Biomass feedstocks contain roughly 10-30% lignin, a substance that can not be converted to fermentable sugars. Hence, most schemes for producing biofuels (ethanol) assume that the lignin coproduct will be utilized as boiler fuel to provide heat and power to the process. However, the chemical structure of lignin suggests that it will make an excellent high value fuel additive, if it can be broken down into smaller molecular units. From fiscal year 1997 through fiscal year 2001, Sandia National Laboratories was a participant in a cooperative effort with the National Renewable Energy Laboratory and the University of Utah to develop and scale a base catalyzed depolymerization (BCD) process for lignin conversion. SNL's primary role in the effort was to utilize rapidly heated batch microreactors to perform kinetic studies, examine the reaction chemistry, and to develop alternate catalyst systems for the BCD process. This report summarizes the work performed at Sandia during FY97 and FY98 with alcohol based systems. More recent work with aqueous based systems will be summarized in a second report.Batch microreactor studies demonstrated that the conversion of lignin to ether solubles by KOH in methanol or ethanol was rapid at 290 "C, reaching the maximum value (only 7% ether insoluble material remaining) within 10-15 minutes. Model compound studies confirmed that the dominant depolymerization route is the solvolysis of ether linkages. Strong bases (KOH, NaOH, CsOH) were shown to convert more of the lignin to ether soluble material than weaker bases (LiOH, Ca(OH)2, and Na2C03). An excess of base relative to lignin monomer units is required for maximum conversion. However, a synergistic interaction between NaOH and Ca(OH)* allows reasonable conversions of lignin to be achieved with small amounts of NaOH by coupling it with Ca(OH)2. Ethanol and methanol are converted to acetic and formic acid respectively under the reaction conditions with an activation energy of approximately 50 kcal/mol. This results in a loss of solvent, but more importantly neutralizes the base catalyst, halting forward progress of the reaction, and accounting for the excess base requirement.3