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Advances in Membrane Materials Provide New Gas … File name 1 Advances in Membrane Materials...

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1 File name 1 Advances in Membrane Materials Provide New Gas Processing Solutions Patrick Hale Randall Gas Technologies A Division of ABB Lummus Global (ABB) Kaaeid Lokhandwala Membrane Technology and Research, Inc. (MTR)
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1File name 1

Advances in Membrane Materials Provide New Gas Processing Solutions

Patrick HaleRandall Gas TechnologiesA Division of ABB Lummus Global (ABB)

Kaaeid LokhandwalaMembrane Technology and Research, Inc. (MTR)

2File name 2

Outline

• ABB–Randall Gas Technologies/MTR Alliance

• Composite Membranes• Materials selection flexibility

• Improved stability and fouling resistance

• New Processes• NGL Removal

• Nitrogen Removal

• CO2 Removal

• H2S Removal

3File name 3

ABB–Randall Gas Technologies and MTR Have Formed an Alliance

• Randall Gas Technologies• A division of ABB Lummus Global (ABB)

• A process development and engineering company serving the

natural gas industry

• Membrane Technology and Research, Inc. (MTR) • A supplier of membrane gas separation systems

• A leader in membrane development

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ABB/MTR’s Technology is Based on New Composite Membranes

Nonporous Coated Selective Layer

MicroporousSupportLayer

SupportFabric

Composite Membrane

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The Porous Support and the Selective Layer Can Be Optimized Separately

Desired Properties

• High permeability

• High selectivity

• Chemical resistance

Desired Properties

• No mass transfer resistance

• Mechanical strength

• Chemical resistance

6File name 6

Composite Membranes and Processes

Nitrogen RejectionN2/CH4NitroSep™

CO2 RemovalCO2/CH4Z-Top™

H2S RemovalH2S/CH4P-TopTM

Fuel ConditioningDew Point Adjustment

NGL/Natural GasVaporSep®

ApplicationSeparationProcess Name

7File name 7

Membranes Are Packaged in Spiral-Wound Modules

Each module contains

20 to 50 m2 of membrane

Area

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Membrane Fouling is a Major ProcessDesign Concern

Potential Foulants in Natural Gas

• Carbon Dioxide

• Hydrogen Sulfide

• Mercury

• Salt

• Asphaltenes

• Waxes

• Water

• Mercaptans

• Oxygen

• Aromatics

• Glycols

• Methanol

• Amines

• Sulfur

9File name 9

Effect of Water and BTEX Aromaticson ABB/MTR’s Composite Membranes

• Membranes are inert to water vapor or liquid

• Water goes with the permeate gas

• VaporSep and P-Top membranes preferentially permeate BTEX

• Vapor concentrations up to saturation are not a problem

• Z-Top rejects BTEX aromatics

• High vapor concentrations do not effect membrane but condensation should be minimized to avoid physical damage

Water

BTEX Aromatics

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Hydrocarbon-Permeable Membranes Phase Envelope

0

300

600

900

1200

1500

1800

-100 -50 0 50 100 150

Temperature (oF)

Pres

sure

(psi

a)

Point A

Point B

Low PressureNGL-Rich Stream

NGL-Depleted Stream

Point AFeed Gas

Point BResidue Gas

Residue GasPhase Envelope

Feed GasPhase Envelope

11File name 11

Hydrocarbon-Rejecting CO2 Permeable Membranes - Phase Envelope

0

300

600

900

1200

1500

1800

-50 -30 -10 10 30 50 70 90 110 130 150

Temperature (oF)

Pres

sure

(psi

a)

Point A

Point B

Low PressureCO2-Rich Stream

CO2-Depleted Stream

Point AFeed Gas

Point B Residue Gas

Residue Gas Phase Envelope

Feed Gas Phase Envelope

12File name 12

Potential Pretreatment Options for Membrane Systems

Feed GlycolDehydration

CoalescingFilter

AbsorbentGuard Bed

Refrigeration

Particle Filter MembraneHeater

Braces and a belt will handle any upset but are expensive

Tough membranes minimize pretreatment required

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ABB/MTR Processes

• NGL Removal by VaporSepTM

• Nitrogen Removal by NitroSepTM

• CO2 Removal by Z-TopTM

• H2S Removal by P-TopTM

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History of NGL Membrane Applications

• A long history of use for various hydrocarbon separation and recovery applications

• Commercial success – Prestigious Kirkpatrick Award Winning Technology

Applied for wide range of flows: 0.2 to 90 MMscfdApplied at wide range of pressures: 50 to 1,000 psia

• More than 80 reference plants worldwide• Customers include ExxonMobil (8 Plants), BP Amoco (4

Plants), Sabic (4 plants), Formosa (10 plants)• More than 400 years of cumulative on-stream time

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Propylene and Isobutane Recovery Membrane Unit at a Polyolefins Plant

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NGL Separation - Applications

• Dew point control• Conditioning of rich fuel gas

• Three reference plants• Good fix for “black start gas” problem

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NGL Separation – UEG (El Paso) System

• Operational since May, 2002

• Processing 90 MMSCFD @ 900 psig

• Constant performance reducing C3+ to meet Siemens Turbine Fuel Specs.

• System Turndown to 25%

• System delivery in 14 weeks.

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Fuel Gas Conditioning Process Design

Main gas line

Membrane skid

Gas engine

Conditioned gas

dew point 4 ˚C

Pipeline gas

Main pipeline compressor

Raw fuel gasdew point

35 ˚C

Rich recycle gas

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Comparison of Nitrogen Removal Processes

Earlycommercialization

heavy hydrocarbons in product gas

Simple continuous operation

0.5-25Membrane

Early commercialization

heavy hydrocarbons in tail gas

Simple; batch operation requires bed switching

2-15PSA

Matureheavy hydrocarbonsIn product gas

Complex>15Cryogenic

Development Stage

Hydrocarbon RecoveryComplexityFlow Range

(MMscfd)Process

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Nitrogen Removal Process

Recycle gas(10-15% N2)

Separator

Pipeline gas(<4% N2)

Nitrogencontaminated

Fuel gas(50% N2)

low-pressure gas(10% N2)

CompressorCondensate

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Nitrogen Removal Skid

• Operational since November , 2002

• Constant performance reducing N2 content in natural gas from 6.5 mol-% to 2.5 mol-%.

• System Turndown to 50% on the fly

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Nitrogen Removal Process – Green Ranch

• Reducing N2 content in natural gas from 24 mol-% to 4 mol-%.

• Unattended operation –Remote Monitoring

• Capacity: 1 MMSCFD

• Designed for maximum flexibility for variation in inlet pressure, product pressure and flow rate.

• Under Installation at Site

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CO2 Removal: High CO2 Feed Gas

Pipeline product(2% CO2)Lean solvent

Membrane skids Solvent process(Bulk CO2 removal) (Polishing step)

Solvent to regeneration

CO2 depleted gas to solvent process

(8% CO2)High CO2feed gas

(60% CO2)To fuel/reinjection

(>90% CO2)

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H2S Removal – Fuel Gas Treatment

Main gas line

Membrane skid

H2S enriched recycle gas

High H2S Fuel 3400 ppm

Pipeline gasMain pipeline compressor

Low H2S Fuel To Engines

40 ppm

25File name 25

Composite Membranes: A Breakthrough in Membrane Technology

• Reduced pretreatment

• Greater flexibility in material selection

• Better performance

• Many new applications

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Membranes Are Not Just for CO2 Anymore

H2S

Heavy Hydrocarbons

Nitrogen

All Are Possible

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Thank You!

Membrane Technology and Research, Inc. (MTR)1360 Willow Road, Menlo Park, CA 94025

Telephone: 650-328-2228 Fax: 650-328-6580Website: www.mtrinc.com

and

Randall Gas TechnologiesA Division of Lummus Process Technology

ABB Lummus Global3010 Briarpark, Houston, TX 77042

Telephone: 713-821-4100 Fax: 713-821-3538Website: www.abb.com\lummus


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