NOTICE

Forums are temporarily disabled while we are working on a new login procedure.

When migrating the old forums over to our new forums we were unable to retain the identity of the authors, so the old posts will show up as "anonymous". All NEW posts will show up credited to their authors. So please participate and share knowledge just as you have in the past.

You must log in if you are an existing user or register if you are a new user in order to contribute to the discussions.

Discussion Forums - The Hendrix Group
HomeHomeDiscussionsDiscussionsMaterial Select...Material Select...co2 corrosionco2 corrosion
Previous
 
Next
New Post
5/26/2007 9:00 AM
 
We are working on natural gas compression project, where the gas, predominantly, Methane, is saturated, having 6% CO2 and 100 ppm of H2S. The gas enters the compressor at a suction pressure of 807 psia @ 144 deg F and the discharge pressure of the compressor is maintained at 909 psia), the corresponding temperature is 280 deg. F. We are using after cooler to bring gas temperature down to 122 deg. F in one case and in the other, it is going down to 118 deg. F. The compressor has inlet filter separators, which can remove droplet, greater than 1 micron size with an efficiency of 98.6%, with 3 micron size, 99.9%. While working on the material selection for this project, we have following questions for our better understanding the corrosive nature of the service and the suitability of the material being proposed: > > 1. Can we use austenitic stainless steel (SS 300 series), where our temperature is at or above 60 deg. C? The partial pressure of H2S varies, (with the operating pressure) however, is always less than 100 kpa or 1 bar (absolute). > 2. Can we use vessel internals (like trays, demister, cyclone tubes, etc.) being non pressure retaining in SS 300 series constructions, where the H2S partial pressure is at or above 100 kpa (absolute) and the temperature is above 60 deg. C? > 3. Can we consider vessel internal cladding as non pressure retaining and therefore can use SS 300 series cladding material where the H2S partial pressure is at or above 100 kpa (absolute) and the temperature is above 60 deg. C?
 
New Post
6/2/2007 9:00 AM
 
peeyar1: Re your below question regarding the use of 300 series stainless steels in CO2 and H2S service, in general the 300-series stainless steels should be resistant to your stated concentrations of carbon dioxide and hydrogen sulfide. However, you need to consider whether chlorides are present before selecting these materials. Chlorides can pit and crack the 300SS depending on the concentation, temperature, deposits, etc. Hope this helps! David Hendrix The Hendrix Group Inc. >We are working on natural gas compression project, where the >gas, predominantly, Methane, is saturated, having 6% CO2 and >100 ppm of H2S. The gas enters the compressor at a suction >pressure of 807 psia @ 144 deg F and the discharge pressure >of the compressor is maintained at 909 psia), the >corresponding temperature is 280 deg. F. We are using after >cooler to bring gas temperature down to 122 deg. F in one >case and in the other, it is going down to 118 deg. F. The >compressor has inlet filter separators, which can remove >droplet, greater than 1 micron size with an efficiency of >98.6%, with 3 micron size, 99.9%. While working on the >material selection for this project, we have following >questions for our better understanding the corrosive nature >of the service and the suitability of the material being >proposed: >> >> 1. Can we use austenitic stainless steel (SS 300 series), where our temperature is at or above 60 deg. C? The partial pressure of H2S varies, (with the operating pressure) however, is always less than 100 kpa or 1 bar (absolute). >> 2. Can we use vessel internals (like trays, demister, cyclone tubes, etc.) being non pressure retaining in SS 300 series constructions, where the H2S partial pressure is at or above 100 kpa (absolute) and the temperature is above 60 deg. C? >> 3. Can we consider vessel internal cladding as non pressure retaining and therefore can use SS 300 series cladding material where the H2S partial pressure is at or above 100 kpa (absolute) and the temperature is above 60 deg. C?
 
New Post
6/5/2007 9:00 AM
 
I suggest you to look in NACE / ISO 15156 for SS limit in Sour Service. CO2 corrosion is usually not an issue when you use SS. regards Vitt
 
New Post
7/25/2007 9:00 AM
 
the only known material to resist this corrosion is calorised pipes. You can get these from us
 
Previous
 
Next
HomeHomeDiscussionsDiscussionsMaterial Select...Material Select...co2 corrosionco2 corrosion


  

News

With a little delay, our Calculation of Ammonium Salt Deposition Temperatures...read more
Our sulfidic corrosion calculators are now available at hghouston.com/calcula...read more

Stay Current

Sign up for our quarterly newsletter

covering updates on corrosion

Sign Up