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This report presents a cost analysis of Monoethylene Glycol (MEG) production from synthesis gas (syngas). In this process, syngas is carbonylated to dimethyl oxalate intermediate, which is then hydrogenated to MEG. This report was developed based essentially on the following reference(s): (1) US Patent 4453026, issued to Ube Industries Ltd. in 1984 (2) CN Patent 102380382, issued to Shenyang University of Chemical Technology in 2012 Keywords: 1,2-Ethanediol, Carbonylation, Hydrogenation, Nitric Oxide, Ube, Fujian Research Institute on the Structure of Matter, FJIRSM, Union Carbide, ARCO, Gasification
This report presents a cost analysis of Monoethylene Glycol (MEG) production from synthesis gas (syngas) In this process, syngas is carbonylated to dimethyl oxalate intermediate, which is then hydrogenated to MEG. This report was developed based essentially on the following reference(s): (1) US Patent 4453026, issued to Ube Industries Ltd. in 1984 (2) CN Patent 102380382, issued to Shenyang University of Chemical Technology in 2012 Keywords: 1,2-Ethanediol, Carbonylation, Hydrogenation, Nitric Oxide, Ube, Fujian Research Institute on the Structure of Matter, FJIRSM, Union Carbide, ARCO, Gasification
This report presents a cost analysis of Monoethylene Glycol (MEG) production from ethylene The process examined is similar to Shell OMEGA process. In this process, ethylene is first oxidized with oxygen to produce ethylene oxide, which is further converted to MEG. This report was developed based essentially on the following reference(s): (1) US Patent 8329959, issued to Shell in 2012 (2) US Patent 8217190, issued to Shell in 2012 Keywords: Ethene, Shell, OMEGA, Only MEG Advantage, Oxidation, Catalytic Process
This report presents a cost analysis of Monoethylene Glycol (MEG) production from ethylene oxide. The process examined is similar to Shell OMEGA process. In this process ethylene glycol is produced from ethylene oxide, with ethylene carbonate as an intermediate. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) Keywords: Shell, OMEGA, Only MEG Advantage, Oxidation, Catalytic Process, Mitsubishi
This report presents a cost analysis of Monoethylene Glycol (MEG) production from ethylene This process consists of a two-steps process. First, ethylene is oxidized with oxygen to produce ethylene oxide, which is further hydrolyzed to MEG. Diethylene glycol (DEG) and triethylene glycol (TEG) are also generated as by-products in the process. This report was developed based essentially on the following reference(s): (1) "Ethylene Oxide", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) "Ethylene Glycol", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Ethene, Shell Master, Scientific Design, Oxidation, Dow METEOR
This report presents a cost analysis of Monoethylene Glycol (MEG) production from ethylene. The process examined is similar to Shell OMEGA process. In this process, ethylene is first oxidized with oxygen to produce ethylene oxide. Part of the ethylene oxide generated is sold as a by-product and the remaining part is converted to MEG as the final product. This report was developed based essentially on the following reference(s): (1) US Patent 8329959, issued to Shell in 2012 (2) US Patent 8217190, issued to Shell in 2012 Keywords: Ethene, Shell, OMEGA, Only MEG Advantage, Oxidation, Catalytic Process
This report presents a cost analysis of Monoethylene Glycol (MEG) production from ethylene oxide. In this process ethylene oxide is hydrolyzed to MEG. Diethylene glycol (DEG) and triethylene glycol (TEG) are also generated as by-products in the process. This report was developed based essentially on the following reference(s): (1) "Ethylene Oxide", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) "Ethylene Glycol", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Shell Master, Scientific Design, Oxidation
This report presents a cost analysis of Syngas (Synthesis Gas) production from vacuum residue. The process examined is a typical non-catalytic partial oxidation process using as raw material the bottom product of a vacuum distillation unit, known as vacuum residue. This report was developed based essentially on the following reference(s): Keywords: Carbon Monoxide, Partial Oxidation
This report presents a cost analysis of Monoethylene Glycol (MEG) production from ethylene. The process examined is similar to Shell OMEGA process. In this process, ethylene is first oxidized with oxygen to produce ethylene oxide, which is further converted to MEG. This report was developed based essentially on the following reference(s): (1) US Patent 8329959, issued to Shell in 2012 (2) US Patent 8217190, issued to Shell in 2012 Keywords: Ethene, Shell, OMEGA, Only MEG Advantage, Oxidation, Catalytic Process