dgallup
Automotive
- May 9, 2003
- 4,710
I have a helical compression spring in a natural gas atmosphere. The natural gas will be in compliance with ISO 15403-2 which has rather strict limits on the amount of sulfur:
⎯ Total sulfur 120 mg/m3 (short-term, 150 mg/m3)
⎯ Mercaptan sulfur 6 mg/m3
⎯ Hydrogen sulfide 5 mg/m3 (short-term, 16 mg/m3)
I'm assuming the pressure is ~1 ATM, I don't see it specified anywhere.
We have been using a 316 spring but it's fatigue life has been less than satisfactory. The 17-7PH CH900 spring has doubled the B10 life. However, I'm getting some opinions that it's corrosion resistance will be inferior to the 316 spring. We have had similar parts in the field for 6 years with a 302 spring with zero failures.
I've read NASA MSFC-SPEC-522B and it's replacement MSFC-STD-3029 but they only cover stress corrosion cracking in Sodium Chloride environments. I've read excerpts from MqGuire's book Stainless Steels for Design Engineers which lists 17-7PH in any condition as acceptable for petroleum industry applications. However, I have a copy of NACE MR0175:2003 and can't find any mention of 17-7 or S17700 anywhere in it.
Can someone point me something definitive on corrosion resistance between 304, 316 & 17-7PH CH900 in this kind of relatively mild atmosphere?
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The Help for this program was created in Windows Help format, which depends on a feature that isn't included in this version of Windows.
⎯ Total sulfur 120 mg/m3 (short-term, 150 mg/m3)
⎯ Mercaptan sulfur 6 mg/m3
⎯ Hydrogen sulfide 5 mg/m3 (short-term, 16 mg/m3)
I'm assuming the pressure is ~1 ATM, I don't see it specified anywhere.
We have been using a 316 spring but it's fatigue life has been less than satisfactory. The 17-7PH CH900 spring has doubled the B10 life. However, I'm getting some opinions that it's corrosion resistance will be inferior to the 316 spring. We have had similar parts in the field for 6 years with a 302 spring with zero failures.
I've read NASA MSFC-SPEC-522B and it's replacement MSFC-STD-3029 but they only cover stress corrosion cracking in Sodium Chloride environments. I've read excerpts from MqGuire's book Stainless Steels for Design Engineers which lists 17-7PH in any condition as acceptable for petroleum industry applications. However, I have a copy of NACE MR0175:2003 and can't find any mention of 17-7 or S17700 anywhere in it.
Can someone point me something definitive on corrosion resistance between 304, 316 & 17-7PH CH900 in this kind of relatively mild atmosphere?
----------------------------------------
The Help for this program was created in Windows Help format, which depends on a feature that isn't included in this version of Windows.