Viswa KN
Petroleum
- Jan 24, 2017
- 3
Hello All,
By reviewing the SHELL DEP 30.10.02.15(the MATERIALS FOR USE IN H2S-CONTAINING ENVIRONMENTS IN OIL AND GAS PRODUCTION
(AMENDMENTS AND SUPPLEMENTS TO ISO 15156:2009amendment for ISO 15156) noticed that more environmental restrictions are imposed.On Table A.2 its mentioned that UNS 20910(Nitronic 50) the max allowed temperature is only 66 degC and the allowed H2S partial pressure is 100 kpa.
The allowed temperature is much lower to SS316L(149 degC).Actually the UNS 20910 is better MOC and harder than SS316L.
Moreover for valves its mostly used as Shaft/stem.In ISO 15156 there is a Table A.3 for shaft,stem and pin and it allows UNS 20910 without any restriction.
How these two valid standards be so contrary.Moreover presume that temperature mentioned as Max is only the operating and not the design condition.Please clarify.
By reviewing the SHELL DEP 30.10.02.15(the MATERIALS FOR USE IN H2S-CONTAINING ENVIRONMENTS IN OIL AND GAS PRODUCTION
(AMENDMENTS AND SUPPLEMENTS TO ISO 15156:2009amendment for ISO 15156) noticed that more environmental restrictions are imposed.On Table A.2 its mentioned that UNS 20910(Nitronic 50) the max allowed temperature is only 66 degC and the allowed H2S partial pressure is 100 kpa.
The allowed temperature is much lower to SS316L(149 degC).Actually the UNS 20910 is better MOC and harder than SS316L.
Moreover for valves its mostly used as Shaft/stem.In ISO 15156 there is a Table A.3 for shaft,stem and pin and it allows UNS 20910 without any restriction.
How these two valid standards be so contrary.Moreover presume that temperature mentioned as Max is only the operating and not the design condition.Please clarify.