Stress- -Assisted Corrosion (SAC) in Assisted Corrosion (SAC) in - - PowerPoint PPT Presentation

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Stress- -Assisted Corrosion (SAC) in Assisted Corrosion (SAC) in - - PowerPoint PPT Presentation

Stress- -Assisted Corrosion (SAC) in Assisted Corrosion (SAC) in Stress Boiler Tubes Boiler Tubes Preet M. Singh* and Steve J. Pawel Pawel @ @ Preet M. Singh* and Steve J. * Georgia Institute Technology, Atlanta, GA * Georgia Institute


slide-1
SLIDE 1

Stress Stress-

  • Assisted Corrosion (SAC) in

Assisted Corrosion (SAC) in Boiler Tubes Boiler Tubes

Preet M. Singh* and Steve J. Preet M. Singh* and Steve J. Pawel Pawel@

@

* Georgia Institute Technology, Atlanta, GA * Georgia Institute Technology, Atlanta, GA @ Oak Ridge National Laboratory, Oak Ridge, TN @ Oak Ridge National Laboratory, Oak Ridge, TN

DOE Project #DE DOE Project #DE-

  • FC07

FC07-

  • 01ID1443

01ID1443

slide-2
SLIDE 2

Project Background Project Background

Industrial Boilers Industrial Boilers

To stack To stack

Electrostatic Electrostatic precipitator precipitator

Primary Primary Secondary Secondary Tertiary Tertiary

Air delivery: Air delivery: (Fuel) (Fuel) Smelt! Smelt! Economizer Economizer Boiler Boiler Superheater Superheater Screen Tubes Screen Tubes

slide-3
SLIDE 3

Stress Assisted Corrosion in Waterwall Tubes Stress Assisted Corrosion in Waterwall Tubes

Boilers can experience SAC from waterside Boilers can experience SAC from waterside in in

  • Floor

Floor

  • Waterwalls

Waterwalls

  • Screens

Screens

  • Roof

Roof

Stress Assisted Corrosion/ Cracking Stress Assisted Corrosion/ Cracking Welded Plate/Joint Welded Plate/Joint

  • Economizers

Economizers

  • Floor

Floor-

  • to Sidewall Seals

to Sidewall Seals

  • Smelt Box Attachments

Smelt Box Attachments

  • Port Attachments

Port Attachments

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SLIDE 4

Waterside Cracks in Waterwall Tube Near Waterside Cracks in Waterwall Tube Near Attachment Weld Attachment Weld

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SLIDE 5

SAC in Recovery Boiler Tubes SAC in Recovery Boiler Tubes

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SLIDE 6

Industrial Boilers and SAC Industrial Boilers and SAC

  • Water Leak in Some Industrial Boilers

Water Leak in Some Industrial Boilers can Potentially Cause Explosion can Potentially Cause Explosion

  • Numerous Accidents Reported

Numerous Accidents Reported

  • Some were Fatal

Some were Fatal

  • Project Benefits

Project Benefits

  • ~25 Trillion BTUs by 2020

~25 Trillion BTUs by 2020

  • Cost Savings of ~ $133

Cost Savings of ~ $133 Millon Millon/Year /Year

  • Safety

Safety

STEEL 1% PULP & PAPER 58% MANUFACTURING 4% MINING 4% PETROCHEMICAL 16% UTILITY 7% AGRICULTURE 1% CHEMICALS 4% FOOD 1% AUTOMOTIVE 4% STEEL 1% PULP & PAPER 58% MANUFACTURING 4% MINING 4% PETROCHEMICAL 16% UTILITY 7% AGRICULTURE 1% CHEMICALS 4% FOOD 1% AUTOMOTIVE 4%

Survey Data from Hercules Survey Data from Hercules-

  • BetzDearborn

BetzDearborn

SAC is Experienced in Various Industrial Boilers SAC is Experienced in Various Industrial Boilers

slide-7
SLIDE 7

Project Objective Project Objective

  • To Clarify Mechanisms Involved in Stress Assisted

To Clarify Mechanisms Involved in Stress Assisted Corrosion (SAC) of Boiler Tubes Corrosion (SAC) of Boiler Tubes

  • Determine K

Determine Key Parameters in its Mitigation and Control ey Parameters in its Mitigation and Control

  • Microstructure

Microstructure

  • Water Chemistry

Water Chemistry

  • Stress

Stress

  • Residual Stresses Due to Welding

Residual Stresses Due to Welding

  • Operational Stresses

Operational Stresses

slide-8
SLIDE 8

Project Team Project Team

  • Oak Ridge National Laboratory

Oak Ridge National Laboratory -

  • Dr. Steve J.
  • Dr. Steve J. Pawel

Pawel

  • Georgia Institute of Technology

Georgia Institute of Technology -

  • Dr. Preet M. Singh
  • Dr. Preet M. Singh
  • Others

Others

  • Lawrence Livermore National Laboratory

Lawrence Livermore National Laboratory -

  • Dr. Mike Quarry
  • Dr. Mike Quarry
  • Industrial Partners

Industrial Partners

  • Other Project Advisors

Other Project Advisors

  • Mr. John
  • Mr. John Hainsworth

Hainsworth – – B&W B&W

  • Dr. Ray
  • Dr. Ray Vasudevan

Vasudevan -

  • International

International Paper Paper

  • Mr. Mike Cooper
  • Mr. Mike Cooper –

– Longview Longview Inspections Inspections

  • Dr. W.B.A. Sharp
  • Dr. W.B.A. Sharp–

– MeadWestvaco MeadWestvaco

  • Mr. Steve
  • Mr. Steve Lukezich

Lukezich – – MeadWestvaco MeadWestvaco

  • Mr. Paul B.
  • Mr. Paul B. Desch

Desch -

  • ONDEO

ONDEO-

  • Nalco

Nalco

  • Dr. Peter
  • Dr. Peter Gorog

Gorog -

  • Weyerhaeuser

Weyerhaeuser Company Company Mark Mark Labell Labell – – Ahlstrom Ahlstrom

  • Dr. Barry Dooley
  • Dr. Barry Dooley –

– EPRI EPRI

  • Dr. Jim Keiser
  • Dr. Jim Keiser -
  • ORNL

ORNL

  • Mr. Mel
  • Mr. Mel Esmacher

Esmacher -

  • GE Specialty

GE Specialty Materials Materials

  • Mr. Karl
  • Mr. Karl Morency

Morency – – Georgia Pacific Georgia Pacific

slide-9
SLIDE 9

Main Project Tasks Main Project Tasks

  • Task 1:

Task 1: Laboratory Simulation of SAC Laboratory Simulation of SAC

  • IPST

IPST-

  • GTech

GTech

  • Task 2:

Task 2: Material Characterization Material Characterization

  • [ORNL and IPST

[ORNL and IPST-

  • GTech

GTech] ]

  • Task 3:

Task 3: Evaluation of Stress Effects Evaluation of Stress Effects

  • [ORNL]

[ORNL]

  • Task 4:

Task 4: Evaluation of Environmental Effects Evaluation of Environmental Effects

  • [IPST

[IPST-

  • GTech

GTech and ORNL] and ORNL]

  • Task 5:

Task 5: Communication to US Industry Communication to US Industry

  • [IPST

[IPST-

  • GTech

GTech and ORNL] and ORNL]

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SLIDE 10

Laboratory Simulation of SAC Laboratory Simulation of SAC

Task 1 Task 1

  • Develop Facilities to Simulate Boiler Tube

Develop Facilities to Simulate Boiler Tube Environment in Laboratory Environment in Laboratory

  • Capable of Controlling Water

Capable of Controlling Water-

  • Chemistry

Chemistry Variables Variables

  • Dissolved Oxygen

Dissolved Oxygen

  • pH

pH

  • Cl

Cl-

  • , SO

, SO4

4-

  • 2

2, and Other Ions

, and Other Ions

  • Conductivity

Conductivity

slide-11
SLIDE 11

Test Autoclave with Recirculation Loop Test Autoclave with Recirculation Loop

  • Test Capabilities

Test Capabilities

  • Temperature up to 350

Temperature up to 350oC, Pressure up to 3500 C, Pressure up to 3500 psi psi

  • Electrochemical Tests

Electrochemical Tests

  • AC Impedance

AC Impedance

  • Stressed Samples for SAC

Stressed Samples for SAC

  • Special Fixture for Constant Extension Rate Tests

Special Fixture for Constant Extension Rate Tests

Cooling Chamber Cooling Chamber

Test Test Autoclave Autoclave

Heating Chamber Heating Chamber High Pressure High Pressure Pump Pump Pressure Pressure Reducer Reducer

Storage Tank Storage Tank

Makeup Water Makeup Water

320 320oC, C, 1500 1500 psi psi

Sensors for pH, ORP, Sensors for pH, ORP, O2, Conductivity, etc. , Conductivity, etc.

N

2

N

2 2

+ + O

2

Cooling Chamber Cooling Chamber

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SLIDE 12

Autoclave with Recirculation Loop Autoclave with Recirculation Loop

  • 100 Liter Makeup Tank

100 Liter Makeup Tank

  • Heat Exchangers to Conserve Heat and Achieve Steady State Easily

Heat Exchangers to Conserve Heat and Achieve Steady State Easily

  • High Pressure Pump for Recirculation

High Pressure Pump for Recirculation

  • Continuous Water Chemistry Monitoring

Continuous Water Chemistry Monitoring

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SLIDE 13

Evaluation of Environmental Effects Evaluation of Environmental Effects

Task 4 Task 4

Effect of Environment on Magnetite Growth and Effect of Environment on Magnetite Growth and Properties Properties

slide-14
SLIDE 14

Boiler Environment and Magnetite Film on Boiler Environment and Magnetite Film on Tube Surface Tube Surface

3 Fe + 4 H 3 Fe + 4 H2

2O →

O → Fe Fe3

3O

O4

4 + 4 H

+ 4 H2

2

14 12 10 8 6 4 2 2.0 1.5 1.0 0.5 0.0

  • 0.5
  • 1.0
  • 1.5
  • 2.0

Fe - H2O - System at 320.00 C C:\HSC5\EpH\Fe320.iep pH Eh (Volts)

H2O

Fe Fe2O3 Fe3O4 Fe(+2a) FeO2(-a) ELEMENTS Molality Pressure Fe 1.000E+00 1.112E+02

Above ~ 230 Above ~ 230oC, Magnetite Film Forms on Carbon C, Magnetite Film Forms on Carbon Steel in Slightly Alkaline Oxygen Steel in Slightly Alkaline Oxygen-

  • free Water

free Water

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SLIDE 15

Stress Assisted Corrosion and Oxide Stress Assisted Corrosion and Oxide Scale Morphology Scale Morphology

slide-16
SLIDE 16

Magnetite Film Growth and Morphology Magnetite Film Growth and Morphology Under Boiler Conditions Under Boiler Conditions

  • SA 210 Carbon Steel Tube Samples

SA 210 Carbon Steel Tube Samples

  • Electrically Isolated Samples

Electrically Isolated Samples

  • Samples Attached to Large Cathodes with Different Areas

Samples Attached to Large Cathodes with Different Areas

  • Pure Water

Pure Water (Double

(Double-

  • Deionized

Deionized) )

  • With and Without N

With and Without N2

2 Purge or O

Purge or O2

2 Scavenger

Scavenger

  • 250

250o

  • C to 320

C to 320o

  • C

C

  • X

X-

  • Ray Diffraction of Sample Surface and

Ray Diffraction of Sample Surface and Metallography Metallography to Characterize Film to Characterize Film

  • Atomic Force Microscopy (AFM) for Film Morphology

Atomic Force Microscopy (AFM) for Film Morphology and Properties and Properties

slide-17
SLIDE 17

Atomic Force Microscopy Atomic Force Microscopy

Unexposed SA Unexposed SA-

  • 210 Carbon Steel Surface

210 Carbon Steel Surface

Topography Scan Topography Scan

  • Max. Roughness = 10 nm
  • Max. Roughness = 10 nm

10 8 6 4 2 µm 10 8 6 4 2 µm

  • 30
  • 20
  • 10

10 20 30 nm

slide-18
SLIDE 18

Electrically Isolated SA Electrically Isolated SA-

  • 210 Carbon Steel Exposed to

210 Carbon Steel Exposed to Deaerated Deaerated DI Water at 320 DI Water at 320o

  • C for 114 hours

C for 114 hours

SA210- Carbon Steel (Electrically isolated), in Deaereated DI water at 320C for 144h 10 20 30 40 50 60 70 80 90 100 1.000 1.500 2.000 2.500 3.000 3.500 4.000 4.500 5.000 d/[A] Relative Intensity

Fe Fe Fe3O4 Fe3O4 Fe3O4 Fe3O4 Fe2O3

slide-19
SLIDE 19

Electrically Isolated SA Electrically Isolated SA-

  • 210 Carbon Steel Exposed to

210 Carbon Steel Exposed to Deaerated Deaerated DI Water at 320 DI Water at 320o

  • C for 114 hours

C for 114 hours

10 8 6 4 2 µm 10 8 6 4 2 µm 1.5 1.0 0.5 0.0

  • 0.5
  • 1.0

µm

  • Electrically Isolated C

Electrically Isolated C-

  • Steel

Steel in Boiler Environment in Boiler Environment Forms Dense and Protective Forms Dense and Protective Magnetite Film on Surface Magnetite Film on Surface

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SLIDE 20

SA SA-

  • 210 Carbon Steel in Contact with Large Cathode

210 Carbon Steel in Contact with Large Cathode (Anode

(Anode Cathode Area Ratio 1:127) Cathode Area Ratio 1:127) Exposed to

Exposed to Deaerated Deaerated DI Water at DI Water at 320 320o

  • C for 114 hours

C for 114 hours

SA210- Carbon Steel (Anode-Cathode ratio 1:127), in Deaereated DI water at 320C for 144h 10 20 30 40 50 60 70 80 90 100 1.000 1.500 2.000 2.500 3.000 3.500 4.000 4.500 5.000 d/[A] Relative Intensity Fe

Fe Fe3O4 Fe3O4 Fe3O4 Fe3O4 Fe2O3 Fe2O3

slide-21
SLIDE 21

10 8 6 4 2 µm 10 8 6 4 2 µm

  • 600
  • 400
  • 200

200 400 600 nm

SA SA-

  • 210 Carbon Steel in Contact with Large Cathode

210 Carbon Steel in Contact with Large Cathode (Anode

(Anode Cathode Area Ratio 1:127) Cathode Area Ratio 1:127) Exposed to

Exposed to Deaerated Deaerated DI Water at DI Water at 320 320o

  • C for 114 hours

C for 114 hours

  • Contact with Large

Contact with Large Cathodic Cathodic Area Area (Magnetite Film or Noble (Magnetite Film or Noble Metal) Metal) Produces Fine Produces Fine-

  • Grained

Grained Porous Film with Tetrahedral Porous Film with Tetrahedral Crystals on Surface Crystals on Surface

  • Film Growth Rates are Higher

Film Growth Rates are Higher for Porous Oxide Film for Porous Oxide Film

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SLIDE 22

Proposed SAC Initiation Mechanism Proposed SAC Initiation Mechanism – –

Based on Film Growth Results Based on Film Growth Results

  • Initially Thin Dense Magnetite Film is Formed on C

Initially Thin Dense Magnetite Film is Formed on C-

  • Steel Tube

Steel Tube Surfaces Surfaces

  • New Tubes or Acid Cleaned Tubes

New Tubes or Acid Cleaned Tubes

  • If Thin Protective Magnetite Film is Locally Disrupted

If Thin Protective Magnetite Film is Locally Disrupted (Stress Effects) (Stress Effects)

  • Remaining Intact Magnetite on the Tube Will Act as

Remaining Intact Magnetite on the Tube Will Act as Cathodic Cathodic Surface Surface

  • New Oxide Growth in the Damaged Areas may Form Porous Oxide Film

New Oxide Growth in the Damaged Areas may Form Porous Oxide Film

  • Further Damage Accumulation by Disruption or Fracture of Porous

Further Damage Accumulation by Disruption or Fracture of Porous Film Due to Stress Concentration at Notches Developed Film Due to Stress Concentration at Notches Developed

  • SAC Initiation and Growth!!

SAC Initiation and Growth!!

  • Further Tests Going on to Test This Mechanism

Further Tests Going on to Test This Mechanism

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SLIDE 23

Material Characterization Material Characterization

Task 2 Task 2

  • Tubes from Over Ten Boilers Analyzed at

Tubes from Over Ten Boilers Analyzed at GTech GTech and ORNL and ORNL

  • Role of Microstructure on SAC Initiation and Propagation

Role of Microstructure on SAC Initiation and Propagation-

  • Rate

Rate

slide-24
SLIDE 24

Inner Tube Surface Inner Tube Surface Middle of Tube Middle of Tube

Microstructure of Carbon Steel Tubes With SAC Microstructure of Carbon Steel Tubes With SAC

Not Necessary for SAC but may facilitate easier Initiation Not Necessary for SAC but may facilitate easier Initiation

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SLIDE 25

Microhardness Microhardness and Microstructure and Microstructure

Microhardness as Function of Distance from Inner Surface

100 110 120 130 140 150 160 170 180 190 500 1000 1500 2000 2500 3000 3500 4000 Distance from Inner Surface (microns) Microhardness (VHN)

WV5-161 WV-160 WV-160-Little WV7-143 WV4-161

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SLIDE 26

Microstructure of Composite Tubes Removed from Front Microstructure of Composite Tubes Removed from Front Wall Wall (near smelt spouts) (near smelt spouts) of Recovery Boilers

  • f Recovery Boilers

No SAC in these Tubes No SAC in these Tubes

slide-27
SLIDE 27

Evaluation of Stress Effects Evaluation of Stress Effects

Task 3 Task 3

  • Finite Element Modeling

Finite Element Modeling -

  • Effect of

Effect of Attachment Plate on Recovery Boiler Wall Attachment Plate on Recovery Boiler Wall Panel Stresses Panel Stresses – – Gorti

Gorti Sarma Sarma -

  • ORNL

ORNL

  • Stress Measurements on Boiler Tubes

Stress Measurements on Boiler Tubes

  • SSRT Tests in Simulation Autoclave

SSRT Tests in Simulation Autoclave

slide-28
SLIDE 28

Temperature Distribution in the Panel Temperature Distribution in the Panel

  • Uniform heat flux of 0.3 W/mm

Uniform heat flux of 0.3 W/mm2

2 was applied on the fireside of the panel

was applied on the fireside of the panel

  • Tube inside surface was assumed to be in contact with water at 3

Tube inside surface was assumed to be in contact with water at 305 05° °C C

  • Cold side of panel was assumed to be exposed to air at 100

Cold side of panel was assumed to be exposed to air at 100° °C C Attachment Attachment Plate Plate

slide-29
SLIDE 29

Stress Distribution Due to Temperature Differences Stress Distribution Due to Temperature Differences

  • Load due to pressurized water on inside surface of tube was 8.62

Load due to pressurized water on inside surface of tube was 8.62 MPa MPa

  • Residual stress values calculated from 2

Residual stress values calculated from 2-

  • D welding analyses

D welding analyses

  • Stresses due to welding of attachment plate to the wall panel we

Stresses due to welding of attachment plate to the wall panel were not re not included in this initial analyses included in this initial analyses

slide-30
SLIDE 30

Constraint on the Expansion of Panel Due Constraint on the Expansion of Panel Due to Attachment plate to Attachment plate

  • Highly magnified

Highly magnified view of the deformed view of the deformed mesh shows effect of mesh shows effect of attachment plate attachment plate

  • Constraint from

Constraint from attachment plate attachment plate influences the stresses influences the stresses in the tube in the tube

slide-31
SLIDE 31

Attachment Plate Constraint on Deformation of Wall Attachment Plate Constraint on Deformation of Wall Tube Panel Due to Operational Hoop Stresses Tube Panel Due to Operational Hoop Stresses

  • Attachment plate causes changes in stress state in the

Attachment plate causes changes in stress state in the vicinity of the weld, with fairly sharp gradients vicinity of the weld, with fairly sharp gradients

  • Stresses change significantly on either side over a length of 3

Stresses change significantly on either side over a length of 3 elements, which is about 18.3 mm (0.72 in.) elements, which is about 18.3 mm (0.72 in.)

slide-32
SLIDE 32

Hoop Stresses at Inside Surface Under Operating Hoop Stresses at Inside Surface Under Operating Cycles for Panel Tubes without Attachment Plate Cycles for Panel Tubes without Attachment Plate

  • Hoop stress at the inside surface of tube crown on the cold

Hoop stress at the inside surface of tube crown on the cold side becomes slightly tensile during operation, but returns side becomes slightly tensile during operation, but returns to initial value upon shutdown to initial value upon shutdown

slide-33
SLIDE 33

Hoop Stresses at Inside Surface Under Operating Hoop Stresses at Inside Surface Under Operating Cycles for Panel Tubes with Attachment Plate Cycles for Panel Tubes with Attachment Plate

  • Hoop stress at the inside surface of tube at the weld becomes

Hoop stress at the inside surface of tube at the weld becomes slightly tensile at operating temperature, and even more tensile slightly tensile at operating temperature, and even more tensile after shutdown after shutdown

  • Hoop stress remains tensile during subsequent operating cycles

Hoop stress remains tensile during subsequent operating cycles

slide-34
SLIDE 34
  • Identify a Boiler with Known SAC Problem

Identify a Boiler with Known SAC Problem Areas Areas

  • Make installation during outage (prior to

Make installation during outage (prior to restart) restart)

  • $50K budgeted for gages, equipment

$50K budgeted for gages, equipment

  • Collect data every 15

Collect data every 15-

  • 30 seconds for 6

30 seconds for 6+ months months

  • Use data to support finite element model

Use data to support finite element model

  • Attempt post

Attempt post-

  • test evaluation of the

test evaluation of the instrumented areas instrumented areas

  • radiography,

radiography, ultrasonics ultrasonics, , borescope borescope

Stress Measurements on Boiler Tubes Stress Measurements on Boiler Tubes

scallop scallop-

  • type

type attachment weld attachment weld tube crown tube crown

30 30° ° 60 60° °

membrane membrane

Circumferential and longitudinal gages Circumferential and longitudinal gages Circumferential gages only Circumferential gages only

slide-35
SLIDE 35

Future Tasks for FY 05

  • Role of Water Chemistry on Magnetite Film Formation and its

Role of Water Chemistry on Magnetite Film Formation and its Properties Properties

  • X

X-

  • Ray Diffraction, SEM and AFM Analysis of Films to Characterize

Ray Diffraction, SEM and AFM Analysis of Films to Characterize Composition, Morphology, and Mechanical Properties Composition, Morphology, and Mechanical Properties

  • Role of Microstructure on SAC Initiation and Propagation

Role of Microstructure on SAC Initiation and Propagation – – Tests on As Tests on As Received and Heat Treated Steels Received and Heat Treated Steels

  • More Failure Analysis of Tubes Removed from Boilers

More Failure Analysis of Tubes Removed from Boilers

  • Continue FEM Modeling to Calculate Inner Tube Surface Strains At

Continue FEM Modeling to Calculate Inner Tube Surface Strains At Attachment Welds Attachment Welds

  • SSRT Tests to Evaluate Role of Stress on SAC Initiation and

SSRT Tests to Evaluate Role of Stress on SAC Initiation and Propagation Propagation

  • Strain Gages on Boiler Tubes with Attachment to Measure Strains

Strain Gages on Boiler Tubes with Attachment to Measure Strains Experienced During Startup and Shutdown as well as During Operat Experienced During Startup and Shutdown as well as During Operation ion

slide-36
SLIDE 36
slide-37
SLIDE 37

Energy Savings Energy Savings

Impact by the year 2020 ENERGY SAVINGS Electricity Gas Oil Coal Total Energy Savings Vision Industry [billion kWh] [billion ft3] [million barrels] [million tons] [trillion BTU's] Petrochemical 0.13 4.0 0.05 0.04 6.25 Chemical 0.08 2.3 0.025 0.01 5.5 Other Manf. 0.07 2.2 0.025 0.01 5.0 Metal 0.05 1.8 0.02 0.01 2.5 Glass 0.07 2.0 0.02 0.01 3.0 Paper 0.02 0.05 0.002 .003 0.75 Total Savings 0.42 12.4 0.14 0.083 23 Impact by the year 2020 ENERGY SAVINGS Electricity Gas Oil Coal Total Energy Savings Vision Industry [billion kWh] [billion ft3] [million barrels] [million tons] [trillion BTU's] Petrochemical 0.13 4.0 0.05 0.04 6.25 Chemical 0.08 2.3 0.025 0.01 5.5 Other Manf. 0.07 2.2 0.025 0.01 5.0 Metal 0.05 1.8 0.02 0.01 2.5 Glass 0.07 2.0 0.02 0.01 3.0 Paper 0.02 0.05 0.002 .003 0.75 Total Savings 0.42 12.4 0.14 0.083 23

slide-38
SLIDE 38

Energy Impact Energy Impact (in Dollars)

(in Dollars)

Impact by the Year 2020 Energy Cost Savings

Vision Industry Energy Savings [Million $/Year] Petrochemical 48 Chemical 28 Other Manufacturing 25 Metal 12 Glass 15 Paper 5

Total

133

Impact by the Year 2020 Energy Cost Savings

Vision Industry Energy Savings [Million $/Year] Petrochemical 48 Chemical 28 Other Manufacturing 25 Metal 12 Glass 15 Paper 5

Total

133

slide-39
SLIDE 39

Project Status Summary Project Status Summary

Task ID Milestone Planned Completion Actual Completion Comments 1.0 Lab simulation of SAC 1.1 Establish autoclave

  • peration

April 2003 Completed Autoclave and heaters are working satisfactorily 1.2 Develop tensile test rig August 2003 Completed 1.3 Simulate SAC in lab tests

  • Sept. 2004

On-Going 1.4 Oxide growth experiments Sept 2004 On-Going 2.0 Material characterization 2.1 Examine tubes with SAC

  • Sept. 2003

Completed (On- Going) Various tubes were received and were examined at ORNL and IPST 2.2 Document inspection reports

  • Dec. 2003

NA 2.3 Inspections to assess SAC rate

  • Sept. 2004

On-Going 3.0 Evaluation of stress effects 3.1 Document failure reports April 2004 Some data was received and is being

  • reviewed. Required information is missing

in most cases 3.2 Deploy field strain gages

  • Dec. 2004

On-Going 3.3 Model internal stress/strains On-Going 4.0 Environmental effects 4.1 Assess key chemistry data

  • Mar. 2005

On-Going 4.2 Deploy on-line monitoring April 2005 4.3 Document effect of cleaning

  • Sept. 2005

5.0 Communication to US industry Presentations were made at TAPPI and NACE meetings and appropriate Committees attended by US industry reps. 5.1 Technical review meetings Every six months Second meeting will be held in June 2003 Task ID Milestone Planned Completion Actual Completion Comments 1.0 Lab simulation of SAC 1.1 Establish autoclave

  • peration

April 2003 Completed Autoclave and heaters are working satisfactorily 1.2 Develop tensile test rig August 2003 Completed 1.3 Simulate SAC in lab tests

  • Sept. 2004

On-Going 1.4 Oxide growth experiments Sept 2004 On-Going 2.0 Material characterization 2.1 Examine tubes with SAC

  • Sept. 2003

Completed (On- Going) Various tubes were received and were examined at ORNL and IPST 2.2 Document inspection reports

  • Dec. 2003

NA 2.3 Inspections to assess SAC rate

  • Sept. 2004

On-Going 3.0 Evaluation of stress effects 3.1 Document failure reports April 2004 Some data was received and is being

  • reviewed. Required information is missing

in most cases 3.2 Deploy field strain gages

  • Dec. 2004

On-Going 3.3 Model internal stress/strains On-Going 4.0 Environmental effects 4.1 Assess key chemistry data

  • Mar. 2005

On-Going 4.2 Deploy on-line monitoring April 2005 4.3 Document effect of cleaning

  • Sept. 2005

5.0 Communication to US industry Presentations were made at TAPPI and NACE meetings and appropriate Committees attended by US industry reps. 5.1 Technical review meetings Every six months Second meeting will be held in June 2003