mcecasf
Chemical
- Jul 2, 2012
- 20
Hi,
A contractor has installed a section of pipework, control valve, flowmeter and isolation valves in 316 stainless steel (may be 316L not sure). The duty will be saturated brine at ~10-20 degC. It is ~1" line and will see a reasonably constant flow for most of the time but possibility of e.g. 4 days out of 7 no flow (but still flooded).
I'm worried about corrosion and pitting. Is there anything I can do to already installed equipment to reduce the likelihood of damage to the lines? I've already asked them to confirm passivation completed before we put into service, should I insist on pickling first?
I'd rather not have to have it ripped out and replaced at this stage in the game.
A contractor has installed a section of pipework, control valve, flowmeter and isolation valves in 316 stainless steel (may be 316L not sure). The duty will be saturated brine at ~10-20 degC. It is ~1" line and will see a reasonably constant flow for most of the time but possibility of e.g. 4 days out of 7 no flow (but still flooded).
I'm worried about corrosion and pitting. Is there anything I can do to already installed equipment to reduce the likelihood of damage to the lines? I've already asked them to confirm passivation completed before we put into service, should I insist on pickling first?
I'd rather not have to have it ripped out and replaced at this stage in the game.