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This report presents a cost analysis of Methyl Methacrylate (MMA) production from isobutylene using an oxidation process. The process examined is similar to Sumitomo/Nippon Shokubai process. In this process, methacrylic acid (MAA) intermediate is initially produced by two-stage catalytic oxidation of isobutene. Then, MAA is esterified with methanol to produce MMA. This report was developed based essentially on the following reference(s): (1) EP Patent 1052017, issued to Nippon Shokubai in 2012 (2) "Methacrylic Acid and Derivatives", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Isobutene, Methylpropene, Esterification, Two-Stage Oxidation, Japan Methacryl Monomer, JMM
This report presents a cost analysis of Methyl Methacrylate (MMA) production from acetone, ammonia and natural gas The process examined is similar to Evonik Aveneer process. In this process, hydrogen cyanide, acetone and methanol are used as raw materials for the production of MMA. Different from the conventional acetone cyanohydrin (ACH) process, this process does not use sulfuric acid. The hydrogen cyanide used is generated from ammonia and natural gas in an on-site unit. This report was developed based essentially on the following reference(s): (1) US Patent 8569539, issued to Evonik in 2013 (2) US Patent 20120232305, issued to Evonik in 2012 (3) US Patent 20080194875, issued to Evonik in 2008 Keywords: Propanone, Hydrolysis, Transesterification, Dehydration, Prussic Acid
This report presents a cost analysis of Methyl Methacrylate (MMA) production from t-butanol and methanol. The process examined is carried out in three steps: oxidation of t-butanol to metacrolein; metacrolein oxidation to methacrylic acid; and esterification of methacrylic acid with methanol to generate the methyl methacrylate product. This report was developed based essentially on the following reference(s): Keywords: Tertiary Butyl Alcohol, Tertiary Butanol, Mitsubishi, Nippon Shokubai
This report presents a cost analysis of Methyl Methacrylate (MMA) production from acetone and hydrogen cyanide (HCN). The process examined is similar to Evonik Aveneer process. In this process, hydrogen cyanide, acetone and methanol are used as raw materials for the production of MMA. Different from the conventional acetone cyanohydrin (ACH) process, this process does not use sulfuric acid. This report was developed based essentially on the following reference(s): (1) US Patent 8569539, issued to Evonik in 2013 (2) US Patent 20120232305, issued to Evonik in 2012 (3) US Patent 20080194875, issued to Evonik in 2008 Keywords: Propanone, Hydrolysis, Transesterification, Dehydration, Prussic Acid
This report presents a cost analysis of Methacrylic Acid (MAA) production from isobutylene The process examined is a typical oxidation process. This report was developed based essentially on the following reference(s): Keywords: Unsaturated Polyester, UPR, MAA, i-Butylene