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Commodity Production Costs Olefins & Derivatives

Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 10:1)

This feasibility study approaches n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly developed by JM Davy and Union Carbide, employing Selector 10 catalyst. The production ratio of n- to iso-butyraldehyde is about 10.

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Commodity Production Costs Olefins & Derivatives

Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 30:1)

This report presents an economic analysis of n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. The production ratio of n- to iso-butyraldehyde is about 30.

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Commodity Production Costs Olefins & Derivatives

Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 4:1)

This report concerns the costs associated with the production of n-Butyraldehyde from propylene and syngas. The process under analysis is a propylene hydroformylation similar to the technology jointly developed by Rhodia (former Rhône-Poulenc) and Ruhrchemie. The economic analysis presented assumes a plant located in the United States.

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