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Simultaneous Production of LNG and NGL

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Title: Gas liquids recovery in LNG plants Author: Philip Hagyard Last modified by: Anonymous Created Date: 12/20/2003 4:34:51 PM Document presentation format – PowerPoint PPT presentation

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Title: Simultaneous Production of LNG and NGL


1
Simultaneous Productionof LNG and NGL
2
  • Why NGL with LNG is of increasing interest
  • NGL recovery processes
  • Case study Cryomax process
  • ? 0 - 65 ethane recovery
  • ? Three configurations in LNG train
  • Operability and reliability considerations

3
NGL recovery in LNG plants
Next step
Existing LNG plants
100
Sometimes
C4
90 - 95
Sometimes
C3
30 - 50
Once
C2
Turbo-Expander
Scrub column
Scheme
4
Ethane
  • New markets require lean revaporised NG
  • UK Wobbe Index 51.4 MJ/Sm3 (max)
  • 50.8 MJ/Sm3 in Qatar
  • Met with 36 ethane extraction
  • Ethylene from ethane in Qatar
  • Qatar 2.5 Mtpa in 2008
  • UK 2.8 Mtpa (all feed stocks)
  • France 3.4 Mtpa (all feed stocks)

5
  • Why NGL with LNG is of increasing interest
  • NGL recovery processes
  • Case study Cryomax process
  • ? 0 - 65 ethane recovery
  • ? Three configurations in LNG train
  • Operability and reliability considerations

6
NGL recovery processes
  • Efficient ethane and propane plus extraction
  • Flexibility in ethane recovery
  • Good selectivity - minimal methane in NGL
  • Entrainment tolerant no heavy ends, ever
  • Resistance to equipment failure
  • Lean gas at high pressure to favour liquefaction

7
Conventional scrub column
C3R
NG 54 bar -35C
NG 55 bar -16C
NGL
LNG
C3R
SCRUB COLUMN
LIQUEFACTION MCHE
REFLUX
PRECOOLING
LEAN GAS
C3R
MR
NGL
DRY NG
8
Scrub column (high recovery)
MCHE
NG 52 bar -65C
NG 55 bar -35C
LNG
NGL
REFLUX
LIQUEFACTION MCHE
PRECOOLING
SCRUB COLUMN
OVERHEAD
LEAN GAS
C3R
MR
NGL
DRY NG
9
Cryomax
LNG
LIQUEFACTION MCHE
PRECOOLING
CRYOMAX DUAL COLUMN NGL RECOVERY
LEAN GAS
C3R
MR
NGL
DRY NG
10
Cryomax - LNG
LEAN GAS TO MCHE
PRECOOLED GAS
36 bar -80C
29 bar
DC1
RT
Recovery Tower Reflux
NGL
Demethaniser Reflux
US Patent 5,291,736
11
  • Why NGL with LNG is of increasing interest
  • NGL recovery processes
  • Case study Cryomax process
  • ? 0 - 65 ethane recovery
  • ? Three configurations in LNG train
  • Operability and reliability considerations

12
Cryomax Case Study
  • Qatar North Field gas climate
  • APCI C3/MCR process
  • High LNG capacity (approximately 5 Mtpa)
  • High natural gas pressures
  • Two GE Frame 7 gas turbines
  • MCHE outlet temperature 148C
  • Hydraulic turbines for MCR and LNG
  • Four ethane extraction rates (0-65) in three
    configurations

13
Cryomax Unit Location
  • Front End
  • Warm natural gas feed
  • No propane refrigeration
  • Driven by lean gas compression
  • Inlet Outlet (P T)

NG
NGL
NRU OFF GAS
FRONT END
NGL RECOVERY
LEAN GAS COMPRESSION
C3 PRECOOLING
NG LIQUEFACTION
NITROGEN REMOVAL
LNG
  • Straddle
  • Pre-cooled feed
  • Inlet Outlet (P T)

NGL
NG
STRADDLE
NRU OFF GAS
NGL RECOVERY
LEAN GAS COMPRESSION
C3 PRECOOLING
NG LIQUEFACTION
NITROGEN REMOVAL
  • Mid train
  • Pre-cooled feed
  • P2 lt P1
  • Simpler
  • Less power
  • Less capacity

LNG
NG
NGL
NRU OFF GAS
MID TRAIN
C3 PRECOOLING
NITROGEN REMOVAL
NGL RECOVERY
NG LIQUEFACTION
LNG
14
  • Why NGL with LNG is of increasing interest
  • NGL recovery processes
  • Case study Cryomax process
  • ? 0 - 65 ethane recovery
  • ? Three configurations in LNG train
  • Operability and reliability considerations

15
NGL recovery rates
65
36
16
1
Ethane
97.7
94.5
95.8
99.0
Propane
100
100
100
100
Butane
1019.0
1033.8
1042.0
1046.6
HHV Btu/scf
50.5
50.8
51.0
51.1
Wobbe MJ/Sm3
In LNG tanks in Qatar
16
Specific power
Target C2 Recovery
Front end
Straddle
Mid-train
17
  • Why NGL with LNG is of increasing interest
  • NGL recovery processes
  • Case study Cryomax process
  • ? 0 - 65 ethane recovery
  • ? Three configurations in LNG train
  • Operability and reliability considerations

18
Straddle - Lean gas compressor failure
  • Same as mid-train scheme
  • LNG quality unchanged
  • 10 to 15 reductionin throughput

19
Straddle - Joule-Thomson Mode
  • C3 precooling lean gas compressor OK
  • Specifications OK except Wobbe
  • 5-10 reductionin throughput

20
Straddle - Joule-Thomson Mode
  • C3 precooling lean gas compressor OK
  • Specifications OK except Wobbe
  • 5-10 reductionin throughput

Expander
JT mode
-
5.4
Expander power MW
1
36
Ethane recovery
76
93
Propane recovery
51.2
50.8
Wobbe Index MJ/Sm3
0.287
0.267
Sp consumption MW.h/t
21
Conclusions
  • Ethane and C3/C4 LPG extraction in Qatar meets
    lean gas specifications directly
  • The Cryomax process can be adapted to a wide
    range of ethane recovery requirements
  • Process efficiency insensitive to extraction rate
    or location
  • Cryomax Straddle Efficient and reliable
  • New or existing trains

22
Technip and Totalthank you for your attention
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