capturing an opportunity - fakultet for … conferences...lean lng tank 6. feed and epc contracting...
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Slide No: 13 April 2005
Capturing an OpportunityCapturing an Opportunity-- NGL Recovery from RasGas LNG Train 4 NGL Recovery from RasGas LNG Train 4 --
Presented by Douglas C. Smith
Co-authored by Brett L. Ryberg
Slide No: 33 April 2005
Presentation Outline
� Opportunity
� Incentives
� Project Design Basis and Scope
� Execution Plan
� NGL Recovery Process Selection
� LNG Train Modifications
� Conclusions
Slide No: 43 April 2005
The Opportunity
1. Train 4 committed LNG sales could accommodate a
leaner product
2. Plot space & utilities available for NGL recovery as
a result of Acid Gas Injection on LNG Train 4
3. Ability to share in Al Khaleej Gas Project fractionation, LPG treating, and LPG storage &
loading facilities
Slide No: 53 April 2005
The Opportunity
Former SRU
Location
Sub-Station
Gas Receiving &Condensate Stabilization
Acid Gas Removal
RefrigerantPrep
Liquefaction and RefrigerationN2 Rejection
& Helium Recovery
Sub-station
Liquefaction and RefrigerationDehydration & Regeneration
Gas Treating
Instrument House
Train 4 Process Area - Base Layout
NGL
Recovery
Sub-Station
Gas Receiving &Condensate Stabilization
Acid Gas Removal
RefrigerantPrep
Liquefaction and RefrigerationN2 Rejection
& Helium Recovery
Sub-station
Liquefaction and RefrigerationDehydration & Regeneration
Gas Treating
Instrument
House
Train 4 Process Area - Opportunity
Slide No: 63 April 2005
Incentives
1. Ability to produce both “rich” and “lean” LNG products
opens new markets• “Lean” LNG compatible with Western markets
• “Lean” LNG able to access US East Coast
terminals, with better net pricing and lower shipping costs than US Gulf Coast
2. LPG products are higher value (“net back” basis) than LNG
3. Increased condensate production
4. Net result is a significant revenue boost, particularly if LNG production can be maintained despite NGL
recovery
Slide No: 73 April 2005
950 1000 1050 1100 1150 1200
Btu / SCF
RG Tr 4 w/
C3+ Recovery
RG Tr 1 / 2 / 3
UK and USA
India
(Petronet)
Continental
Europe
Asia
Incentives
New Market
Opportunities
Comparison of Typical LNG Product Specifications
Slide No: 83 April 2005
Project Scope
1. Method for recovery of NGLs
2. Modifications to Train 4 as required
3. New LNG rundown for lean LNG
4. New lean LNG storage and product loading
manifolds
Slide No: 93 April 2005
Original Train 4 Scope Unchanged
AKG Scope
Modified Train 4 Scope for NGL Extraction
New Train 4 NGL Extraction Scope
Block Flow Diagram - LNG Train 4 NGL Recovery
AGE / AGI
INLET FACILITIES
ACID GAS REMOVAL
GAS DEHYDRATION
MERCURY REMOVAL
OFFSHORE
CONDENSATESTORAGE
RICH LNG
LIQUEFACTION
AKG Fractionation
Plant
LEAN LNG
NGL RECOVERY
AKG LPG Storage & Loading
NGL
LPG´s
Slide No: 103 April 2005
Execution Plan
1. Feasibility & marketing studies
2. Process selection studies by competing suppliers
3. Unit re-rating studies by various technology
providers to identify necessary changes
4. Definition / implementation of changes via Change
Orders to EPC Contract
5. Procurement of long-lead turbomachinery & new
lean LNG tank
6. FEED and EPC contracting
Slide No: 113 April 2005
Execution Plan - Strategies
1. NGL Recovery facilities designed to minimize changes to Train 4
• Preserve Train 4 EPC lump sum pricing
• Manage Train 4 schedule risk
2. Priority given to earliest practical definition & implementation of Train 4 changes
3. Use existing EPC contractor for EPC of NGL Recovery facilities
• Minimize interferences with existing activities
4. Provisions for future C2 recovery
5. Construction planned & being executed to minimize work required after LNG Train 4 start-up
Slide No: 123 April 2005
Execution Plan - Schedule
1Q 2Q 3Q 4Q 1Q 2Q 3Q 4Q 1Q 2Q 3Q 4Q 1Q 2Q 3Q 4Q 1Q 2Q
Feasibility / Conceptual Studies
Process Screening
FEED
LNG 4 Rating and Modification Eng
Lean LNG Tank
EPC
Cooldown
Residue Gas Compressor Procurement
NGL Recovery Facilities EPC
Commissioning
AKG-1 Onplot
RasGas Expansion Projects
Train 4 NGL
2006
AKG-1 Offplot
Projects2004 20052002 2003
LNG Train 4
1st LNG
1st GAS
1st LPG
1st NGL
Slide No: 133 April 2005
NGL Recovery Process Selection
Key decision parameters:
1. Impact on Train 4 schedule
2. Impact on Train 4 liquefaction capacity
3. Impact on Train 4 availability
4. LPG recovery efficiency
5. Ability to accommodate future C2 recovery
6. Cost & schedule
Slide No: 143 April 2005
M
Residue
Gas
Feed
Gas
LPG
GE Frame 5
EC
Selected NGL Recovery Process Schematic (Ortloff)
Slide No: 153 April 2005
LNG Train Modifications
1. Train 4 facilities modifications to increase
throughput to compensate for feed gas shrinkage:
a. Inlet facilities
b. Condensate handling
c. Gas treating
2. Modifications to liquefaction & other units to
accommodate leaner feed stream
3. New facilities for storage & loading of lean LNG
product:
a. Additional lean LNG rundown piping
b. Additional LNG storage tank and inlet manifold
c. Product loading manifolds
Slide No: 163 April 2005
Lean LNG / C3 Recovery Mode Schematic
RefrigerantPreparation Unit
NGL Extraction Equipment Al Khaleej Gas
LPG Fractionation, Treating, Storage,
& Loading
G
M
M
End Flash Gas Exchanger
Fuel Gas Compressorw/ AFD Motor & Drive
(Increased Power)
Residue Gas CompressorFr 5 D Turbine andVFD Helper Motor
Hydraulic Turbine / Generator
w/ Excess Flow
Bypass
LNG RundownPump
N2 RejectionFlash Drum
NGL Extraction Unit
NNF
Excess C3/C4 NNF
ScrubColumn
Excess C3/C4 Refrigerant
MixedRefrigerant
(Tubes Reratedfor Higher Pressure)
M
C
H
E
Mixed LPG
- 41 degC
66.4BarA
- 33 degC
57 BarA
TreatedGas
RefrigerantMake-Up
Fuel Gas
LNG to Storage
Excess C2
(Changed from
Trays to Packing)
Slide No: 173 April 2005
Project Status
3Q 4Q 1Q 2Q 3Q 4Q 1Q 2Q 3Q 4Q 1Q 2Q 3Q
CONSTRUCTION
(Incl. Tank # 5)
2003 2004 2005 2006
ENGINEERING
PROCUREMENT
97%
94%
46%
MA
NGL
MA LNGTank# 5
31 Dec 31 Jan
Slide No: 183 April 2005
Conclusions
1. Production of lean LNG provides RasGas with new
market opportunities
• LNG to growing UK and US markets
• New LPG products
• Increased condensate production
2. LPG recovery can be incorporated without impact on guaranteed LNG production rate (BTU / hr basis)
3. Significant change successfully introduced into a lump sum project to enhance shareholder value