Componentes San Alberto

0.9672(

1.51960

0.55(92

1.0(820

1.52260

2.00680

C4H

10

C5H

12

C5H

12

C6H

14+

N2

CO2

CH4

C2H

6

C3H

8

C4H

10

C4H

10

C5H

12

C5H

12

C6H

14+

N2

CO2

CH4

C2H

6

C3H

8

C4H

10


4/32


5/32

72.15000

72.15000

86.17500

C5H

12

C5H

12

C6H

14+


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,ES-,%, &E"%#- &'N("&)& &E"%#-

&E"%T-/% %S*"-$-,O )B(O*U$) %S*"-$-,O

"-$-,O -,E%" *+,U"&O -,E%"

%g3a 1 *bs / -a%n

0.66410 24.'800 5.5'6'0 182.'+

0.00000 0.0000 0.00000 0.00

0.00000 0.0000 0.00000 0.00

0.00000 0.0000 0.00000 0.00

0.66410 24.3800 5.53630 182.37

Pie' gas*an " Pie' gas*Pie' i.


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PRECIOS MONT BELVIEU (US CENTS/GALON) AL 31/05

PROMEIO PROMEIOPROUCTO ENERO !EBRERO 3/22/2004 3/23/2004 3/24/2004

ETANO 66.25 66.25 66.25 66.25 66.25PROPANO "8.72 "1.62 "2.43 101.37 0.00

BUTANO 128.31 118.30 111.82 11".55GASOL.NAT 145.43 133.70 136."3 154.12

C#US/GALON #US/PC #US/BBL #US/T$

ETANO 66.25 4.96 2+.82 4"1.02GLP 104.18 +.+9 4'.+5 518."3GASOLINA 142.55 10.66 5".87 9.86+66 590.+6582'51

181.8241406+++

G&' *&+/COMPOSICION ENSIA(L,.) L-,$'

GLP (%) *+&& 60!14.6"6'&ETANO 0.'564' 280.54

PROPANO 65.'0 0.50+'8 2+2.'2BUTANO '4.+0 0.5+'52 2''.54

GLP 100.00 0.53033 258.86

C O S T O S (CAPEOPE) GLP#US/MPC () #US/TON #US/+$

TOTAL 0.18 122.'5 0.122'OPE&%#- 0.055 '+.'8 0.0'+4-/E&S-O 0.125 84.96 0.0850(7) F3ene E%

#O/E-O :$S*;;" :$S*TOOPE&%#- 0.9++6 11.5"45

16 ;s*10


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/06

PROMEIO PROMEIO3/25/2004 MAR9O ENE!EBMAR

66.25 66.25 66.250.00 0.00 96.04

119.50142.55

58.04


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PLANTA E ETRACCION E LICUABLES EL GAS NATURAL ARGENTINACOMPOSICION PROMEIO

:UN./04 & OCT./04

COMPONENTES

A N T E S A L A S A L I A E P L A N

E PLANTA GAS RESIUAL

!oar !oar !oar !oar

0.45000 0.45 0.00 0.00

1.52000 1.52 0.00 0.00

8"."6000 89.96 0.00 0.00

5.03000 5.0' 0.00 0.00

1.84000 0.18 0.00 1.66

0.48000 0.00 0.00 0.48

0.40000 0.00 0.00 0.40

0.16000 0.00 0.00 0.00

0.07000 0.00 0.00 0.00

0.0"00 0.00 0.00 0.00 ∑ = 100.0000 9+.14 0.00 2.54

Po=er #aor>?ico S3perior ;ase Seca &ea (;T$* pc)

a 60 @F A 14B696 psia 10"1 1034 0 283"/O"$!E

27.70 26.91 0.00 0.+0 MM BTU/-& 1B06+B498.5 982B98'.+ 0.00 +0B424.2 #US/MM BTU 5.0000 0.0000 8.0183

#US/-& 4B914B918.69 0.00 564B680.58 #US/&;$ 1B+9'B945B'2'.6+ 0.00 206B6+'B092.+0

Τ ΝΟ

on*=ia 1B+68.51 1+68.51 0.00 ;;"*=ia '1B2'8.52 '12'8.52 0.00

GLPon*=ia 1B546.+6 94.8+ 1B451.89 ;;"*=ia 18B'50.58 11++.21 1+B1+'.'+

GASOLINAS;*=ia 2809.46

P R E C I O S !;/*T- Sprea= ena !;/*T- Precio =e /ena #oso Procesamieno Prec

"P :*TO 518."3 mies mJKimos 3n 85% =e rec3peracin =e Eano A "5% =e Propano L asimism

=e "P (#'B i#4 A n#4) A gasoinas (i#5B n#5 A #6I

)

&E,-!-ETOS


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PLANTA E ETRACCION E ETANO > LICUABLES EL GAS EN ARGENTINA

GAS RESIUAL A GASOUCTO

26."1

PLANTA E ETRACCION E ETANOGAS NATURAL ETANO

27.70 0.00???O:O@@@

ATOS EINGRESO

* RESUMEN GLP 0.70

GASOLINAS 0.0"&E#$PE&%#-O ET%O 0 0.7"

&E#$PE&%#-O P&OP%O "0&E#$PE&%#-O ;$T%O 100

&E#$PE&%#-O %SO"-%S(#5I) 1003mero =e corriene 1 2 ' #orriene ENTRAA GAS RESIUAL RECUPERACION

#ompoC Peso nenes !oec3ar !oar rmo*hr !oar !oar rmo*hr !oar !oar

r*rmo Ki Ki normaiMa=o normaiMa=o

28.01' 0.45 48'.'28 0.45 0.46 48'.'28 0.00 0.00

44.010 1.52 1B6'2.5+' 1.52 1.56 1B6'2.5+' 0.00 0.00

16.04' 89.96 96B622.549 89.96 92.60 96B622.549 0.00 0.00

'0.0+0 5.0( 5B402.528 5.0' 5.18 5B402.528 0.00 0.00

44.09+ 1.84 1B9+6.2+' 0.18 0.19 19+.62+ 0.00 0.00

58.12' 0.48 515.549 0.00 0.00 0.000 0.00 0.00

58.12' 0.40 429.624 0.00 0.00 0.000 0.00 0.00

+2.150 0.16 1+1.850 0.00 0.00 0.000 0.00 0.00

+2.150 0.07 +5.184 0.00 0.00 0.000 0.00 0.00

86.1+5 0.09 96.666 0.00 0.00 0.000 0.00 0.00 ∑ = 100.00 107406.124 9+.14 100.00 104338.605 0.00 0.00

2+B+00B000 26B908B888

Τ ΝΟ

on*=ia 1B+68.51 1B+68.51;*=ia '1B2'8.5 '1B2'8.5

GLP

on*=ia 1B546.+6 94.8+

;*=ia 18B'50.6 1B1++.2

GASOLINAS on*=ia 284.+1

;*=ia 2B809.5

C$$*' B&'*Presion 14.696 psia

Tempera3ra 60 @FE&&

F3No 27700000Peso moec3ar 18.'062 r*rmo

C$'&*'

'5.'1466+10.+'164 (psia7pc)*(rmo7@&)

5.614584 pc*;

!! m'*=

!! m'*= !! m'*=

!! m'*=

!! m'*=

2

#O2

#1

#2

#'

iC#4

nC#4

iC#5

nC#5

#6I

=3 /&

m'*=ia

pc*m'

#ompren=e separacin =e EanoB apicJn=ose como >mies mJKimos 3n 85% =e rec3peracin =e Eano A "5% =e Propano L asim (# # # ) ( # # # )

1

2

44

'


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COMPARACION E PRECIOS E GAS NATURAL E EPORTACION BRASIL < ARGENTINA 200

!ECA 14


16/32

PO!R CA#ORI*ICO, !NSI!A! ) CO$PRSII#I!A!

! AC"R!O CON #A %PA 2145 &RSI'N 200( ) AST$ ! (588 - 9

ATOS EINGRESO

&%/E,%, ,ES-,%, &E"%#- PO,E& #%" PO,E& #%"

#O!POETES !oar !oar ESPE#QF-#% &E"%T-/% %S*"-$-,O S$PE&-O& S$PE&-O&

=e a corriene ormaiMa=o ,E" %S "-$-,O -,E%" SE#O i=ea SE#O rea

Ki %ire 1 %g3a 1

-T&OEO 0.45 0.45 0.96+'0 0.8068+ 91.129 0.0 0.0 ,-OR-,O ,E #%&;OO 1.52 1.52 1.519+0 0.8220' 59.095 0.0 0.0

!ET%O 89.96 89.96 0.55'9+ 0.'000' 59.1'+ 1010.0 1012.0

ET%O 5.0' 5.0' 1.0'8'0 0.'564' '+.50' 1+69.+ 1+84.6

P&OP%O 1.84 1.84 1.522+0 0.50+'8 '6.404 2516.2 2562.1

-.;$T%O 0.48 0.48 2.00+10 0.56295 '0.644 '252.0 ''49.0

.;$T%O 0.40 0.40 2.00+10 0.58408 '1.+94 '262.4 ''+2.' -.PET%O 0.16 0.16 2.49140 0.62460 2+.'90 4000.9 420'.0

.PET%O 0.0+ 0.0+ 2.49140 0.6'11' 2+.6+6 4008.+ 42'5.0

C6 0.09 0.09 2.9+580 0.66410 24.'80 4+56.0 52'8.9

S$!%TO&-% 100.00 100.00

PO,E& #%"O&-F-#O S$PE&-O& ( as -=ea ) PCS BASE SECA 1B086,ES-,%, &E"%T-/% ( as -=ea ) G )re 1 0.6'21

POER CALORI!ICO SUPERIOR ( G&' R*&+ ) PCS *&+ BASE SECA 10"1

ENSIA RELATIVA ( G&' R*&+ ) A* F 1 G *&+ 0.6335

POER CALORI!ICO SUPERIOR ( G&' R*&+ ) BASE UMEA 1072

!ACTOR E COMPRESIBILIA 9 0.""74

SIST$A *PS CON!ICIONS AS 60 * / 14,696 PSIA

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BTU / P*(


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PO!R CA#ORI*ICO, !NSI!A! ) CO$PRSII#I!A

! AC"R!O CON #A %PA 2145 &RSI'N 200( ) AST$ ! (58SIST$A *PS CON!ICIONS AS 60 * / 14,696 PSIA

ATOS EINGRESO

&%/E,%, ,ES-,%, &E"%#- PO,E& #%" PO,E& #%" F%

#O!POETES !oar !oar ESPE#QF-#% &E"%T-/% %S*"-$-,O S$PE&-O& S$PE&-O& S$

=e a corriene ormaiMa=o ,E" %S "-$-,O -,E%" SE#O i=ea SE#O rea P

Ki %ire 1 %g3a 1

-T&OEO 0.45 0.46 0.96+'0 0.8068+ 91.129 0.0 0.0 0,-OR-,O ,E #%&;OO 1.52 1.56 1.519+0 0.8220' 59.095 0.0 0.0 0

!ET%O 89.96 92.60 0.55'9+ 0.'000' 59.1'+ 1010.0 1012.0 0

ET%O 5.0' 5.18 1.0'8'0 0.'564' '+.50' 1+69.+ 1+84.6 0

P&OP%O 0.18 0.19 1.522+0 0.50+'8 '6.404 2516.2 2562.1 0

-.;$T%O 0.00 0.00 2.00+10 0.56295 '0.644 '252.0 ''49.0 0

.;$T%O 0.00 0.00 2.00+10 0.58408 '1.+94 '262.4 ''+2.' 0-.PET%O 0.00 0.00 2.49140 0.62460 2+.'90 4000.9 420'.0 0

.PET%O 0.00 0.00 2.49140 0.6'11' 2+.6+6 4008.+ 42'5.0 0

#6I 0.00 0.00 2.9+580 0.66410 24.'80 4+56.0 52'8.9 0

S$!%TO&-% 9+.14 100.00

PO,E& #%"O&-F-#O S$PE&-O& ( as -=ea ) PCS ;%SE SE#% 1B0'2,ES-,%, &E"%T-/% ( as -=ea ) G )re 1 0.59+9

POER CALORI!ICO SUPERIOR ( G&' R*&+ ) PCS *&+ BASE SECA 1034

ENSIA RELATIVA ( G&' R*&+ ) A* F 1 G *&+ 0.5""0 "s*"sC!o

!ACTOR E COMPRESIBILIA 9 0.""78


;T$ * Pie'

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ATOS EINGRESO

&%/E,%, ,ES-,%, &E"%#- PO,E& #%" PO,E& #%"

#O!POETES !oar !oar ESPE#QF-#% &E"%T-/% %S*"-$-,O S$PE&-O& S$PE&-O&

=e a corriene ormaiMa=o ,E" %S "-$-,O -,E%" SE#O i=ea SE#O rea

Ki %ire 1 %g3a 1

-T&OEO 0.00 0.00 0.96+'0 0.8068+ 91.129 0.0 0.0

,-OR-,O ,E #%&;OO 0.00 0.00 1.519+0 0.8220' 59.095 0.0 0.0

!ET%O 0.00 0.00 0.55'9+ 0.'000' 59.1'+ 1010.0 1012.0

ET%O 0.00 0.00 1.0'8'0 0.'564' '+.50' 1+69.+ 1+84.6

P&OP%O 0.00 0.00 1.522+0 0.50+'8 '6.404 2516.2 2562.1

-.;$T%O 0.00 0.00 2.00+10 0.56295 '0.644 '252.0 ''49.0

.;$T%O 0.00 0.00 2.00+10 0.58408 '1.+94 '262.4 ''+2.'

-.PET%O 0.00 0.00 2.49140 0.62460 2+.'90 4000.9 420'.0

.PET%O 0.00 0.00 2.49140 0.6'11' 2+.6+6 4008.+ 42'5.0

#6I 0.00 0.00 2.9+580 0.66410 24.'80 4+56.0 52'8.9

S$!%TO&-% 0.00 0.00

PO,E& #%"O&-F-#O S$PE&-O& ( as -=ea ) PCS ;%SE SE#% 0,ES-,%, &E"%T-/% ( as -=ea ) G )re 1 0.0000


ENSIA RELATIVA ( G&' R*&+ ) A* F 1 G *&+ 0.0000 "s*"sC!o

!ACTOR E COMPRESIBILIA 9 1.0000


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ATOS EINGRESO

&%/E,%, ,ES-,%, &E"%#- PO,E& #%" PO,E& #%" F%



Ki %ire 1 %g3a 1

-T&OEO 0.00 0.00 0.96+'0 0.8068+ 91.129 0.0 0.0 0,-OR-,O ,E #%&;OO 0.00 0.00 1.519+0 0.8220' 59.095 0.0 0.0 0

!ET%O 0.00 0.00 0.55'9+ 0.'000' 59.1'+ 1010.0 1012.0 0

ET%O 0.00 0.00 1.0'8'0 0.'564' '+.50' 1+69.+ 1+84.6 0P&OP%O 1.66 65.'0 1.522+0 0.50+'8 '6.404 2516.2 2562.1 0-.;$T%O 0.48 18.9' 2.00+10 0.56295 '0.644 '252.0 ''49.0 0

.;$T%O 0.40 15.++ 2.00+10 0.58408 '1.+94 '262.4 ''+2.' 0-.PET%O 0.00 0.00 2.49140 0.62460 2+.'90 4000.9 420'.0 0.PET%O 0.00 0.00 2.49140 0.6'11' 2+.6+6 4008.+ 42'5.0 0#6I 0.00 0.00 2.9+580 0.66410 24.'80 4+56.0 52'8.9 0

S$!%TO&-% 2.54 100.00

PO,E& #%"O&-F-#O S$PE&-O& ( as -=ea ) PCS ;%SE SE#% 2B++',ES-,%, &E"%T-/% ( as -=ea ) G )re 1 1.6908

POER CALORI!ICO SUPERIOR ( G&' R*&+ ) PCS *&+ BASE SECA 283"

ENSIA RELATIVA ( G&' R*&+ ) A* F 1 G *&+ 1.7280 "s*"sC!o

!ACTOR E COMPRESIBILIA 9 0."781


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ATOS EINGRESO

&%/E,%, ,ES-,%, &E"%#- PO,E& #%" PO,E& #%" F%



Ki %ire 1 %g3a 1

-T&OEO 0.00 0.00 0.96+'0 0.8068+ 91.129 0.0 0.0 0,-OR-,O ,E #%&;OO 0.00 0.00 1.519+0 0.8220' 59.095 0.0 0.0 0

!ET%O 0.00 0.00 0.55'9+ 0.'000' 59.1'+ 1010.0 1012.0 0

ET%O 0.00 0.00 1.0'8'0 0.'564' '+.50' 1+69.+ 1+84.6 0P&OP%O 0.00 0.00 1.522+0 0.50+'8 '6.404 2516.2 2562.1 0-.;$T%O 0.00 0.00 2.00+10 0.56295 '0.644 '252.0 ''49.0 0

.;$T%O 0.00 0.00 2.00+10 0.58408 '1.+94 '262.4 ''+2.' 0-.PET%O 0.16 50.00 2.49140 0.62460 2+.'90 4000.9 420'.0 0.PET%O 0.0+ 21.88 2.49140 0.6'11' 2+.6+6 4008.+ 42'5.0 0#6I 0.09 28.1' 2.9+580 0.66410 24.'80 4+56.0 52'8.9 0

S$!%TO&-% 0.'2 100.00

PO,E& #%"O&-F-#O S$PE&-O& ( as -=ea ) PCS ;%SE SE#% 4B215,ES-,%, &E"%T-/% ( as -=ea ) G )re 1 2.62+6


ENSIA RELATIVA ( G&' R*&+ ) A* F 1 G *&+ 2.7"52 "s*"sC!o

!ACTOR E COMPRESIBILIA 9 0."3"7


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VOLUMENES ESTIMAOS E INGRESOS BRUTOS EN !RONTERA

AO VOLUMEN TOTAL RESIUAL RESIUAL GLP GLP GASOLNAT

MM=3 MM=3 MPC TON/IA BBL/IA BBL/IA

2006 6.5 6.'1 222B8'5.55 '40 4B0'4 6592007 +.+ +.48 264B15'.+1 40' 4B+81 +812008 +.+ +.48 264B15'.+1 40' 4B+81 +81200" +.+ +.48 264B15'.+1 40' 4B+81 +812010 10.2 9.91 '49B968.'5 5'5 6B'4+ 1B0'52011 12.+ 12.'4 4'5B+82.99 665 +B889 1B2882012 18 1+.49 61+B65'.5' 94' 11B188 1B8252013 2' 22.'4 +88B929.66 1205 14B296 2B'''2014 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092015 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092016 2+.+ 26.91 950B'1+.69 1452 1+B226 2B809

2017 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092018 2+.+ 26.91 950B'1+.69 1452 1+B226 2B809201" 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092020 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092021 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092022 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092023 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092024 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092025 2+.+ 26.91 950B'1+.69 1452 1+B226 2B8092026 2+.+ 26.91 950B'1+.69 1452 1+B226 2B809

INVERSIHN ESTIMAA E PLANTAS

!LU:O GAS ETRAC. GLP ETRAC. GASOL GAS RESI. INVERSIHN APRO OP/MTTO/AM

TON/IA BBL/IA MM=3 MMUS# MMUS#/AO

6.5 '40 659 6.'1 100 1.00 2.2+.+ 40' +81 +.48 100 1.00 9.1+.+ 40' +81 +.48 100 1.00 1'.'+.+ 40' +81 +.48 100 1.00 20.4

10.2 5'5 1B0'5 9.91 120 1.20 24.612.+ 665 1B288 12.'4 144 1.44 '018 94' 1B825 1+.49 1+' 1.+'2' 1205 2B''' 22.'4 20+ 2.0+

2+.+ 1452 2B809 26.91 249 2.492+.+ 1452 2B809 26.91 299 2.992+.+ 1452 2B809 26.91 '58 '.582+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.94


22/32

2+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.94

2+.+ 1452 2B809 26.91 '94 '.942+.+ 1452 2B809 26.91 '94 '.94


23/32

INGRESO RESIUAL ING. GLP ING. GASOLINA ING. BRUTO ING. BRUTO ING. BRUTO BP

US#/IA US#/IA US#/IA US#/IA US#/AO US#/AO

1B152B524 1'6B000 '9B556 1B'28B080 484B+49B02' 460B'1'B6181B'66B225 161B200 46B858 1B5+4B28' 5+4B61'B'18 545B648B0401B'66B225 161B200 46B858 1B5+4B28' 5+4B61'B'18 545B648B0401B'66B225 161B200 46B858 1B5+4B28' 5+4B61'B'18 545B648B0401B810B065 214B000 62B0+2 2B086B1'+ +61B440B0'9 +2'B05'B4682B25'B906 266B000 ++B285 2B59+B191 94+B9+4B+60 900B188B'+5'B194B555 '++B200 109B500 'B681B255 1B'4'B658B146 1B2+5B924B0+64B080B410 482B000 1'9B980 4B+02B'90 1B+16B'+2B18+ 1B629B848B2054B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B169

4B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B1694B915B122 580B800 168B568 5B664B489 2B06+B5'8B6'2 1B96'B'10B169

cos rec3p ao10B2++B5+5 1B466B+681B494B9261B494B9261B980B9682B466B2+0'B495B682

;&%S-" 4B465B''8+.'''''''' 6.++11111111 5B'+8B9'2

6.9 '0.''''''' 8.402''''''' 5B'+8B9'24.2 44.''''''' 12.280''''''' 5B'+8B9'2+.1 68 18.8'6 5B'+8B9'2

4.2 82 22.+14 5B'+8B9'25.4 100 2+.+ 5B'+8B9'25B'+8B9'25B'+8B9'25B'+8B9'25B'+8B9'25B'+8B9'25B'+8B9'25B'+8B9'2


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ING COMPAIAS ING ESTAO ING COMPAIAS ING ESTAO ISPONIBLE

US#/AO US#/AO US#/AO US#/AO >PGB

50/50 50/50 50/18 50/18 US#/AO2'0B156B809 2'0B156B809 105B805B84+ '54B50+B++12+2B824B020 2+2B824B020 125B420B4+6 420B22+B5642+2B824B020 2+2B824B020 125B420B4+6 420B22+B5642+2B824B020 2+2B824B020 125B420B4+6 420B22+B564'61B526B+'4 '61B526B+'4 166B198B1+8 556B855B290450B094B18+ 450B094B18+ 206B91'B699 69'B2+4B6+66'+B962B0'8 6'+B962B0'8 29'B2+8B804 982B645B2+2814B924B10' 814B924B10' '+4B6'0B'89 1B255B21+B816981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+

981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+981B655B085 981B655B085 451B2+8B622 1B512B0'1B54+


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EVALUACION ECONOMICA PLANTA ETRACCION LICUABLES >ACUIBA

AO OLUMEN TOTA RESIUAL RESIUAL GLP GASOLNAT PRECIO RESO RESIU

MM=3 MM=3 MPC TON/IA BBL/IA GAS RESIUAL US#/IA

VENTA

#US/MMBTU

2006 6.5 6.'1 222B8'6 '40.+ 659 5.00 1B152B5242007 +.+ +.48 264B154 40'.59 +81 5.00 1B'66B2252008 +.+ +.48 264B154 40'.59 +81 5.00 1B'66B225200" +.+ +.48 264B154 40'.59 +81 5.00 1B'66B2252010 10.2 9.91 '49B968 5'4.6' 1B0'5 5.00 1B810B0652011 12.+ 12.'4 4'5B+8' 665.6+ 1B288 5.00 2B25'B9062012 15.2 14.++ 521B598 +96.+ 1B542 5.00 2B69+B+462013 1+.+ 1+.19 60+B059 92+.+4 1B+95 5.00 'B1'9B+602014 20.2 19.62 692B8+4 1058.+8 2B049 5.00 'B58'B6012015 22.+ 22.05 ++8B688 1189.81 2B'02 5.00 4B02+B441

2016 25.2 24.48 864B50' 1'20.85 2B556 5.00 4B4+1B2812017 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222018 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B122201" 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222020 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222021 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222022 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222023 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222024 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222025 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222026 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B1222027 2+.+ 26.91 950B'18 1451.89 2B809 5.00 4B915B122

TOT%"ES

INVERSIHN ESTIMAA E PLANTAS

!LU:O GAS ETRAC. GLP TRAC. GASO GAS RESI. VERSIHN APRO OP/MTTO/AM

TON/IA BBL/IA MM=3 MMUS# MMUS#/AO

6.5 '62.96 659 6.'1 100 1.00+.+ 429.9+ +81 +.48 100 1.00

+.+ 429.9+ +81 +.48 100 1.00+.+ 429.9+ +81 +.48 100 1.00

10.2 569.56 1B0'5 9.91 120 1.2012.+ +09.16 1B288 12.'4 144 1.4415.2 848.+6 1B542 14.++ 1+' 1.+'1+.+ 988.'6 1B+95 1+.19 20+ 2.0+20.2 112+.96 2B049 19.62 249 2.4922.+ 126+.56 2B'02 22.05 299 2.9925.2 140+.16 2B556 24.48 '58 '.58


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2+.+ 1546.+6 2B809 26.91 '94 '.942+.+ 1546.+6 2B809 26.91 '94 '.942+.+ 1546.+6 2B809 26.91 '94 '.942+.+ 1546.+6 2B809 26.91 '94 '.942+.+ 1546.+6 2B809 26.91 '94 '.94 20.88899'82+.+ 1546.+6 2B809 26.91 '94 '.94

2+.+ 1546.+6 2B809 26.91 '94 '.942+.+ 1546.+6 2B809 26.91 '94 '.942+.+ 1546.+6 2B809 26.91 '94 '.94

!LU:O GAS 1er mo=3o 2=o mo=3o 'er mo=3o 4o mo=3o 5o mo=3o

2006 6.52007 +.+ 502008 +.+ 50200" +.+ 502010 10.2

2011 12.+ 502012 15.2 1002013 1+.+ 1002014 20.2 502015 22.+2016 25.22017 2+.+2018 2+.+201" 2+.+2020 2+.+2021 2+.+2022 2+.+

2023 2+.+2024 2+.+2025 2+.+2026 2+.+


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PRECIO ING. GLP PRECIO ING. GASOLINA ING. BRUTO ING. BRUTO INVERSION EPRECIACION

GLP US#/IA GASOLINA US#/IA US#/IA US#/AO

VENTA NATURAL

#US/TON #US/TON MMUS# MMUS# MMUS#

'89 1'2B508 54.8+ '6B1+' 1B'21B205 0.00 0.00'89 156B968 54.8+ 42B851 1B566B044 50.00 0.00'89 156B968 54.8+ 42B851 1B566B044 5+1.61 50.00 6.25'89 156B968 54.8+ 42B851 1B566B044 5+1.61 50.00 12.50'89 20+B9'' 54.8+ 56B+64 2B0+4B+62 +5+.29 0.00 18.+5'89 258B898 54.8+ +0B6+6 2B58'B480 942.9+ 50.00 18.+5'89 '09B860 54.8+ 84B589 'B092B195 1B128.65 100.00 25.00'89 '60B825 54.8+ 98B502 'B599B08+ 1B'1'.6+ 100.00 '+.50'89 411B+90 54.8+ 112B414 4B10+B805 1B499.'5 50.00 50.00'89 462B+51 54.8+ 126B'2+ 4B616B519 1B685.0' 56.25

'89 51'B+1+ 54.8+ 140B2'9 5B125B2'+ 1B8+0.+1 50.00'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9 4'.+5'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9 '+.50'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9 '+.50'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9 '1.25'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9 18.+5'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9 6.25'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9'89 564B682 54.8+ 154B152 5B6''B956 2B056.'9

450.00 450.00


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2.8'168464 45 12+.425809

2+.+ 45 1246.5 9.+82162+6

400,EP&E#-%#-O

-/E&S-O 1ra 2=a 'ra 4a 5a Toa

0 050 0 050 6.25 6.2550 12.5 0 12.50 12.5 6.25 18.+5

50 12.5 6.25 18.+5100 12.5 6.25 6.25 0 25100 12.5 6.25 18.+5 0 '+.550 12.5 6.25 18.+5 12.5 0 50

12.5 6.25 18.+5 18.+5 0 56.256.25 6.25 18.+5 18.+5 0 50

6.25 18.+5 18.+5 0 4'.+518.+5 18.+5 0 '+.518.+5 18.+5 0 '+.512.5 18.+5 0 '1.25

18.+5 0 18.+56.25 6.25

450 100 50 150 150 0 450


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PRECIO COSTO COSTOS UTILIAES !LU:O !LU:O

GAS RICO MATERIA OPERACIHN ANTES E IMPUESTO NETO NETO

MAT. PRIMA PRIMA IMPUESTOS UTILIAES ACUMULAO

#US/MMBTU MMUS# MMUS# MMUS# MMUS# MMUS# MMUS#

5.00 0.00 0.00 0.00 0.005.00 0.00 0.00 C50.00 C50.005.00 541.55 5.45 18.'5 4.59 C29.99 C+9.995.00 541.55 5.45 12.10 '.0' C28.42 C108.415.00 +1+.'8 +.22 1'.94 '.48 29.20 C+9.215.00 89'.21 8.99 22.02 5.50 C14.+4 C9'.945.00 1B069.04 10.+6 2'.85 5.96 C5+.11 C151.055.00 1B244.8+ 12.5' 18.++ 4.69 C48.42 C199.485.00 1B420.+0 14.'0 14.'5 '.59 10.+6 C188.+15.00 1B596.5' 16.0+ 16.18 4.05 68.'9 C120.''

5.00 1B++2.'6 1+.84 '0.52 +.6' +2.89 C4+.445.00 1B948.18 19.61 44.85 11.21 ++.'9 29.955.00 1B948.18 19.61 51.10 12.++ +5.82 105.++5.00 1B948.18 19.61 51.10 12.++ +5.82 181.605.00 1B948.18 19.61 5+.'5 14.'4 +4.26 255.865.00 1B948.18 19.61 69.85 1+.46 +1.14 '26.995.00 1B948.18 19.61 82.'5 20.59 68.01 '95.015.00 1B948.18 19.61 88.60 22.15 66.45 461.455.00 1B948.18 19.61 88.60 22.15 66.45 52+.905.00 1B948.18 19.61 88.60 22.15 66.45 594.'55.00 1B948.18 19.61 88.60 22.15 66.45 660.805.00 1B948.18 19.61 88.60 22.15 66.45 +2+.25

294.+1 881.0+ 220.2+ +2+.25

TASA INTERNA E RETORNO(%) 16.54VALOR PRESENTE NETO MMUS#

AL 10% 60.34 "4.27 154.61AL 15% 3".77 15.5" 55.35AL 20% 31.11 18.32 4".42


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440.19+'24

Mod_060_Planta Recuperacion de Licuables Calculo_GLP

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