Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations waross on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Material for 10000 PPM Chlorides 2

Status
Not open for further replies.

nickypaliwal

Materials
Aug 28, 2014
199
Which material can be used for the piping and the pump for above chloride content. Chlorides of 10,000 PPM.

Operating Temp: 45 deg C.

Also recommend material for even higher chlorides say Sea Water.

 
Replies continue below

Recommended for you

At what pH? near neutral?

Cost wise the first choice would be non-metallic, either solid plastic or fiberglass.
That is if the temp and pressure allow it.

If you want to go metal you really are looking at alloys suitable for seawater service.
The Cl level is not the major factor, Temp and pH are more important.
Alloys such as 6% Mo superaustenitics (AL-6XN, 25-6Mo, 1925hMo), or for thin wall tubing a superferritic (Sea-Cure or AL-294C), or a superduplex (255, 2507) all have proven service in these conditions.

= = = = = = = = = = = = = = = = = = = =
Plymouth Tube
 
Thanks for your response ... Our client does not agree with Superduplex without any reference.. Is there any standard document available for the same... Also for the other suggestions of 6% Mo, can you please advise any document... NI-AL Bronze is Ok but we can not find suitable (approved) suppliers so is not an option...
 
There is a ton of data in NACE or North Sea specs about using these alloys.
The 6% Mo alloys have been in use in seawater for 30 years, they are considered legacy materials.
Look at the ATI reference

I wouldn't touch NAB for piping (pumps and valves maybe, but it needs low velocity), maybe 70/30 Cu/Ni as another option, but much lower strength than SS and it has its own corrosion issues.

= = = = = = = = = = = = = = = = = = = =
Plymouth Tube
 
Unless this is for extremely high pressures, why on earth wouldn't you use a non-metallic? I'd prefer corrosion immunity to corrosion resistance any day of the week.
 
At 45C and perhaps with chlorination non-metallics will not be free from long term environmental degradation.
But that said they would be my first choice also.
Unless heat transfer is involved (like in a heat exchanger) they are often a much more economical option.
One reason is that people often are reluctant to spend the money on the correct alloy so they try to cut the corrosion resistance close. This results in serious ongoing corrosion issues and high maintenance costs.

= = = = = = = = = = = = = = = = = = = =
Plymouth Tube
 
Although I don't remember the exact pressure but it was considerably high... I am not aware of flow rates limitation of NI-AL Bronze ... Can you please elaborate....

Also do you mean that DSS can be used for Sea Water application at temperatures of 45 deg C... Same is mentioned in NACE ??

Non metallic is not considered an option here ...
 
A superduplex would be considered a seawater service alloy, these are alloys with higher Cr and Mo than the standard 2205, it isn't a seawater grade.
If you really need strength then a a superduplex would have advantages.
But the welding of these alloys is much more difficult that for the superaustenitic alloys.

If you look in data from Outokumpu you can find temperature and Cl limits for duplex alloys.



= = = = = = = = = = = = = = = = = = = =
Plymouth Tube
 
If the pressure is high and the temperature is not, then non-metallic lined construction is the way to go.
 
Status
Not open for further replies.

Part and Inventory Search

Sponsor