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Differences Between API-2000
5th
and 6th
Editions
Brad Otis
April 26, 2010
2010 API Spring Refining and Equipment Standards Meeting
The companies in which Royal Dutch Shell plc directly or indirectly owns investments are separate entities. In this presentation
the expressions "Shell", "Group" and "Shell Group" are sometimes used for convenience where references are made to Group
companies in general. Likewise the words "we", "us" and "our" are also used to refer to Group companies in general or those
who work for them. The expressions are also used where there is no purpose in identifying specific companies.
Shell Global Solutions is a network of independent technology companies in the Shell Group. In this presentation the expression
‘Shell Global Solutions’ is sometimes used for convenience where reference is made to these companies in general, or where
no useful purpose is served by identifying a particular company.
 
The information contained in this presentation contains forward-looking statements, that are subject to risk factors which may
affect the outcome of the matters covered. None of Shell International B.V., any other Shell company and their respective
officers, employees and agents represents the accuracy or completeness of the information set forth in this presentation and
none of the foregoing shall be liable for any loss, cost, expense or damage (whether arising from negligence or otherwise)
relating to the use of such information.
The information contained in this presentation is intended to be general in nature and must not be relied on as specific advice
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Permission should be sought from Shell International B.V. before any part of this presentation is reproduced, stored or
transmitted by any means, electronic or mechanical including by photocopy, recording or information storage and retrieval
system.
 
Agenda
 Recent History
 Significant Differences
o Normal Tank Venting
o Internal Deflagration
o Flame Propagation Through PVVs
o Refrigerated Tank Venting
o Testing of Venting Devices
 Path Forward
Recent History
 API-2000 5th
Edition
o Published April 1998
o Work started on 6th
edition
 ISO - 28300
o New work item submitted in June 2006
o Convert and update API-2000 into ISO Standard
o FDIS 28300 submitted Jan 2008
o Memo highlighting differences issued
o FDIS approved with no negative ballots
 API adopted-back in Dec 09 with no negative ballots
 Now working 2nd
edition of ISO-28300 (API-2000 7th
edition)
Microsoft Office
Word 97 - 2003 Document
Significant Differences
Normal Tank Venting
 EN 14015 Tank Venting
o EN 14015 Tank design standard used in Europe
o Venting model based on theory and validated via test
o Applicable to any tank service, any temperature, and
any size
o Therefore placed in main body of ISO standard
 API-2000 5th
Edition Tank Venting
o Venting model based on theory with simplified
assumptions
o Applicable to hexane or similar services, temperature
< 120 F, and tanks < 180,0000 bbls
o Therefore placed in Annex A of ISO standard
EN-14015 Validation Test
Tests and model calculations at Hoechst in 1980 and 1981
• Tank: V = 617 m3
; D = 8,5 m; H = 10,6 m
• 17 °C ≤ Δ T ≤ 26 °C
• Water (rain) flow density: about 60 kg/m2
h
• TRbF-model calculation
Significant Differences
Normal Tank Venting - continued
 Discussion
o Both methods are acceptable when applied correctly
o Both were included
• To fill gap where Annex A method does not apply
• To allow continued use of the Annex A method
• To ensure global support for the FDIS
o EN-14015 vent loads can be higher than Annex A
• Calculations and comparison courtesy of Protego
(USA) Inc.
Calculation – Examples
Tank 1
Tank:
- Height: 5m
- Diameter: 7m
- Tank volume: 192.4 m3
- Pump in rate: 96 m3/h
- Pump out rate: 96 m3/h
- Vertical tank
- No insulation
- MAWP: 7.5 mbar
- MAWV: 2.5 mbar
Inbreathing Requirements (Total) for Tank 1
Inbreathing requirements Tank 1
0
50
100
150
200
250
300
350
400
API 2000 EN 14015,
North, VP
Hexane
EN 14015,
North, VP>
Hexane
EN 14015, 42-
58, VP Hexane
EN 14015, 42-
58, VP>
Hexane
EN 14015,
South, VP
Hexane
EN 14015,
South, VP>
Hexane
TRbF 20
Ventingrequirements[m3/h]
Pump out Thermal
Outbreathing Requirements (Total) for Tank 1
226
116 117 123 130
118 122
109
Outbreathing requirements Tank 1
0
50
100
150
200
250
API 2000, FP
<37.8C
API 2000, FP
>=37.8C
EN 14015,
North
EN 14015, 42-
58
EN 14015,
South
TRbF 20 TRbF 20-2 TRbF 20-3
Ventingrequirements[m3/h]
Pump in Thermal
H/D = 0.5
H/D = 2
H/D = 0.71
Overview Inbreathing Venting Requirements (thermal)
Small tanks (<3,180 m3)
Comparision Venting Requirements for Thermal Inbreathing
0
200
400
600
800
1000
1200
1400
1600
1800
2000
100 200 500 1000 2000 3180
Tank Volume [m3]
VentingRequirements[m3/h]
API 2000 EN 14015, North, VP Hexane, T<25C EN 14015, North, VP> Hexane, T>= 25C
EN 14015, 42-58, VP Hexane, T<25C EN 14015, 42-58, VP>Hexane, T<25C EN 14015, South, VP Hexane, T< 25C
EN 14015, South, VP>Hexane, T>=25C TRbF 20
Overview Inbreathing Venting Requirements (thermal)
Large tanks (>3,180 m3)
Comparision Venting Requirements for Thermal Inbreathing
0
5000
10000
15000
20000
25000
5000 10000 20000 50000 100000
Tank Volume [m3]
VentingRequirements[m3/h]
API 2000 EN 14015, North, VP Hexane, T<25C EN 14015, North, VP> Hexane, T>= 25C
EN 14015, 42-58, VP Hexane, T<25C EN 14015, 42-58, VP>Hexane, T<25C EN 14015, South, VP Hexane, T< 25C
EN 14015, South, VP>Hexane, T>=25C TRbF 20
Outside scope of API 2000
Overview Outbreathing Venting Requirements (thermal)
Small tanks (<3,180 m3)
Comparision Venting Requirements Outbreathing, Thermal
0
100
200
300
400
500
600
100 200 500 1000 2000 3180
Tank Volume [m3}
VentingRequirements[m3/h]
API, FP<37.8C API, FP>37.8C EN 14015, North EN 14015, 42-58 EN 14015, South TRbF 20
Overview Outbreathing Venting Requirements (thermal)
Large tanks (>3,180 m3)
Comparision Venting Requirements Outbreathing, Thermal
0
2000
4000
6000
8000
10000
12000
5000 10000 20000 50000 100000
Tank Volume [m3}
VentingRequirements[m3/h]
API, FP<37.8C API, FP>37.8C EN 14015, North EN 14015, 42-58 EN 14015, South TRbF 20
Outside scope of API 2000
Significant Differences
Normal Tank Venting - continued
 Discussion
o “Operational experience with petroleum or
petrochemical fluid storage tanks indicates that tank
failures/damage due to vacuum have not been
caused by inadequate venting when that relief
system is designed using the method in this Annex”
o Tanks that meet the criteria in Annex A can have
tank vents designed using the method shown in
Annex A.
o Tanks that don’t meet the Annex A criteria, then the
general method in 4.3.2.1 should be used.
 Questions?
Significant Differences
Internal Deflagration
 New section on tank internal deflagration
 Provides examples on how this may be mitigated
 Previously no “home” for this issue
 Detailed presentation on this on 4/28/10 at API-2000
meeting
 Questions?
Significant Differences
Flame Propagation Through PVV
 The 5th edition states “A flame arrester is not
considered necessary for use in conjunction with a PV
valve venting to atmosphere because flame speeds are
less than vapor velocities across the seats of PV.”
 Recent controlled experiments have shown that flash
back through a PVV is possible during very low
unstable outflow conditions or if there is an external
flammable vapor cloud that ignites with sufficient
overpressure to lift the vacuum pallet.
Significant Differences
Flame Propagation Through PVV - continued
 API-2010 and NFPA-30 have language similar to what
was stated in the 5th edition of API-2000
 Until those standards are updated, there will appear to
be an inconsistency on this issue.
 Questions?
Significant Differences
Refrigerated Tank Venting
 Completely re-written
 Previously was based on hexane
 Borrowed heavily from EN14620 and EN1473
 Questions?
Significant Differences
Testing of Venting Devices
 New section to provide consistency in capacity testing
 Combination of API 2000 5th edition section 4.6 and EN
14015 Annex L.6.
 Questions?
Path Forward
 2nd
Edition of ISO-28300 is being worked now
 Fall 2010 is deadline for submitting new items

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Api 2000 5th vs 6th final

  • 1. Differences Between API-2000 5th and 6th Editions Brad Otis April 26, 2010 2010 API Spring Refining and Equipment Standards Meeting
  • 2. The companies in which Royal Dutch Shell plc directly or indirectly owns investments are separate entities. In this presentation the expressions "Shell", "Group" and "Shell Group" are sometimes used for convenience where references are made to Group companies in general. Likewise the words "we", "us" and "our" are also used to refer to Group companies in general or those who work for them. The expressions are also used where there is no purpose in identifying specific companies. Shell Global Solutions is a network of independent technology companies in the Shell Group. In this presentation the expression ‘Shell Global Solutions’ is sometimes used for convenience where reference is made to these companies in general, or where no useful purpose is served by identifying a particular company.   The information contained in this presentation contains forward-looking statements, that are subject to risk factors which may affect the outcome of the matters covered. None of Shell International B.V., any other Shell company and their respective officers, employees and agents represents the accuracy or completeness of the information set forth in this presentation and none of the foregoing shall be liable for any loss, cost, expense or damage (whether arising from negligence or otherwise) relating to the use of such information. The information contained in this presentation is intended to be general in nature and must not be relied on as specific advice in connection with any decisions you may make. Shell Global Solutions is not liable for any action you may take as a result of you relying on such material or for any loss or damage suffered by you as a result of you taking this action. Furthermore, these materials do not in any way constitute an offer to provide specific services. Some services may not be available in certain countries or political subdivisions thereof. Copyright © 2010 Shell Global Solutions (US) Inc. All copyright and other (intellectual property) rights in all text, images and other information contained in this presentation are the property of Shell International B.V. or other Shell companies. Permission should be sought from Shell International B.V. before any part of this presentation is reproduced, stored or transmitted by any means, electronic or mechanical including by photocopy, recording or information storage and retrieval system.  
  • 3. Agenda  Recent History  Significant Differences o Normal Tank Venting o Internal Deflagration o Flame Propagation Through PVVs o Refrigerated Tank Venting o Testing of Venting Devices  Path Forward
  • 4. Recent History  API-2000 5th Edition o Published April 1998 o Work started on 6th edition  ISO - 28300 o New work item submitted in June 2006 o Convert and update API-2000 into ISO Standard o FDIS 28300 submitted Jan 2008 o Memo highlighting differences issued o FDIS approved with no negative ballots  API adopted-back in Dec 09 with no negative ballots  Now working 2nd edition of ISO-28300 (API-2000 7th edition) Microsoft Office Word 97 - 2003 Document
  • 5. Significant Differences Normal Tank Venting  EN 14015 Tank Venting o EN 14015 Tank design standard used in Europe o Venting model based on theory and validated via test o Applicable to any tank service, any temperature, and any size o Therefore placed in main body of ISO standard  API-2000 5th Edition Tank Venting o Venting model based on theory with simplified assumptions o Applicable to hexane or similar services, temperature < 120 F, and tanks < 180,0000 bbls o Therefore placed in Annex A of ISO standard
  • 6. EN-14015 Validation Test Tests and model calculations at Hoechst in 1980 and 1981 • Tank: V = 617 m3 ; D = 8,5 m; H = 10,6 m • 17 °C ≤ Δ T ≤ 26 °C • Water (rain) flow density: about 60 kg/m2 h • TRbF-model calculation
  • 7. Significant Differences Normal Tank Venting - continued  Discussion o Both methods are acceptable when applied correctly o Both were included • To fill gap where Annex A method does not apply • To allow continued use of the Annex A method • To ensure global support for the FDIS o EN-14015 vent loads can be higher than Annex A • Calculations and comparison courtesy of Protego (USA) Inc.
  • 8. Calculation – Examples Tank 1 Tank: - Height: 5m - Diameter: 7m - Tank volume: 192.4 m3 - Pump in rate: 96 m3/h - Pump out rate: 96 m3/h - Vertical tank - No insulation - MAWP: 7.5 mbar - MAWV: 2.5 mbar
  • 9. Inbreathing Requirements (Total) for Tank 1 Inbreathing requirements Tank 1 0 50 100 150 200 250 300 350 400 API 2000 EN 14015, North, VP Hexane EN 14015, North, VP> Hexane EN 14015, 42- 58, VP Hexane EN 14015, 42- 58, VP> Hexane EN 14015, South, VP Hexane EN 14015, South, VP> Hexane TRbF 20 Ventingrequirements[m3/h] Pump out Thermal
  • 10. Outbreathing Requirements (Total) for Tank 1 226 116 117 123 130 118 122 109 Outbreathing requirements Tank 1 0 50 100 150 200 250 API 2000, FP <37.8C API 2000, FP >=37.8C EN 14015, North EN 14015, 42- 58 EN 14015, South TRbF 20 TRbF 20-2 TRbF 20-3 Ventingrequirements[m3/h] Pump in Thermal H/D = 0.5 H/D = 2 H/D = 0.71
  • 11. Overview Inbreathing Venting Requirements (thermal) Small tanks (<3,180 m3) Comparision Venting Requirements for Thermal Inbreathing 0 200 400 600 800 1000 1200 1400 1600 1800 2000 100 200 500 1000 2000 3180 Tank Volume [m3] VentingRequirements[m3/h] API 2000 EN 14015, North, VP Hexane, T<25C EN 14015, North, VP> Hexane, T>= 25C EN 14015, 42-58, VP Hexane, T<25C EN 14015, 42-58, VP>Hexane, T<25C EN 14015, South, VP Hexane, T< 25C EN 14015, South, VP>Hexane, T>=25C TRbF 20
  • 12. Overview Inbreathing Venting Requirements (thermal) Large tanks (>3,180 m3) Comparision Venting Requirements for Thermal Inbreathing 0 5000 10000 15000 20000 25000 5000 10000 20000 50000 100000 Tank Volume [m3] VentingRequirements[m3/h] API 2000 EN 14015, North, VP Hexane, T<25C EN 14015, North, VP> Hexane, T>= 25C EN 14015, 42-58, VP Hexane, T<25C EN 14015, 42-58, VP>Hexane, T<25C EN 14015, South, VP Hexane, T< 25C EN 14015, South, VP>Hexane, T>=25C TRbF 20 Outside scope of API 2000
  • 13. Overview Outbreathing Venting Requirements (thermal) Small tanks (<3,180 m3) Comparision Venting Requirements Outbreathing, Thermal 0 100 200 300 400 500 600 100 200 500 1000 2000 3180 Tank Volume [m3} VentingRequirements[m3/h] API, FP<37.8C API, FP>37.8C EN 14015, North EN 14015, 42-58 EN 14015, South TRbF 20
  • 14. Overview Outbreathing Venting Requirements (thermal) Large tanks (>3,180 m3) Comparision Venting Requirements Outbreathing, Thermal 0 2000 4000 6000 8000 10000 12000 5000 10000 20000 50000 100000 Tank Volume [m3} VentingRequirements[m3/h] API, FP<37.8C API, FP>37.8C EN 14015, North EN 14015, 42-58 EN 14015, South TRbF 20 Outside scope of API 2000
  • 15. Significant Differences Normal Tank Venting - continued  Discussion o “Operational experience with petroleum or petrochemical fluid storage tanks indicates that tank failures/damage due to vacuum have not been caused by inadequate venting when that relief system is designed using the method in this Annex” o Tanks that meet the criteria in Annex A can have tank vents designed using the method shown in Annex A. o Tanks that don’t meet the Annex A criteria, then the general method in 4.3.2.1 should be used.  Questions?
  • 16. Significant Differences Internal Deflagration  New section on tank internal deflagration  Provides examples on how this may be mitigated  Previously no “home” for this issue  Detailed presentation on this on 4/28/10 at API-2000 meeting  Questions?
  • 17. Significant Differences Flame Propagation Through PVV  The 5th edition states “A flame arrester is not considered necessary for use in conjunction with a PV valve venting to atmosphere because flame speeds are less than vapor velocities across the seats of PV.”  Recent controlled experiments have shown that flash back through a PVV is possible during very low unstable outflow conditions or if there is an external flammable vapor cloud that ignites with sufficient overpressure to lift the vacuum pallet.
  • 18. Significant Differences Flame Propagation Through PVV - continued  API-2010 and NFPA-30 have language similar to what was stated in the 5th edition of API-2000  Until those standards are updated, there will appear to be an inconsistency on this issue.  Questions?
  • 19. Significant Differences Refrigerated Tank Venting  Completely re-written  Previously was based on hexane  Borrowed heavily from EN14620 and EN1473  Questions?
  • 20. Significant Differences Testing of Venting Devices  New section to provide consistency in capacity testing  Combination of API 2000 5th edition section 4.6 and EN 14015 Annex L.6.  Questions?
  • 21. Path Forward  2nd Edition of ISO-28300 is being worked now  Fall 2010 is deadline for submitting new items