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.

附加文件3：技术经济分析（Technoeconomic Analysis, TEA）开发所用数据。
表S11：采用ASPEN软件开展液液萃取、溶剂蒸馏及中链脂肪酸（Medium-Chain Fatty Acid, MCFA）分离的流程建模汇总表。
表S12：纳入美国国家可再生能源实验室（National Renewable Energy Laboratory, NREL）技术经济分析的资本支出汇总表。
表S13：纳入NREL技术经济分析的运营支出及额外产品收入汇总表。
表S14：经更新后纳入中链脂肪酸生产支出与收入的NREL技术经济分析30年现金流情况。
表S15：额外资本支出的计算明细。
表S16：从Zauba平台获取的辛酸、己酸及2-辛醇的化学品成本数据。