1 End Uses of Natural Gas

8/18/2019 1 End Uses of Natural Gas

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20444 A 07 END USES OF NATURAL GAS

END USES OF NATURAL GAS


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2

0 1

3 I F P T


C T

G G G

G

T

C

P


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2 0 1

3 I F P T


T G C

R

CONDITIONING/TRANSPORT

LIQUEFACTION

MARKETS

ENERGGAS

RI

T (NGV)

LNG

COMPRESSION

CNG

PIPE

CHEMICALCONVERSION

GTL / FT

DME

METHANOL

O /PP/PE

LPG CONDENSATES

LIQUIDS

F M O

H2S

Others (e.g. hydrates transport)

COMPRESSION R(EOR)

T /D

PROCESSING

PROCESSING

CO2 N2 O2 H2O

PRODUCTION

H


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2 0 1

3 I F P T


G :

L

G FG F

G

W

P

P

W

N N

S S P

LP

W

G


5/72


6/72

2 0 1

3 I F P T


G :

ETHANE

PROPANEBUTANE

PENTANES & HEAV FRACTIONS:P N C

C3C4

C2

C1

C5+

N G

L

W N H

CO2 H2S M ...

T (LPG, ) .

T , .


7/72

2 0 1

3 I F P T


G :

W : . O

. G , .

T , , :

DR : WATER H DROCARBONS

, W

C


8/72

2 0 1

3 I F P T


G :

N : L (D ) G L NGL R (W ) G H NGL

S G P CO2 / H2S H (V ) S G H CO2 / H2S A G A

(H2S+CO2) S G G L C G H CO2 / N 2

G NGL .

R : H2S / CO2, .

S (H2S CO2 ). T (C ) .

I CO2 , .

C


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2 0 1

3 I F P T


G :

G F :

− R

− I : , ,

R

− T

F − NGV: N G V ( : 60 MM

500,000 )

W ,


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2 0 1

3 I F P T


G :

G : ( ) ( , ,

)

I

N

( .

T . N ,

. G : ,

C


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2 0 1

3 I F P T

11EP 20500 A 06 FUNDAMENTALS OF LIQUEFIED NATURAL GAS (LNG)

G ,

A , E , J /K

COMMENTS

S : BP S R 2013


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2 0 1

3 I F P T


G : ,

C : T

− GTL FT : D N L

− C D E (DME) T DME

T − C M

− C O

C ,


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2 0 1

3 I F P T


G : ,

C , , .

G , , F.

I D E . DME LPG. T ,

.

G ,

L . S

T . O ,

.

C


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2 0 1

3 I F P T


G :

G EOR (E O R )

G

S E P

G


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2 0 1

3 I F P T


G :

N

OO

U

G

LNG

CNG

F /

L &C /

PE

GTL/FT

METHANOL

DME

NGH

CONVERSION TRANSPORT

GTW

D

G


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2 0 1

3 I F P T


G :

G ( 1000 ),

.

T , : , LNG ( LNG), GTW (G W

, CNG (C N G ) NGH (N G T / .

A , , : GTL, DME (D M E ).

H , , LNG,

, .

16

C


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2

0 1

3 I F P T


T

T G L (LNG)

C (CNG) T (NGH) G (GTW)

C

P

C

G


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2 0 1

3 I F P T


G :

T

A :

G

C P

R

T


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G :


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2 0 1

3 I F P T


G :

S : 90 50

SI ING OF MAIN GAS PIPELINE

L ( )

F

( M S 3 /

)

G :


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3 I F P T


G :

T .

B , 100 1000 , 24 56 6 7 MS3/ , . . 5500 MM .

N 48 , . C ,

56 . S ,

. G , 80 . E 100 , .

C

G :


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3 I F P T


G :

A M R

E , CO2 N E A

D L

L S N

I : C 1 % 1000 1.5 2 T CO2/MMB

LNG: LNG


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3 I F P T


LNG: LNG

L , T : 1 8 MTPA T : T= 160C 1 3 LNG = 580 S 3

LNG: LNG


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3 I F P T


LNG: LNG

L , 580 3 3 LNG. T

160C. T LNG MTPA, . . 4.5 3/ ),

, J , A LNG :

(

, )

, L P G (LPG)

( )

.

T : . O , ,

C

LNG:


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3 I F P T


LNG:

W 8 , 22.25 MT/ LNG + 1 M / LPG + 10 M /

LNG:


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3 I F P T


1

3

$/MMB

800

3200

4000

6400

8000

1600

4

2

5

LNG:

H : ($/ ) P : 0. 2.5P : 0.1 0.25 * 3

T : 0.5 4.5D : 1.2 2.8TOTAL: 2.1 10.5

C

LNG:


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3 I F P T


A M , LNG (FLNG) E

E S F

D H T

CO2 H CO2 U E

I : CO2 : CO2 < 50 L .: 10 15 % T .: 0.4 %/1000

R .: 0.5 1.5 % L : 35 45

CO2/MM NG :

CNG:


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3 I F P T


3 / 3

V

L

T ( C)

P

(

.

)


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CNG:


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3 I F P T


T CNG ( . 30C). T

150 250 /3, 500 / 3 LNG.

T , , ( )

.

T LNG ) , 2012,

, A ,

C

CNG:


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3 I F P T


A N

M

O

D N 2012

I

H

I K 0 : 12% T : 1%/1000 T 2000 :

30 T CO2/MM

NG : ,

T (NGH):


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3 I F P T


A CNG, . CNG, ;

T 40/50 . T . A N .

C


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T (NGH):


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3 I F P T


N 180 ( LNG 600 CNG 300 ). T

. NGH 20C. I

:

P : . 10C 60 , , .

T :

. R : ,

NGH , .

C

T (NGH):


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3 I F P T


A T

D I ,

. 2015 2020?

T 85% ()

I

H V

I K 0 .: 4 5 % T .: 3 %/1000 T 3000 : 50 T

CO2/MMB NG :

G (GTW):


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3 I F P T


G (GTW):


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3 I F P T


O . T , GTW (G W ), :

GTW

.

GTW :

, GTW ,

. T , , .

20 . A . S GTW

.

C

GTW:


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3 I F P T


GTW:


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3 I F P T


T . H

ISO 58%. T , , ,

T ; ,

A : , . .

(3*33 % (92% ) ,

, , S (54 1260 MW )

(25 )

C

G (GTW):


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3 I F P T



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G (GTW):


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3 I F P T


A M A

O R ( 2

) O

N

D E

< 1000 MW N (> 1500 2000 )

V AC/DC DC/AC

I 1 MS 3/ = 250 MW (

) E

( ): 50 % NG :


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0 1

3 I F P T


G

T

C F T (GTL/FT) D M E (DME) M

P

C

C


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3 I F P T


C


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3 I F P T


A . T , (

PO ) ( PO ), (CO) (H2). T H2/CO

T : F T , D

DME: ,

T . T , .) .

F , :

GTL/FT: H2/CO = 1.7 H2/CO = 2 D DME: H2/CO = 1 M H2 CO2 / CO + CO2 = 2

C

GTL/FT:


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3 I F P T


1920 1940 1960 1980 2000

1924 1935 WWII 1955 1980 82

1993

1990 2000 2006 2007

G C CO & H2

F.F & H.T

P F& T

1 I FTA

R

9 FT P G

S G II

( 16,000BPD)

WWII G LP R

SASOL II M PS R L(8,000 BPD)

ARGEF B R

SASOL II & III150,000 BPD SA , F C F BR

SASOLD .

SASOL II & III RR

S CFB R

SHELL BINTULU12,500 BPD M , C FB R

OR X (QP+SASOLC )34,000 BPD Q C C . S R .

PEARL(QP+SHELL)2 70,000 BPD Q

C C . F R .

GTL/FT:


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3 I F P T


P 3 S F T

FP

H2O / O2

S

S

FT

L HC (

)

HH

D+

P

(+ )

MARKETS:L

P

L

GTL/FT:


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3 I F P T


C F T , GTL/FT, . I :

( ),

F T : , ,

, (25 %).

A GTL , .

T , CO2 , .

C

GTL/FT:


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3 I F P T


R ( /

)

1. SMR

D

( S)

P

B

S/C > 2.5T: 850 900 CP 20 H2/CO 4.8


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GTL/FT:


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3 I F P T


3. ATR

S/C 1.2T 1050 CP 20 50 H2/CO 2.6

C : CO2 , F T

A

C POX

N.B. ATR,

GTL/FT: F T


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3 I F P T


M CO + 2 H2 (CH2) + H2O + 165 J

T

C : R :

: C1 >C200

, ,

HC

GTL/FT:


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3 I F P T


A U

E N

D

H2S H

CO2 H

( ) C

I H2S < 0.1 E : 42 52% E : 150 T CO2/M

NG :

O S /QP: 34,000

DME:

T :

P P JFE T F


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3 I F P T


T :

T : ( ) (

)

P P JFE T F

DME:


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3 I F P T


T D M E (DME) 150,000 , , . S

, DME ( . W 3

O CH3, DME LPG.

T DME, , .

T : (65 70 .

T : TOPSOE, LURGI, TEC , JFE .

C

DME:


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3 I F P T


A L CO2 GTL/FT

S P LPG

D H2S I :

2011 ( ) M

I H2S < 0.1 E : 60% E : 75 T CO2/MM

NG :

M :

3


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3 I F P T


3 : S M D

M :


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3 I F P T


M , CH3 OH, . M

( . ) , . T MTBE ( . 1/4 ),

. I , T :

F .

T 1000 / 198

.

C

F :


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3 I F P T


4 : DME (MTO / DTO)

SyngasPlant

MethanolPlant

N

MTO

+ OCPPlant

I MTO PE PP

PolyethylenePlant

PolypropylenePlantDME

Plant

M :


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3 I F P T


A M M CO2

GTL/FT

T

S

I H2S < 0.1 E : 65% E : 75 T CO2/M NG :

D H2S M :

,


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0 1

3 I F P T


T

T

C

P

C


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C

C


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3 I F P T


T : ( . ) ( )

I , W

. W , ,

.

T H ): C3+ . G J , , N2 .

C , L ( ), W 47 MJ/N 3,

T G N. S , .

C

T

3 H2S/CO2


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3 I F P T


2 2

EASEE : E A S E E

EASEE : H2S+COS < 3 < 19 L : CO2 25% T

H2S, S H2S+COS

0

4

3

2

1

T

C


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3 I F P T


I EASEE H2S H2S + COS 3 .

G :

LNG, (CO2 )

, , 2S , (H2S , )

, CNG : (H2S, CO2) .

C


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K

T :


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3 I F P T


T : , , .

T

G ( ), ( 160 ) (CNG).

C

(GTL/FT, DME) , .

T , (

, ). G ,

, .

A


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Volumecubic feet (cf)

cubic meter (cm) 35

Débit

Million cubic feet per day(MMcfd)

Billion cubicmeter per year(Bcm/y)

100 1

Valeur CalorifiqueBtu/cf Mcal/m3 Btu/m3 Mj/m3 kWh/m31000 9 35 000 35 10

Gaz naturel liquéfiém3 (GNL) m3 (gaz) MMBtu kWh

t (GNL) 2,5 1500 53 15 000

EquivalencesMMBtu gaz m3 gaz

1 bep 6 1801 t charbon 25 750

Chaleur / EnergieGJ Mcal kWh

Million Btu (MMBtu) 1 250 300

H / E

H V

L

(LNG)3 (LNG) 3 ( )

F

1

3 ( )

1 End Uses of Natural Gas

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