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This report presents the economics of bio-based Butanol production from corn in the United States. The process under analysis is a conventional Acetone-Butanol-Ethanol (ABE) fermentation process. Initially, corn undergoes wet milling to separate starch, which is hydrolyzed in two steps. Glucose is fermented to produce butanol, acetone and ethanol.
This report examines a conventional Acetone-Butanol-Ethanol (ABE) fermentation process. This economic analysis assumes a plant located in Germany using raw sugar as feedstock, which is fermented to Butanol, acetone and ethanol by a novel strain of Clostridium. Each product is separated.
This study analyzes the costs for n-Butanol production from butyraldehyde. In this process, n-butyraldehyde is hydrogenated generating n-Butanol. The economic analysis is based on a plant constructed in the United States.
The report shows an economic analysis of the construction of an industrial plant in the United States for n-Butanol production. In the process reviewed ethanol is dimerized into n-Butanol via the Guerbet reaction. This reaction is composed by dehydrogenation, aldol condensation and hydrogenation.
This report presents an economic analysis of n-Butanol production from propylene and syngas, assuming a plant located in the United States. The process under analysis is similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. This process comprises hydroformylation of propylene and n-butyraldehyde hydrogenation.