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Reformer Tube Life Assessment
All rights reserved to thepetrostreet.com
Prepared by: Eitzaz Hussain
ContentsContents
Primary reformer introduction
F‐2501 history
Tube design parameters
Tube damage & assessment
Methods of tube life assessment
Scope of LM Method
Larson‐Miller Method
An example of LM‐Method
Uncertainties in LM‐Method
Limitations of LM‐Method
all rights reserved to thePetroStreet team
Primary ReformerPrimary Reformer
Primary reformers are used to convert a “process gas”
mixture of hydro carbons & steam into hydrogen‐rich gases
which can be used in the manufacture of ammonia. The
process gas is passed under pressure through vertical tubes
filled with catalyst and, since high temperature(900‐950 OC)
is required to maintain the required chemical reaction, the
outside of the tubes are heated by burners in a largey g
furnace.
H O + CH CO + 4HH2O + CH4 CO2 + 4H2
all rights reserved to thePetroStreet team
F‐2501(History)F 2501(History)
• Foster Wheeler designed Terrace type
• Operated 19 years(1967‐1986) in Pascagoula (USA)
• Mothballed for 5 years(1986‐1991)
• Reconstructed with new radiant tubes, arch roof sealing, roof 
& wall refractory outlet pigtails and header (incoloy 800H)& wall refractory, outlet pigtails and header (incoloy 800H)
all rights reserved to thePetroStreet team
Tube Design ParametersTube Design Parameters
• Design pressure • Quantity 392g p
500 psig
• Design temperature
Q y
• Material Abex TX‐63
• O.D 4.7 inch
1780 0F
• Theoretical design life
• I.D 3.7 inch
• Length 42 ft
100,000 hours • MSW 0.465 inch
all rights reserved to thePetroStreet team
Tube Damages & AssessmentTube Damages & Assessment 
Damages Damage assessmentg
• Creep damage
• Thermal cycling /shock
g
• Ultra sonic technique
• Eddy current testing
• External oxidation
• Internal carburization
• Radiography
• Dye penetrant test
( )• Leak test (soap solution)
• Thermography
• Refractory inspection• Refractory inspection
all rights reserved to thePetroStreet team
Methods of Life AssessmentMethods of Life Assessment
1. Destructive stress rupture testing
2 Larson Miller Equation (Paper study)2. Larson‐Miller Equation (Paper study)
all rights reserved to thePetroStreet team
Scope of LM MethodScope of LM Method
1. Estimation of tube life at given temperature, pressure, 
corrosion rate ??corrosion rate ??
2. Estimation of temperature for  specified life at given pressure 
& corrosion rate??
3. Operating pressure & TMT reduction for the extended tube 
life??
all rights reserved to thePetroStreet team
Larson‐Miller MethodLarson Miller Method
• Tabulation of required data
• Calculation of average stress• Calculation of average stress
• Evaluation of Larson‐Miller parameter & constant
• Rupture time calculationRupture time calculation
• Remaining tube life
all rights reserved to thePetroStreet team
Required DataRequired Data
• Tube material
• Tube metal temperature (TMT)• Tube metal temperature (TMT)
• Operating gauge pressure (P)
• Tube O.D (D0 )Tube O.D (D0 )
• Initial minimum tube thickness(δ)
all rights reserved to thePetroStreet team
Average Stress CalculationAverage Stress Calculation
Mean diameter equation
Ϭ beginning=P/2{(D0/δ beginning) ‐1}
Ϭ end=P/2{(D0/δ end) ‐1}
Ϭ =(Ϭ +Ϭ )/2Ϭ AVG    =(Ϭ beginning +Ϭ end)/2
Ϭ=Stress
P=Pressure
δ=Thickness
all rights reserved to thePetroStreet team
Larson‐Miller ParameterLarson Miller Parameter
Larson Miller Parameter Curves
(LM values are taken against average stress from curves )
(S.I units)
LMP= (T+273)(C +log t )x10‐3LMP= (T+273)(CLM +log tr)x10 3
(US customary units)(US customary units) 
LMP= (T+460)(CLM +log tr)x10‐3
LMP=Larson Miller Parameter
CLM = Larson Miller Constant
t r = Rupture Timer p
all rights reserved to thePetroStreet team
LM PARAMETER
all rights reserved to thePetroStreet team
Graph GuideGraph Guide
1. Specified minimum tensile strength
2. Tensile strengthg
3. Specified minimum yield strength
4. Yield strength
5. Elastic allowable stress
6 Rupture allowable stress6. Rupture allowable stress
7. Limiting design metal temperature
8. Minimum rupture strength
9. Average rupture strength
10. Elastic design governs above this stress
Graph----Stress curves (SI units) for ASTM A 213, ASTM A 271,
ASTM A 312 and ASTM A 376 types 347 and 347 H(18 Cr-10 Ni-ASTM A 312 and ASTM A 376 types 347 and 347 H(18 Cr 10 Ni
Nb)stainless steel
all rights reserved to thePetroStreet team
Rupture Timep
• Calculated from LM parameters
• Minimum strength rupture timeMinimum strength rupture time
• Average strength rupture time
t r(avg) > t r(min)
all rights reserved to thePetroStreet team
Remaining Tube LifeRemaining Tube Life
• Life fraction = operating period ÷ rupture time
• Life accumulated = Ʃ life fractions• Life accumulated = Ʃ life fractions
• Remaining fraction = 1 - (Ʃ life fractions)
• Remaining tube life = Remaining fraction x rupture lifeRemaining tube life Remaining fraction x rupture life
all rights reserved to thePetroStreet team
An Example
all rights reserved to thePetroStreet team
Uncertainties in LM MethodUncertainties in LM Method
• Tube damage
(uncertain TMT Operating pressure Corrosion rate etc )(uncertain TMT, Operating pressure, Corrosion rate etc.)
• Actual rupture strength is no precise
• Tube damage rule {t r =t r (Ϭ,T)}Tube damage rule {t r t r (Ϭ,T)}
(it asserts that creep rupture will occur when the life
fraction totals unity)
all rights reserved to thePetroStreet team
Limitations of LM MethodLimitations of LM Method
• Apply to thin tubes
N id ti f hiti ti b i ti• No consideration for graphitization, carburization,
oxidation & hydrogen attack
• Apply to seamless tubesApply to seamless tubes
all rights reserved to thePetroStreet team
For more details & information, please contact
us.
thePetroStreet Team
www.thepetrostreet.com
support@thepetrostreet.com

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Reformer tube life_assessment_thepetrostreet

  • 1. Reformer Tube Life Assessment All rights reserved to thepetrostreet.com Prepared by: Eitzaz Hussain
  • 3. Primary ReformerPrimary Reformer Primary reformers are used to convert a “process gas” mixture of hydro carbons & steam into hydrogen‐rich gases which can be used in the manufacture of ammonia. The process gas is passed under pressure through vertical tubes filled with catalyst and, since high temperature(900‐950 OC) is required to maintain the required chemical reaction, the outside of the tubes are heated by burners in a largey g furnace. H O + CH CO + 4HH2O + CH4 CO2 + 4H2 all rights reserved to thePetroStreet team
  • 4. F‐2501(History)F 2501(History) • Foster Wheeler designed Terrace type • Operated 19 years(1967‐1986) in Pascagoula (USA) • Mothballed for 5 years(1986‐1991) • Reconstructed with new radiant tubes, arch roof sealing, roof  & wall refractory outlet pigtails and header (incoloy 800H)& wall refractory, outlet pigtails and header (incoloy 800H) all rights reserved to thePetroStreet team
  • 5. Tube Design ParametersTube Design Parameters • Design pressure • Quantity 392g p 500 psig • Design temperature Q y • Material Abex TX‐63 • O.D 4.7 inch 1780 0F • Theoretical design life • I.D 3.7 inch • Length 42 ft 100,000 hours • MSW 0.465 inch all rights reserved to thePetroStreet team
  • 6. Tube Damages & AssessmentTube Damages & Assessment  Damages Damage assessmentg • Creep damage • Thermal cycling /shock g • Ultra sonic technique • Eddy current testing • External oxidation • Internal carburization • Radiography • Dye penetrant test ( )• Leak test (soap solution) • Thermography • Refractory inspection• Refractory inspection all rights reserved to thePetroStreet team
  • 7. Methods of Life AssessmentMethods of Life Assessment 1. Destructive stress rupture testing 2 Larson Miller Equation (Paper study)2. Larson‐Miller Equation (Paper study) all rights reserved to thePetroStreet team
  • 8. Scope of LM MethodScope of LM Method 1. Estimation of tube life at given temperature, pressure,  corrosion rate ??corrosion rate ?? 2. Estimation of temperature for  specified life at given pressure  & corrosion rate?? 3. Operating pressure & TMT reduction for the extended tube  life?? all rights reserved to thePetroStreet team
  • 9. Larson‐Miller MethodLarson Miller Method • Tabulation of required data • Calculation of average stress• Calculation of average stress • Evaluation of Larson‐Miller parameter & constant • Rupture time calculationRupture time calculation • Remaining tube life all rights reserved to thePetroStreet team
  • 10. Required DataRequired Data • Tube material • Tube metal temperature (TMT)• Tube metal temperature (TMT) • Operating gauge pressure (P) • Tube O.D (D0 )Tube O.D (D0 ) • Initial minimum tube thickness(δ) all rights reserved to thePetroStreet team
  • 11. Average Stress CalculationAverage Stress Calculation Mean diameter equation Ϭ beginning=P/2{(D0/δ beginning) ‐1} Ϭ end=P/2{(D0/δ end) ‐1} Ϭ =(Ϭ +Ϭ )/2Ϭ AVG    =(Ϭ beginning +Ϭ end)/2 Ϭ=Stress P=Pressure δ=Thickness all rights reserved to thePetroStreet team
  • 12. Larson‐Miller ParameterLarson Miller Parameter Larson Miller Parameter Curves (LM values are taken against average stress from curves ) (S.I units) LMP= (T+273)(C +log t )x10‐3LMP= (T+273)(CLM +log tr)x10 3 (US customary units)(US customary units)  LMP= (T+460)(CLM +log tr)x10‐3 LMP=Larson Miller Parameter CLM = Larson Miller Constant t r = Rupture Timer p all rights reserved to thePetroStreet team
  • 13. LM PARAMETER all rights reserved to thePetroStreet team
  • 14. Graph GuideGraph Guide 1. Specified minimum tensile strength 2. Tensile strengthg 3. Specified minimum yield strength 4. Yield strength 5. Elastic allowable stress 6 Rupture allowable stress6. Rupture allowable stress 7. Limiting design metal temperature 8. Minimum rupture strength 9. Average rupture strength 10. Elastic design governs above this stress Graph----Stress curves (SI units) for ASTM A 213, ASTM A 271, ASTM A 312 and ASTM A 376 types 347 and 347 H(18 Cr-10 Ni-ASTM A 312 and ASTM A 376 types 347 and 347 H(18 Cr 10 Ni Nb)stainless steel all rights reserved to thePetroStreet team
  • 15. Rupture Timep • Calculated from LM parameters • Minimum strength rupture timeMinimum strength rupture time • Average strength rupture time t r(avg) > t r(min) all rights reserved to thePetroStreet team
  • 16. Remaining Tube LifeRemaining Tube Life • Life fraction = operating period ÷ rupture time • Life accumulated = Ʃ life fractions• Life accumulated = Ʃ life fractions • Remaining fraction = 1 - (Ʃ life fractions) • Remaining tube life = Remaining fraction x rupture lifeRemaining tube life Remaining fraction x rupture life all rights reserved to thePetroStreet team
  • 17. An Example all rights reserved to thePetroStreet team
  • 18. Uncertainties in LM MethodUncertainties in LM Method • Tube damage (uncertain TMT Operating pressure Corrosion rate etc )(uncertain TMT, Operating pressure, Corrosion rate etc.) • Actual rupture strength is no precise • Tube damage rule {t r =t r (Ϭ,T)}Tube damage rule {t r t r (Ϭ,T)} (it asserts that creep rupture will occur when the life fraction totals unity) all rights reserved to thePetroStreet team
  • 19. Limitations of LM MethodLimitations of LM Method • Apply to thin tubes N id ti f hiti ti b i ti• No consideration for graphitization, carburization, oxidation & hydrogen attack • Apply to seamless tubesApply to seamless tubes all rights reserved to thePetroStreet team
  • 20. For more details & information, please contact us. thePetroStreet Team www.thepetrostreet.com support@thepetrostreet.com