Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments

There has been an increase in the production of bio-fuels. Organosolv delignification, high temperature ethanol/water environments, can be used to separate lignin, cellulose, and hemicelluloses in the bio-mass for bio-fuel production. These environments have been shown to induce stress corrosion cra...

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Main Author: Gulbrandsen, Stephani
Language:en_US
Published: Georgia Institute of Technology 2013
Subjects:
Online Access:http://hdl.handle.net/1853/47815
id ndltd-GATECH-oai-smartech.gatech.edu-1853-47815
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spelling ndltd-GATECH-oai-smartech.gatech.edu-1853-478152013-07-15T03:12:34ZStress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environmentsGulbrandsen, StephaniEthanol and water solutionsStainless steelStress corrosion crackingAustenitic stainless steel Stress corrosionAustenitic stainless steel CrackingBiomass energyLignin OxidationThere has been an increase in the production of bio-fuels. Organosolv delignification, high temperature ethanol/water environments, can be used to separate lignin, cellulose, and hemicelluloses in the bio-mass for bio-fuel production. These environments have been shown to induce stress corrosion cracking (SCC) in 316L stainless steel. Previous research has been done in mixed solvent environments at room temperature to understand SCC for stainless steels, but little is known about the behavior in high temperature environments. Simulated organosolv delignification environments were studied, varying water content, temperature, pHe, and Cl- content to understand how these constituents impact SCC. In order for SCC to occur in 316L, there needs to be between 10 and 90 volume % water and the environment needs to be at a temperature around 200°C. Once these two conditions are met, the environment needs to either have pHe < 4 or have more than 10 ppm Cl-. These threshold conditions are based on the organosolv delignification simulated environments tested. SCC severity was seen to increase as water content, temperature, and Cl- content increased and as pHe decreased. To prevent failure of industrial vessels encountering organosolv delignification environments, care needs to be taken to monitor and adjust the constituents to prevent SCC.Georgia Institute of Technology2013-06-18T18:41:24Z2013-06-18T18:41:24Z2012-06Thesishttp://hdl.handle.net/1853/47815en_US
collection NDLTD
language en_US
sources NDLTD
topic Ethanol and water solutions
Stainless steel
Stress corrosion cracking
Austenitic stainless steel Stress corrosion
Austenitic stainless steel Cracking
Biomass energy
Lignin Oxidation
spellingShingle Ethanol and water solutions
Stainless steel
Stress corrosion cracking
Austenitic stainless steel Stress corrosion
Austenitic stainless steel Cracking
Biomass energy
Lignin Oxidation
Gulbrandsen, Stephani
Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments
description There has been an increase in the production of bio-fuels. Organosolv delignification, high temperature ethanol/water environments, can be used to separate lignin, cellulose, and hemicelluloses in the bio-mass for bio-fuel production. These environments have been shown to induce stress corrosion cracking (SCC) in 316L stainless steel. Previous research has been done in mixed solvent environments at room temperature to understand SCC for stainless steels, but little is known about the behavior in high temperature environments. Simulated organosolv delignification environments were studied, varying water content, temperature, pHe, and Cl- content to understand how these constituents impact SCC. In order for SCC to occur in 316L, there needs to be between 10 and 90 volume % water and the environment needs to be at a temperature around 200°C. Once these two conditions are met, the environment needs to either have pHe < 4 or have more than 10 ppm Cl-. These threshold conditions are based on the organosolv delignification simulated environments tested. SCC severity was seen to increase as water content, temperature, and Cl- content increased and as pHe decreased. To prevent failure of industrial vessels encountering organosolv delignification environments, care needs to be taken to monitor and adjust the constituents to prevent SCC.
author Gulbrandsen, Stephani
author_facet Gulbrandsen, Stephani
author_sort Gulbrandsen, Stephani
title Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments
title_short Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments
title_full Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments
title_fullStr Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments
title_full_unstemmed Stress corrosion cracking of 316L austenitic stainless steel in high temperature ethanol/water environments
title_sort stress corrosion cracking of 316l austenitic stainless steel in high temperature ethanol/water environments
publisher Georgia Institute of Technology
publishDate 2013
url http://hdl.handle.net/1853/47815
work_keys_str_mv AT gulbrandsenstephani stresscorrosioncrackingof316lausteniticstainlesssteelinhightemperatureethanolwaterenvironments
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