TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Method: The method further comprises: contacting the volatile component from a lipid-rich biomass with a dehydration catalyst to produce a first product which on cooling to 1-20 degrees C produces a second volatile component, a first renewable fuel and water; contacting the second volatile component with an aromatization catalyst to produce a second product which on cooling to 1-20 degrees C produces a third volatile component, a second renewable fuel and water, and recovering the second renewable fuel; contacting the third volatile compound with a gas-upgrading catalyst to produce a third product which on cooling to 1-20 degrees C produces a fourth volatile component, a third renewable fuel and water, and recovering the third renewable fuel; subjecting the fourth volatile component to at least one of other processing stations, a dehydration catalyst, an aromatization catalyst, a gas-upgrading catalyst, and a combustion gas treatment plant; contacting a volatile component from a hemicellulose-rich biomass directly with an aromatization catalyst to produce a fourth product which on cooling to 0-5 degrees C produces a fifth volatile component, a fourth renewable fuel and water, and recovering the fourth renewable fuel; contacting the fifth volatile component with a gas-upgrading catalyst to produce a fifth product which on cooling to 0-5 degrees C produces a sixth volatile component, a fifth renewable fuel and water, and recovering the fifth renewable fuel; routing the sixth volatile component to at least one of other processing stations, a dehydration catalyst, an aromatization catalyst, a gas-upgrading catalyst, or a combustion gas treatment plant; contacting a volatile component from a lignin-rich biomass with a dehydration catalyst to produce a sixth product which on cooling to 2-20 degrees C produces a seventh volatile component, a sixth renewable fuel and water; contacting the seventh volatile component with an aromatization catalyst to produce a seventh product which on cooling to 0-5 degrees C produces an eighth volatile component, a seventh renewable fuel and water, and recovering the seventh renewable fuel; contacting the eighth volatile component with a gas-upgrading catalyst to produce an eighth product which on cooling to 0-5 degrees C produces a ninth volatile component, an eight renewable fuel and water, and recovering the eighth renewable fuel; and subjecting the ninth volatile component to at least one of other processing stations, a dehydration catalyst, an aromatization catalyst, a gas-upgrading catalyst, and a combustion gas treatment plant.