FPPE
Mechanical
- Mar 4, 2022
- 196
Hi,
I am approaching the world of tanks (I am familiar with pressure vessels, heat exchangers, columns calculated with both ASME and EN and the various API codes, TEMA etc.) and I would like to design a tank with the following characteristics provided by our client:
[ul]
[li]ID: 3400 mm[/li]
[li]Height (straight portion): 5000 mm[/li]
[li]Operating pressure: atm[/li]
[li]Design pressure: full of liquid[/li]
[li]Operating temperature: 96°C[/li]
[li]Design temperature: 110°C[/li]
[li]Material: UNS 32760 (duplex)[/li]
[li]Corrosion allowance: 2 mm[/li]
[li]Code: API 650/API 620[/li]
[li]Fluid: Slurry[/li]
[li]Fluid density: 1387 kg/m3[/li]
[li]Type: vertical cylinder[/li]
[li]Bottom: flat - slightly inclined (approx. 2 deg.)[/li]
[li]Top head: pseudo-ell.[/li]
[li]Fluid density: 1387 kg/m3[/li]
[/ul]
As I am a beginner, I therefore have checked on the forum the threads on which code to use and I started to read the standards, but you know better than me that in the beginning you need to have some reference points, so I would need your help.
From an initial analysis, I have understood that the main differences between API 650 and API 620 are as follows:
[ul]
[li]API 650 covers flat bottom tanks[/li]
[li]API 620 also covers flat as well as other shapes[/li]
[li]API 620 max design temp is 50 degrees F higher than the 200 degrees F of API 650. Appendix M of API 650 goes up to 500 °F (260°C)[/li]
[li]API 620 covers up to 15 psi internal and API 650 up to 2.5 psi (appendix F becomes applicable in case of internal pressure)[/li]
[li]API 650 is for vertical tanks only, API 620 is vert and horizontal[/li]
[li]Typically, API 620 is for very large diameters and for field-assembled tanks, API 650 for welded tanks[/li]
[/ul]
So, I have a few questions:
[ol 1]
[li]In Section 5.6.1.1 of API 650, for diameters < 15 m, the minimum plate thickness must be 5 mm; does this mean corroded or can it be less once corroded?[/li]
[li]Can UNS 32760 be used even if it is not tabulated in Table 5.2a of API 650?[/li]
[li]In case Yes, can I use allowable stresses from ASME II for UNS 32760?[/li]
[li]Am I missing something or is it OK to design this tank with API 650?[/li]
[li]Which standard would you use considering the design data I have listed?[/li]
Thank you in advance
[/ol]
I am approaching the world of tanks (I am familiar with pressure vessels, heat exchangers, columns calculated with both ASME and EN and the various API codes, TEMA etc.) and I would like to design a tank with the following characteristics provided by our client:
[ul]
[li]ID: 3400 mm[/li]
[li]Height (straight portion): 5000 mm[/li]
[li]Operating pressure: atm[/li]
[li]Design pressure: full of liquid[/li]
[li]Operating temperature: 96°C[/li]
[li]Design temperature: 110°C[/li]
[li]Material: UNS 32760 (duplex)[/li]
[li]Corrosion allowance: 2 mm[/li]
[li]Code: API 650/API 620[/li]
[li]Fluid: Slurry[/li]
[li]Fluid density: 1387 kg/m3[/li]
[li]Type: vertical cylinder[/li]
[li]Bottom: flat - slightly inclined (approx. 2 deg.)[/li]
[li]Top head: pseudo-ell.[/li]
[li]Fluid density: 1387 kg/m3[/li]
[/ul]
As I am a beginner, I therefore have checked on the forum the threads on which code to use and I started to read the standards, but you know better than me that in the beginning you need to have some reference points, so I would need your help.
From an initial analysis, I have understood that the main differences between API 650 and API 620 are as follows:
[ul]
[li]API 650 covers flat bottom tanks[/li]
[li]API 620 also covers flat as well as other shapes[/li]
[li]API 620 max design temp is 50 degrees F higher than the 200 degrees F of API 650. Appendix M of API 650 goes up to 500 °F (260°C)[/li]
[li]API 620 covers up to 15 psi internal and API 650 up to 2.5 psi (appendix F becomes applicable in case of internal pressure)[/li]
[li]API 650 is for vertical tanks only, API 620 is vert and horizontal[/li]
[li]Typically, API 620 is for very large diameters and for field-assembled tanks, API 650 for welded tanks[/li]
[/ul]
So, I have a few questions:
[ol 1]
[li]In Section 5.6.1.1 of API 650, for diameters < 15 m, the minimum plate thickness must be 5 mm; does this mean corroded or can it be less once corroded?[/li]
[li]Can UNS 32760 be used even if it is not tabulated in Table 5.2a of API 650?[/li]
[li]In case Yes, can I use allowable stresses from ASME II for UNS 32760?[/li]
[li]Am I missing something or is it OK to design this tank with API 650?[/li]
[li]Which standard would you use considering the design data I have listed?[/li]
Thank you in advance
[/ol]