The Corrosion Resistance of Stainless Steels in Weak, Hot Sulphuric and Sulphurous Acid Environments Applicable to the Pre-Hydrolysis of Biomass, 2012 TAPPI PEERS Conference
Please Note: This document will be available in PDF format in the "My Electronic Documents" link on the home page once your order has been completed. Please make sure you have the latest version of Acrobat Reader. Click on the Acrobat Reader icon to check for the latest version, it’s FREE. To print a hardcopy of a PDF file correctly you must have a postscript printer. If you are not sure if your printer is a postscript printer please refer to your owner’s manual.
Purchase of electronic (downloadable) documents made at www.tappi.org by credit cards, followed by instant download CANNOT be cancelled. We do not offer refunds on electronic download documents.
The reason for this work is the current interest in the extraction of hemicelluloses from forest biomass, by acid pre-hydrolysis, for conversion to sugar streams and on to chemicals and fuels. Industrial process designs are not yet set, but the use of hot, weak, sulphuric or sulphurous acid environments are possible. By hot we mean 150° – 210°C; e.g., 150°C for typical mild acid hydrolysis, or 210°C for steam explosion. By weak we mean a pH of around 1. Other anticipated process conditions are batch operations in digester-like vessels (although other process designs and vessels are certainly possible, such as for steam explosion) short pre-hydrolysis time (meaning frequent cycling of temperatures and fresh acid) and the presence of process contaminants from use of industrial grade acid, or cross-contamination from other kraft mill process streams. Biomass is inherently inhomogeneous and the effect of contaminant build-up is often ignored in the scale-up from laboratory to industrial scale.