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New Electrostatic Technology for Desalting Crude Oil

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Page 1: New Electrostatic Technology for Desalting Crude Oil
Page 2: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

New Electrostatic Technology for Desalting Crude Oil

• Gary W. Sams PE–Director Research & Development

• Kenneth Warren PhD–Chief Process Consultant - Electrostatics

Page 3: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Desalter Performance Issues

• Opportunity Crudes• Heavy crude oils• Increased temperatures• Increased oil conductivity• Soluble Water

Page 4: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Oil Desalting

• Critical Variables include:– Flow, Temperature, – Water Content, Solids– Mix Water Injection Points– Mixing Energy Requirements– Recycle Water Schemes– Electrostatic Field Type

Page 5: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Process StagesChemicals – Electrostatic Fields – Hydraulics

• Coagulation– Requires Chemical Reaction

• Flocculation– Assisted by Electrostatic Forces

• Sedimentation– Depends Upon Vessel Flow Regime, Drop

Size & Viscosity

Page 6: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Partnership for Drop Growth

Chemicals Remove the Barriers…

Electrostatics Provide the Muscle…

Page 7: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Selection of Electrostatic Fields

• AC – Conventional & Deep-field• DC (Only with refined products)• Combination AC/DC• Modulated AC/DC Fields• Bi-Modal Modulation

Page 8: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Electrostatic Forces• Dipolar Attraction: Electrical

force produced by positive and negative centers on induced dipoles of water drops.

• Electrophoresis: Electrically induced movement of polar bodies in a uniform field toward closest electrode.

• Dielectrophoresis: Movement of polar bodies induced by a divergent electric field toward increasing gradient.

+ -

+ -

+ -

+ +

+

+

- -

-

-

Page 9: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Critical Voltage Gradient

x

y

y/x>1.9

• Polarized by the electrostatic field

• Deforms to a prolate spheroid

• Splits when ratio of axes becomes too large

or

Maximum Voltage at which Specified Drop Size Can Exist

2/1)/( dEc γε<

( - )

( + )

Page 10: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

AC Electrostatic Dehydrators

Viscous Drag

Weight

Dipolar Attraction

+ +- -

Dielectrophoretic Force ** Only Exists with Divergent Field

-+

Electrophoretic Force

Page 11: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Dipolar Attractive ForceBetween Equal Sized Drops

2

4

66 EKd

rF ε=F = Force of Attraction

e = Dielectric Constant

E = Electric Field Strength

r = Drop Radius

d = Interdrop Distance

Notice the Limitations:

• Very Sensitive to Drop Size

• Operates Over Short Range

• Critical Voltage Gradient Cannot Be Exceeded

Page 12: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Drop Forces in Uniform DC Field

Viscous Drag

Weight

Dipolar AttractionElectrophoretic

Force

++ --+

Page 13: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Drop Forces in Non-Uniform Field

Viscous Drag

Weight

Dipolar Attraction

Electrophoretic Force+

Dielectrophoretic Force:

+-+-

Holds Drops in Field Until Weight Overcomes Suspending Force

Page 14: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

} Bulk Water Removal

AC/DC Electrostatic Field

Page 15: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Coalescence in an AC/DC Field

+

Residual Drops from AC Field

- + - +

+ --+

Electrical Ground Reference

Page 16: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

AC/DC Electrostatic Dehydrator• Separation via Stokes’ Law Sedimentation• Multiple Coalescing Forces Grow Drops

– Brownian Collisions– Dipolar Attraction– Electrophoretic Movement– Dielectrophoretic Movement (Only in Divergent Fields)

• Drop Size “Cut Point” Defined by Balance of Dragand Weight

• Larger Mean Drop Size Than Previous Dehydrators

Page 17: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Electrostatic Field Terminology• Threshold Voltage Gradient

– Voltage Gradient Necessary to Initiate Coalescence

• Critical Voltage Gradient– Maximum Voltage Gradient at which a Specific

Diameter Drop Can Exist

• Modulation Frequency Affects– Drop Transport as function of oil conductivity– Drop Distortion as function of interfacial tension– Field Strength as function of applied voltage

Page 18: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

• Electrophoretic Force = 53 dynes• Drag = Weight = 0.01 dynes• Dipolar Force = 0.004 dynes• Dielectrophoretic Force = 0.002 dynes

Process ConditionsLow Oil Conductivity

750 Micron “Cut Point” Droplet5 kV / in Peak Voltage Gradient0.5% BS&W - Homogeneous

Magnitude of Electrostatic Forces

Page 19: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Conductivity in Crude OilsSources of Conductivity• Excess water in the electrode zone• Polar compounds in the oil• Solids-Stabilized dispersions

Effects of Conductivity – Performance Loss• Excessive arcing• Parasitic electric currents to the Interface• Loss of electrostatic field

Page 20: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

AC/DC Field Decay in Conductive Oils

Increasing Conductivity

Vol

tage

+

-

Page 21: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Conductivity Tolerant Designs

• Current-limiting Composite Electrodes• Electrostatic Field Modifications• Solids Removal Systems

– Mud-wash Systems (Sand Jets)– Interface Sludge Drains

Page 22: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Composite Electrode Array

Page 23: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Laboratory Pilot Tests

0.430.65805Diluted Bitumen

0.29NA

(Current Limit Exceeded)

6031Arabian Heavy

0.72 – 0.921.2 – 1.56015Maya

Outlet BS&W%

Composite Electrode

Outlet BS&W %

Steel Electrode

Flux (BPD/ft2)

Inlet BS&W

%Crude

Page 24: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Pilot Testing Facility

Page 25: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

High Reactance TransformerConventional Transformer Protection

0

20

40

60

80

100

0 10 20 30 40 50 60 70 80 90 100

Voltage, % of Full Scale

Cur

ren

t, %

of F

ull

Sca

le

Operating Range

Page 26: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Low Reactance TransformerPermits Voltage Modulation

0

20

40

60

80

100

0 10 20 30 40 50 60 70 80 90 100

Voltage, % of Full Scale

Cur

ren

t, %

of F

ull

Sca

le

Operating Range

Page 27: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Modulated AC/DC Benefits

Modulation Improvements:• Added Coalescing Power• More Effective on Smaller Drops• Enhanced Drop Growth• Higher Water Tolerance• Tolerant of Conductive Oils

Page 28: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Advanced Electrostatic Field ModulationEstablished Technology• Slow Speed Modulation (as in EDD®)

– Shifts Size Distribution to Larger Drops

Latest Technology• Pulse Modulation (1 to 20 Hz)

– Oscillates Drop Surfaces• Base Frequency (800 to 1600 Hz)

– Used to Limit Field Decay

Page 29: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Benefits of Bi-Modal Dehydration Pulse & Base Frequency

• Energizes Drops at Resonant Frequency• Deformed Drops Coalesce More Readily• Allows Adjustment for Physical Parameters

• Pulse Modulation - Interfacial Tension,Density, Viscosity

• Base Frequency - Oil Conductivity

Page 30: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Resonant Frequency Oscillation

• Electrophoretic movement becomes oscillatory and deforms drops• Surface free energy counters interfacial tension• Drop surface becomes highly reactive• Coalescence enhanced by reduced energy barrier

• High frequency electrostatic field applied• Marangoni Effect produces localized circulation in drop

Page 31: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Dual Frequency® Field Results

0

0.1

0.2

0.3

0.4

0.5

0 20000 40000 60000 80000 100000 120000

Dual Pola

rity (A

C/DC) w/ C

ompo

site

Dual Frequency (Bi -M

odal) w/ C

omposite

Capacity (BOPD)

Out

let B

S&

W (

%)

Page 32: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Dual Frequency Technology

• Sustains electrostatic field• Optimizes frequencies based on crude• Improves droplet mobility• Increases droplet coalescence• Achieves reduced water content

Page 33: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Dual Frequency® Advantages

• Reduced outlet BS&W by 30 to 95%• Tested on oils between 17 & 40 API.

• Reduces outlet salt by similar amounts• Easy retrofit to existing AC/DC dehydrators

or desalters• Easily optimized to process conditions.

Page 34: New Electrostatic Technology for Desalting Crude Oil

NPRA Spring National March 2006

Leadership in Electrostatic Technology