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This report presents the economics of a process similar to Evonik Aveneer for Methyl Methacrylate (MMA) production from acetone and hydrogen cyanide (HCN) in the United States. Initially, HCN purchased from external suppliers, acetone and methanol are used as raw materials for the production of MMA in six main steps, which are described in the report.
This report presents the economics of a process similar to Evonik Aveneer for Methyl Methacrylate (MMA) production from acetone and hydrogen cyanide (HCN) in the United States. Initially, HCN is produced from ammonia (NH3) and natural gas in an on-site unit. Then, acetone and methanol are used as raw materials for the production of MMA in six main steps, which are described in the report.
This report presents the economics of an oxidation process similar to Sumitomo/ Nippon Shokubai process for Methyl Methacrylate (MMA) production from isobutylene in the United States. Initially, isobutylene is oxidized to methacrolein, which is further oxidized to methacrylic acid (MAA). Then, MAA is esterified with methanol to produce MMA.
This report presents the economics of Methyl Methacrylate (MMA) from Methacrylic Acid (MAA) and Methanol. In this process, MMA is produced through the esterification of MAA with methanol. The economic analysis assumes a plant located in the United States.
This study reviews the economics of a process for Methyl Methacrylate (MMA) production from t-Butanol. Initially, t-butanol is oxidized to metacrolein and then to methacrylic acid. Finally, the methacrylic acid undergoes esterification with methanol to generate MMA. The economic analysis performed is based on a plant constructed in the United States.