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Comparison of pressure vessel codes
Why do the codes differ and How do they differ
Presented by: Ray Delaforce
3/24/2011 By Ray Delaforce
03/24/11
By Ray Delaforce
COMPARISON of the various pressure vessel codes
These are the codes we are going to compare:
• ASME Section VIII, Division 1
• ASME Section VIII, Division 2
• PD 5500
• EN 13445 Part 3
But first we look at the most fundamental requirement
What is the ALLOWABLE STRESS ?
This is the primary stress we must not exceedy
A PRIMARY stress results from internal pressure
There are SECONDARY stresses – we do not discuss them
3/24/2011 By Ray Delaforce
03/24/11
By Ray Delaforce
2
COMPARISON of the various pressure vessel codes
We first look at a couple of important material properties
Let us look at the Stress-Strain diagram – we get a lot of information
El ti
Collapse can occur when we reach the yield point
Let us look at the important features of our steel
Elastic
Range
Plastic Range
Fracture
Ductile Range
essσ
Yield Point
Ductile Range
All bl St b t h
Stre
Allowable Stresses about here
3Strain ε0.2% strain
COMPARISON of the various pressure vessel codes
Let us look at the Stress-Strain diagram – we get a lot of information
Consider steel: UTS = 70 000 psi (482 MPa) Yield 38000 psi (262 MPa)
Collapse can occur when we reach the yield point
Let us look at the important features of our steel
There are three important features we must consider
1. There is the limit of proportionality Yield Point 0.2% strain
2. The Ultimate Tensile Strength (UTS) When fracture occurs
3. The Ductility = Yield / UTS Must be less than 1.0
There is a 4th one – Creep which occurs at higher temperatures
4
COMPARISON of the various pressure vessel codes
Allowable stress is base on these characteristics of the metal
ASME Section VIII Division 1
ASME Section VIII Division 2
S = smaller of: UTS / 3.5 or Yield / 1.5 = 20 000 psi (138 MPa)
ASME Section VIII Division 2
EN 13445
Sm = smaller of: UTS / 2.4 or Yield / 1.5
Both based on PED European requirements
= 25 300 psi (174 MPa)
EN 13445
f = smaller of: UTS / 2.4 or Yield / 1.5
Both based on PED European requirements
= 25 300 psi (174 MPa)
PD 5500
f = smaller of: UTS / 2.35 or Yield / 1.5 = 25 300 psi (174 MPa)
5
We consider Carbon Steel for simplicity
COMPARISON of the various pressure vessel codes
We look at this on the Stress Strain diagram
ASME VIII, Division 1 has a larger safety margin – safer
This code is still the favoured code throughout the World
essσ
Yield Point
ASME VIII Di i i 1
ASME VIII Division 2, EN 13445 & PD 5500
Stre
ASME VIII Division 1
Strain ε 6
COMPARISON of the various pressure vessel codes
Let us now look at a typical calculation – the cylindrical shell
Here are the basic dimensions We shall ignore joint efficiency E (z)
W d th l l ti f th li d
P = 300 psi (207 MPa)
D = 60 ins (1 524 mm)
We now do the calculation for the cylinder:
t = 0.454 in (11.534 mm)
By ASME VIII Division 1
S(f) = 20 000 psi (174 MPa)
By ASME VIII Division 2
t = 0.453 in (11.516 mm)t 0.453 in (11.516 mm)
By EN 13445
DO Di
7
t ASME e EN 13445 & PD5500
COMPARISON of the various pressure vessel codes
Let us now look at a typical calculation – the cylindrical shell
Here are the basic dimensions We shall ignore joint efficiency E
W d th l l ti f th li d
Let us now look at a typical calculation – the Elliptical Head
P = 300 psi (207 MPa)
D = 60 ins (1 524 mm)
We now do the calculation for the cylinder:
t = 0.454 in (11.534 mm)
By ASME VIII Division 1
S(f) = 20 000 psi (174 MPa)
By ASME VIII Division 2
t = 0.453 in (11.516 mm)t 0.453 in (11.516 mm)
By EN 13445
t 0 453 i (11 516 )
That is why the differences
are so small – the formulae
are nearly the same !
t = 0.453 in (11.516 mm)
By PD 5500
t = 0 453 in (11 516 mm)
This formula looks odd,
but is actually just about
8
t = 0.453 in (11.516 mm)the same as the others
COMPARISON of the various pressure vessel codes
Let us now look at a typical calculation – the cylindrical shell
Here are the basic dimensions We shall ignore joint efficiency E
W d th l l ti f th li d
Let us now look at a typical calculation – the Elliptical Head
We now do the calculation for the cylinder:
t = 0.454 in (11.534 mm)
By ASME VIII Division 1
Cylinder based on the
By ASME VIII Division 2
t = 0.453 in (11.516 mm)
Cylinder based on the
equilibrium equation
t 0.453 in (11.516 mm)
By EN 13445
t 0 453 i (11 516 )
That is why the differences
are so small – the formulae
are nearly the same !
t = 0.453 in (11.516 mm)
By PD 5500
t = 0 453 in (11 516 mm)
This formula looks odd,
but is actually just about
9
t = 0.453 in (11.516 mm)the same as the others
COMPARISON of the various pressure vessel codes
Let us now look at a typical calculation – the Elliptical Head
Minor Shape is based on true ellipse
Major
h
D/2h = 2
P = 300 psi (207 MPa)
D 60 i (1 524 )
D ASME Division 1 – simple calculationASME Division 2 – complicated calc.
D = 60 ins (1 524 mm)
S(f) = 20 000 psi (138 MPa)
t = 0.451 in t = 11.447 mm
Head formula almost identical to the cylinder formula:Head formula almost identical to the cylinder formula:
Elliptical head:Cylinder:
10
COMPARISON of the various pressure vessel codes
Let us now look at a typical calculation – the Elliptical Head
Minor Shape is based on true ellipse
Major
h
D/2h = 2
P = 300 psi (207 MPa)
D 60 i (1 524 )
D ASME Division 2 – complicated calc.
1 There are many steps to do
D = 60 ins (1 524 mm)
S(f) = 25 300 psi (174 MPa)
2 Cannot calculate t directly . .
. only P
Division 2 allows higher stress
On the next slide we show the calculation per PV Elite
Division 2 allows higher stress
11
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite - ASME Division 2
The Elliptical head is transformed in equivalent Torispherical Head
12
Crown radius
Knuckle radius
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite - ASME Division 2
Next we must calculate some geometry factors
13
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite - ASME Division 2
Even more geometry and other factors………Even more geometry and other factors and more – lots of factors
14
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite - ASME Division 2
Even more geometry and other factors and more – lots of factors
Finally we end up with our starting pressure
15
PV Elite does an iterative calculation to end up with the pressure
Finally we end up with our starting pressure
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite - ASME Division 2
We had to start the calculate with a ‘guess’ thickness t
And we ended up with our starting pressure
We have to use a computer to do this calculation !
The computed thickness is t = 0.3219 in t = 8.1767 mm
16
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite - ASME Division 2
EN 13445 has a similar method – slightly less complicated than ASME
The final computed thickness is: t = 0.3886 in t = 9.8619 mm
17
COMPARISON of the various pressure vessel codes
The method of computing the head by PD 5500 is very different
Minor 1 Calculate h / D = 0.25
Major
h 2 Calculate P / f = 0.119
P = 300 psi (207 MPa)
D 60 i (1 524 )
D
D = 60 ins (1 524 mm)
f = 25 300 psi (174 MPa)
PD 5500 uses a graphical solutions – like this
18
COMPARISON of the various pressure vessel codes
Here is the Graph used to compute this head thickness
1 Calculate h / D = 0.25
2 Calculate P / f = 0.119
e / D
e = D x (e/D)
19
COMPARISON of the various pressure vessel codes
This is the calculation using PV Elite
t = 0.3792 in t = 9.6317 mm
Each code has its own way of computing a head – and other parts
But, where do codes ‘borrow’ procedures from other codes ?
20
COMPARISON of the various pressure vessel codes
Codes ‘Copy’ codes – some examples Flange analysis
ASME Division 1
ASME Division 2 EN 13445-3 PD 5500
21
COMPARISON of the various pressure vessel codes
Codes ‘Copy’ codes – some examples Access openings in skirt
AD Merblatter (AD 2000)
EN 13445-3
22
COMPARISON of the various pressure vessel codes
Codes ‘Copy’ codes – some examples Pressure – Area method
PD 5500PD 5500
ASME Division 1 ASME Division 2 EN 13445-3
E h f th d h difi d th th d i i l
23
Each of the codes has modified the method – same principle
COMPARISON of the various pressure vessel codes
We have looked at various codes of construction
We have learned some important issues
1. ASME VIII Division 1 requires thicker metal – high
safety factor
2 Th th d di d thi t l b t2. The other codes we discussed use thinner metal, but
the allowable stresses are nearer the yield point – less
safety
3 S d i th d h b ‘b d’3. Some procedure in the codes have been ‘borrowed’
from other codes
4. ASME VIII Division 2 and EN 13445 are based on the
PED (European Pressure Equipment Directive)PED (European Pressure Equipment Directive)
24
It is hoped you got some value out of this webinar

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Comparison of Various Pressure Vessel Codes

  • 1. Comparison of pressure vessel codes Why do the codes differ and How do they differ Presented by: Ray Delaforce 3/24/2011 By Ray Delaforce 03/24/11 By Ray Delaforce
  • 2. COMPARISON of the various pressure vessel codes These are the codes we are going to compare: • ASME Section VIII, Division 1 • ASME Section VIII, Division 2 • PD 5500 • EN 13445 Part 3 But first we look at the most fundamental requirement What is the ALLOWABLE STRESS ? This is the primary stress we must not exceedy A PRIMARY stress results from internal pressure There are SECONDARY stresses – we do not discuss them 3/24/2011 By Ray Delaforce 03/24/11 By Ray Delaforce 2
  • 3. COMPARISON of the various pressure vessel codes We first look at a couple of important material properties Let us look at the Stress-Strain diagram – we get a lot of information El ti Collapse can occur when we reach the yield point Let us look at the important features of our steel Elastic Range Plastic Range Fracture Ductile Range essσ Yield Point Ductile Range All bl St b t h Stre Allowable Stresses about here 3Strain ε0.2% strain
  • 4. COMPARISON of the various pressure vessel codes Let us look at the Stress-Strain diagram – we get a lot of information Consider steel: UTS = 70 000 psi (482 MPa) Yield 38000 psi (262 MPa) Collapse can occur when we reach the yield point Let us look at the important features of our steel There are three important features we must consider 1. There is the limit of proportionality Yield Point 0.2% strain 2. The Ultimate Tensile Strength (UTS) When fracture occurs 3. The Ductility = Yield / UTS Must be less than 1.0 There is a 4th one – Creep which occurs at higher temperatures 4
  • 5. COMPARISON of the various pressure vessel codes Allowable stress is base on these characteristics of the metal ASME Section VIII Division 1 ASME Section VIII Division 2 S = smaller of: UTS / 3.5 or Yield / 1.5 = 20 000 psi (138 MPa) ASME Section VIII Division 2 EN 13445 Sm = smaller of: UTS / 2.4 or Yield / 1.5 Both based on PED European requirements = 25 300 psi (174 MPa) EN 13445 f = smaller of: UTS / 2.4 or Yield / 1.5 Both based on PED European requirements = 25 300 psi (174 MPa) PD 5500 f = smaller of: UTS / 2.35 or Yield / 1.5 = 25 300 psi (174 MPa) 5 We consider Carbon Steel for simplicity
  • 6. COMPARISON of the various pressure vessel codes We look at this on the Stress Strain diagram ASME VIII, Division 1 has a larger safety margin – safer This code is still the favoured code throughout the World essσ Yield Point ASME VIII Di i i 1 ASME VIII Division 2, EN 13445 & PD 5500 Stre ASME VIII Division 1 Strain ε 6
  • 7. COMPARISON of the various pressure vessel codes Let us now look at a typical calculation – the cylindrical shell Here are the basic dimensions We shall ignore joint efficiency E (z) W d th l l ti f th li d P = 300 psi (207 MPa) D = 60 ins (1 524 mm) We now do the calculation for the cylinder: t = 0.454 in (11.534 mm) By ASME VIII Division 1 S(f) = 20 000 psi (174 MPa) By ASME VIII Division 2 t = 0.453 in (11.516 mm)t 0.453 in (11.516 mm) By EN 13445 DO Di 7 t ASME e EN 13445 & PD5500
  • 8. COMPARISON of the various pressure vessel codes Let us now look at a typical calculation – the cylindrical shell Here are the basic dimensions We shall ignore joint efficiency E W d th l l ti f th li d Let us now look at a typical calculation – the Elliptical Head P = 300 psi (207 MPa) D = 60 ins (1 524 mm) We now do the calculation for the cylinder: t = 0.454 in (11.534 mm) By ASME VIII Division 1 S(f) = 20 000 psi (174 MPa) By ASME VIII Division 2 t = 0.453 in (11.516 mm)t 0.453 in (11.516 mm) By EN 13445 t 0 453 i (11 516 ) That is why the differences are so small – the formulae are nearly the same ! t = 0.453 in (11.516 mm) By PD 5500 t = 0 453 in (11 516 mm) This formula looks odd, but is actually just about 8 t = 0.453 in (11.516 mm)the same as the others
  • 9. COMPARISON of the various pressure vessel codes Let us now look at a typical calculation – the cylindrical shell Here are the basic dimensions We shall ignore joint efficiency E W d th l l ti f th li d Let us now look at a typical calculation – the Elliptical Head We now do the calculation for the cylinder: t = 0.454 in (11.534 mm) By ASME VIII Division 1 Cylinder based on the By ASME VIII Division 2 t = 0.453 in (11.516 mm) Cylinder based on the equilibrium equation t 0.453 in (11.516 mm) By EN 13445 t 0 453 i (11 516 ) That is why the differences are so small – the formulae are nearly the same ! t = 0.453 in (11.516 mm) By PD 5500 t = 0 453 in (11 516 mm) This formula looks odd, but is actually just about 9 t = 0.453 in (11.516 mm)the same as the others
  • 10. COMPARISON of the various pressure vessel codes Let us now look at a typical calculation – the Elliptical Head Minor Shape is based on true ellipse Major h D/2h = 2 P = 300 psi (207 MPa) D 60 i (1 524 ) D ASME Division 1 – simple calculationASME Division 2 – complicated calc. D = 60 ins (1 524 mm) S(f) = 20 000 psi (138 MPa) t = 0.451 in t = 11.447 mm Head formula almost identical to the cylinder formula:Head formula almost identical to the cylinder formula: Elliptical head:Cylinder: 10
  • 11. COMPARISON of the various pressure vessel codes Let us now look at a typical calculation – the Elliptical Head Minor Shape is based on true ellipse Major h D/2h = 2 P = 300 psi (207 MPa) D 60 i (1 524 ) D ASME Division 2 – complicated calc. 1 There are many steps to do D = 60 ins (1 524 mm) S(f) = 25 300 psi (174 MPa) 2 Cannot calculate t directly . . . only P Division 2 allows higher stress On the next slide we show the calculation per PV Elite Division 2 allows higher stress 11
  • 12. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite - ASME Division 2 The Elliptical head is transformed in equivalent Torispherical Head 12 Crown radius Knuckle radius
  • 13. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite - ASME Division 2 Next we must calculate some geometry factors 13
  • 14. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite - ASME Division 2 Even more geometry and other factors………Even more geometry and other factors and more – lots of factors 14
  • 15. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite - ASME Division 2 Even more geometry and other factors and more – lots of factors Finally we end up with our starting pressure 15 PV Elite does an iterative calculation to end up with the pressure Finally we end up with our starting pressure
  • 16. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite - ASME Division 2 We had to start the calculate with a ‘guess’ thickness t And we ended up with our starting pressure We have to use a computer to do this calculation ! The computed thickness is t = 0.3219 in t = 8.1767 mm 16
  • 17. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite - ASME Division 2 EN 13445 has a similar method – slightly less complicated than ASME The final computed thickness is: t = 0.3886 in t = 9.8619 mm 17
  • 18. COMPARISON of the various pressure vessel codes The method of computing the head by PD 5500 is very different Minor 1 Calculate h / D = 0.25 Major h 2 Calculate P / f = 0.119 P = 300 psi (207 MPa) D 60 i (1 524 ) D D = 60 ins (1 524 mm) f = 25 300 psi (174 MPa) PD 5500 uses a graphical solutions – like this 18
  • 19. COMPARISON of the various pressure vessel codes Here is the Graph used to compute this head thickness 1 Calculate h / D = 0.25 2 Calculate P / f = 0.119 e / D e = D x (e/D) 19
  • 20. COMPARISON of the various pressure vessel codes This is the calculation using PV Elite t = 0.3792 in t = 9.6317 mm Each code has its own way of computing a head – and other parts But, where do codes ‘borrow’ procedures from other codes ? 20
  • 21. COMPARISON of the various pressure vessel codes Codes ‘Copy’ codes – some examples Flange analysis ASME Division 1 ASME Division 2 EN 13445-3 PD 5500 21
  • 22. COMPARISON of the various pressure vessel codes Codes ‘Copy’ codes – some examples Access openings in skirt AD Merblatter (AD 2000) EN 13445-3 22
  • 23. COMPARISON of the various pressure vessel codes Codes ‘Copy’ codes – some examples Pressure – Area method PD 5500PD 5500 ASME Division 1 ASME Division 2 EN 13445-3 E h f th d h difi d th th d i i l 23 Each of the codes has modified the method – same principle
  • 24. COMPARISON of the various pressure vessel codes We have looked at various codes of construction We have learned some important issues 1. ASME VIII Division 1 requires thicker metal – high safety factor 2 Th th d di d thi t l b t2. The other codes we discussed use thinner metal, but the allowable stresses are nearer the yield point – less safety 3 S d i th d h b ‘b d’3. Some procedure in the codes have been ‘borrowed’ from other codes 4. ASME VIII Division 2 and EN 13445 are based on the PED (European Pressure Equipment Directive)PED (European Pressure Equipment Directive) 24 It is hoped you got some value out of this webinar