id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
cet-3730		cet-3730		6	.pdf	application/pdf	3439	139	57	Figure 4: Feasible structure #1b with cutover residues included for boiler fuel 5. P-graph methodology for biomass processing process synthesis As noted previously there was very little profit differential between solutions in region 1 and all six profitable products were present within this region. Delivered biomass feedstock costs are often highly non-linear due to biomass source quantity and distance from the mill.	cache/cet-3730.pdf	txt/cet-3730.txt