MOESM3 of Increasing the economic value of lignocellulosic stillage through medium-chain fatty acid production

Additional file 3. Data used for development of the technoeconomic analysis (TEA). Table S11. Summary of process modeling for liquid-liquid extraction, solvent distillation, and MCFA separation with ASPEN. Table S12. Summary of capitol expenses added to the NREL TEA. Table S13. Summary of operating expenses and additional product revenues added to NREL TEA. Table S14. 30 year cash flow from NREL TEA updated to include MCFA production expenses and revenues. Table S15. Calculations for additional capital expenses. Table S16. Chemical costs for octanoic acid, hexanoic acid and 2-octanol obtained from Zauba.