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New Membrane Applications in Gas ProcessingNew Membrane Applications in Gas Processing
By By
Kaaeid A. Lokhandwala and Marc JacobsKaaeid A. Lokhandwala and Marc Jacobs
Membrane Technology and Research, IncMembrane Technology and Research, Inc. .
1360 Willow Road, Menlo Park, CA 94025 1360 Willow Road, Menlo Park, CA 94025
Membrane Separation MechanismMembrane Separation Mechanism
MTR’s Rubbery Membranes Reject Methane MTR’s Rubbery Membranes Reject Methane and preferentially permeate the heavy hydrocarbonsand preferentially permeate the heavy hydrocarbons
PP11 D D1 1 . S. S11
PP22 D D2 2 . S. S22
=
Permeability = Diffusivity * Solubility Permeability = Diffusivity * Solubility (P) (D) (S)(P) (D) (S)
Membrane SelectivityMembrane Selectivity
Glassy v/s Rubbery MembranesGlassy v/s Rubbery Membranes
Glassy MembranesGlassy MembranesFast GasFast Gas Slow GasSlow Gas
HexaneHexane
PropanePropaneHH22OO
EthaneEthane
COCO22
MethaneMethane
HydrogenHydrogenNitrogenNitrogen
HydrogenHydrogen
COCO22HH22OO
NitrogenNitrogen
MethaneMethane
EthaneEthane
PropanePropaneHexaneHexane
Rubbery Membranes Rubbery Membranes
Fast Gas Fast Gas Slow GasSlow Gas
Membrane System InstallationsMembrane System Installations
Gas/Gas Separation SystemsGas/Gas Separation Systems
Glassy Glassy MembranesMembranes
Rubbery Rubbery MembranesMembranes
HH22/N/N22, CH, CH44 ~ 200 Units ~ 200 Units
OO22/N/N22 ~ 5,000 Units ~ 5,000 Units
COCO22/CH/CH44 ~ 200 Units~ 200 Units
Vapor/Gas Separation SystemsVapor/Gas Separation Systems
VOC/Air VOC/Air
Hydrocarbon/NHydrocarbon/N22. CH. CH44 ~ 100 Units ~ 100 Units
Polymeric Selective Polymeric Selective LayerLayer
Microporous Microporous SupportSupport
Support Support FabricFabric
Separating LayerSeparating Layer
Layers for Mechanical Layers for Mechanical SupportSupport
MTR’s Composite Membrane
Module housingModule housing
SpacerSpacer
MembraneMembrane
SpacerSpacer
Feed flowFeed flow
Permeate flowPermeate flow
after passing throughafter passing throughmembranemembrane
Feed flowFeed flow
Feed flowFeed flow
Permeate flowPermeate flow
Residue flowResidue flow
Residue flowResidue flow
MTR Spiral Wound Cartridge
NGL Separation Skid
Flow CapacityFlow CapacityMax: 8 MMSCFD Max: 8 MMSCFD Operated: 2.5-3.0 MMSCFD Operated: 2.5-3.0 MMSCFD Pressure ratingPressure rating Max: 1250 psig Max: 1250 psig Operated: 475 psigOperated: 475 psig TemperatureTemperatureMax: 135Max: 135ooF F Operated: 100-125Operated: 100-125ooF F
Field Data - Feed/Permeate Flow ratesField Data - Feed/Permeate Flow rates
0
200
400
600
800
1000
1200
1400
4/20 5/10 5/30 6/19 7/9 7/29
Time (Date)
Flo
w R
ate
(s
cfm
)
0 20 40 60 80 89
Operating Time (Days)
Location: Chevron’s Lost Location: Chevron’s Lost Hills Hills Station, CA Station, CA Feed pressure: 450 psig Feed pressure: 450 psig Avg. Feed Flow rate:Avg. Feed Flow rate:
2.8 MMSCFD 2.8 MMSCFD Avg. Permeate Flow rate: Avg. Permeate Flow rate:
0.6 MMSCFD 0.6 MMSCFD
Field data - Percent Removal RatesField data - Percent Removal Rates
10
20
30
40
50
60
70
80
90
100
1997-11-16 1998-1-5 1998-2-24 1998-4-15 1998-6-4 1998-7-24
Date
Per
cen
t R
emo
val
(%
)
C3
C4
C5
C6
C8
Component Average %Removal
Propanes 55.7Butanes 61.0
Pentanes 68.1Hexanes 74.0Octanes 91.4
Field Data - Hydrocarbon Dewpoints
0
20
40
60
80
100
120
140
160
8/8/97 9/27/97 11/16/97 1/5/98 2/24/98 4/15/98 6/4/98 7/24/98
Date
Hyd
rocarb
on
Dew
po
int
in
Dewpoint of Conditioned Gas oF
Feed Gas Temperature oF
Dewpoint of Feed Gas oF
Field Data - Hydrocarbon DewpointsField Data - Hydrocarbon Dewpoints
0
20
40
60
80
100
120
140
160
1997-8-8 1997-9-27 1997-11-16
1998-1-5 1998-2-24 1998-4-15 1998-6-4 1998-7-24
Date
Hyd
roca
rbo
n D
ewp
oin
t in
Dewpoint of Conditioned Gas oF
Feed Gas Temperature oF
Dewpoint of Feed Gas oF
NGL Separation and Recovery ApplicationsNGL Separation and Recovery Applications
• Well-head Gas Dewpoint Control Well-head Gas Dewpoint Control
• Associated Gas Liquids Recovery Associated Gas Liquids Recovery
• Engine and Turbine Fuel Gas Conditioning Engine and Turbine Fuel Gas Conditioning
• Propane Refrigeration Plant Debottleneck Propane Refrigeration Plant Debottleneck
• Re-injection Gas Liquids Recovery Re-injection Gas Liquids Recovery
• Flare Gas Liquids Recovery/Conditioning Flare Gas Liquids Recovery/Conditioning
• Vapor Recovery from Storage Tank LossesVapor Recovery from Storage Tank Losses
Value of NGL (@ $ 14/bbl): $ 1.2 Million/yr Value of NGL (@ $ 14/bbl): $ 1.2 Million/yr Both Hydrocarbon and Water Dewpoint Reduced in one processBoth Hydrocarbon and Water Dewpoint Reduced in one process
Price of VaporSep System: $ 750,000-850,000Price of VaporSep System: $ 750,000-850,000
Membrane Membrane SystemSystem
Raw Raw Natural GasNatural Gas
To High Pressure To High Pressure PipelinePipeline
Stabilizer Stabilizer 250 psia250 psia
Booster Booster CompressorCompressor
250 psia 250 psia 6 MMSCFD6 MMSCFD
Hydrocarbon Hydrocarbon Dewpoint: 15Dewpoint: 15ooF F
1000 psia1000 psia
10562 gpd10562 gpdNGLNGL
1000 psia 1000 psia 9595ooFF
CC33+ enriched gas+ enriched gas
Wellhead Dewpoint ControlWellhead Dewpoint Control
Economic Comparison – Dewpoint ControlEconomic Comparison – Dewpoint Control
ProcessProcess Installed Cost Installed Cost Processing Cost Processing Cost (MM$)(MM$) ($/inlet Mscf) ($/inlet Mscf)
Propane Refrigeration 1.6 0.165 Propane Refrigeration 1.6 0.165 MembraneMembrane 1.1 1.1 0.098 0.098
Propane Refrigeration Cost: Purvin and Gertz, June 1999, Private Study Propane Refrigeration Cost: Purvin and Gertz, June 1999, Private Study
Basis: 10 MMSCFD Plant/Lean Gas (3.9 GPM, 1185 Btu/SCF)Basis: 10 MMSCFD Plant/Lean Gas (3.9 GPM, 1185 Btu/SCF)
Increased Oil Production: Increased Oil Production: 870 Barrels/day 870 Barrels/day Value of Additional Oil Recovered (@ $ 10/bbl): Value of Additional Oil Recovered (@ $ 10/bbl): $ 3.0 Million/yr $ 3.0 Million/yr Additional Power required: Additional Power required: 470 hp 470 hp
Price of VaporSep System: $ 1 - 1.25 MillionPrice of VaporSep System: $ 1 - 1.25 Million
Well-head Well-head Crude Crude
1015 psia1015 psia
Compressed Compressed Natural Gas Natural Gas 47 MMSCFD47 MMSCFD
Crude to Crude to Storage Storage 315 psia315 psia
Membrane System
250 psia250 psia
15 psia15 psia
Associated Associated GasGas
Associated Associated GasGas
Platform Associated Gas TreatmentPlatform Associated Gas Treatment
Gas EngineGas Engine
Raw Fuel GasRaw Fuel Gas
Conditioned Conditioned Fuel GasFuel Gas
CompressorCompressor
Membrane SystemMembrane System
Compressed Compressed Natural GasNatural GasMembrane System Price : $150,000Membrane System Price : $150,000
Process Conditions Process Conditions MembraneMembrane FeedFeed Conditioned Fuel GasConditioned Fuel GasTemperature Temperature ooFF 9595 5151Pressure (psia) Pressure (psia) 955 955 945945Flow Rates (MMscfd)Flow Rates (MMscfd) 0.95 0.95 0.50.5Octane NumberOctane Number 113.7113.7 116116Hydrocarbon Dewpoint (Hydrocarbon Dewpoint (ooF)F) 9595 3737
Fuel Gas Conditioning - Gas Engine ExampleFuel Gas Conditioning - Gas Engine Example
Existing fuel gas compressorExisting fuel gas compressor
Membrane FuelMembrane FuelConditioning UnitConditioning UnitRaw FuelRaw Fuel
GasGas
Conditioned Conditioned Fuel Gas Fuel Gas To TurbineTo Turbine
Fuel Gas Flow Rate (MMSCFD) :Fuel Gas Flow Rate (MMSCFD) : 6.1 6.1 Feed Temperature (Feed Temperature (ooF) :F) : 120 120 Conditioned Fuel Dewpoint(Conditioned Fuel Dewpoint(ooF) :F) : 76 76 NGL Recovered (gpd) :NGL Recovered (gpd) : 15,000 15,000 Value of Recovered NGL (US $) :Value of Recovered NGL (US $) : 500,000 500,000 Membrane System Price (US $) :Membrane System Price (US $) : 400,000 – 600,000400,000 – 600,000
Fuel Gas Conditioning - Gas Turbine Case
Typical Fuel Conditioning Skid-mounted Unit
Location: Nigeria Location: Nigeria Flow Capacity: 2.5 MMSCFD Flow Capacity: 2.5 MMSCFD Pressure rating 550 psig Pressure rating 550 psig Operating pressure: 220 psig Operating pressure: 220 psig Feed hydrocarbon dewpoint: 82Feed hydrocarbon dewpoint: 82ooF F Conditioned Gas Dewpoint: 20Conditioned Gas Dewpoint: 20ooFF
Designed for Offshore Installation Designed for Offshore Installation Main System Components Main System Components Membrane Modules/Housings Membrane Modules/Housings Filter Separator/Coalescer Filter Separator/Coalescer Inlet and Discharge Valves Inlet and Discharge Valves System Dimensions: 6 ft (W) x 8 ft (L) x 8 ft (H)System Dimensions: 6 ft (W) x 8 ft (L) x 8 ft (H)
Advantages of Membrane SystemsAdvantages of Membrane Systems
• Simple passive system Simple passive system
• High on-stream factor (typically > 98%) High on-stream factor (typically > 98%)
• Minimal or no operator attention Minimal or no operator attention
• Small footprint, low weight (Platform Applications) Small footprint, low weight (Platform Applications)
• Ambient temperature operation in many applications Ambient temperature operation in many applications
• Large turndown ratio Large turndown ratio
• Low maintenance Low maintenance
• Lower capital and operating costsLower capital and operating costs
SummarySummary
Wide range of applications in the Oil, Gas and RWide range of applications in the Oil, Gas and R
efining Industries efining Industries
Gas:Gas: Fuel gas conditioning, NG dewpointing, Natural Fuel gas conditioning, NG dewpointing, Natural
Gas Dehydration. Gas Dehydration.
Oil:Oil: Associated gas processing, Vapor recovery from Associated gas processing, Vapor recovery from
storage tanks and transportation. storage tanks and transportation.
Refining:Refining: LPG/Fuel gas, Hydrotreater/Hydrocracker Purg LPG/Fuel gas, Hydrotreater/Hydrocracker Purg
e, Refinery gas plant, Hydrogen recovery. e, Refinery gas plant, Hydrogen recovery.