Ethylene Glycol Production from Carbon Dioxide
Ethylene Glycol Production Costs Report | Issue C | Q2 2024
Report Details |
150 kta United States-based plant | Q2 2024 | 107 pages | Delivered in PDF |
This report presents a cost analysis of a 150 kta (kilo metric ton per annum) United States-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.
Report Abstract
This study presents the economics of Monoethylene Glycol (MEG) production from carbon dioxide (CO2) in the United States using an electrochemical process similar to Liquid Light process. Initially, CO2 is electrochemically reduced and acidified into oxalic acid. Then, oxalic acid is esterified with methanol producing dimethyl oxalate, which is hydrogenated forming MEG.
The report provides a comprehensive study of Ethylene Glycol production and related Ethylene Glycol production cost, covering three key aspects: a complete description of the Ethylene Glycol production process examined; an in-depth analysis of the related Ethylene Glycol plant capital cost (Capex); and an evaluation of the respective Ethylene Glycol plant operating costs (Opex).
The Ethylene Glycol production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Ethylene Glycol plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Ethylene Glycol plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic
The process under analysis comprises three major sections: (1) Bromide Phase; (2) Oxalate Treatment; and (3) MEG Purification.
Bromide Phase. In an electrochemical reactor, CO2 is electrochemically reduced into oxalate at the cathode and bromide is oxidized into bromine. The catholyte and anolyte used in the process are tetrabutylammonium bromide (TBA-Br) salt dissolved in acetonitrile solvent. In this area, the oxalate is acidified to oxalic acid. First, the oxalate anions are absorbed using a basic anion exchange resin and further desorbed using hydrogen bromide dissolved in methanol. The hydrogen bromide is further removed from the oxalic acid dissolved in methanol, while the TBA-Br in acetonitrile is recovered and recycled back to the electrochemical reaction.
Oxalate Treatment. The oxalic acid solution is sent to esterification, where it reacts with methanol to produce dimethyl oxalate. The ester is hydrogenated to generate Ethylene Glycol in a gaseous phase reaction. Methanol is separated from the main product and water, and is recycled to dissolve hydrogen bromide upstream.
MEG Purification. The product stream is passed through a series of columns, in order to remove light and heavy impurities, such as 1,2-butanediol by-product. Fiber Grade Ethylene Glycol is stored.
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Production Process Information
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Production Costs Datasheet
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Operating Cost Details
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Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Plant Cost Breakdowns
Plant Capacity Assessment
Process Flow Diagrams
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Ethylene Glycol production plant examined
Plant Capital Cost Details
Detailing of fixed capital (ISBL, OSBL & Owner’s Cost), working capital and additional capital requirements
Plant Cost Breakdowns
Breakdown of Ethylene Glycol process unit (ISBL) costs and infrastructure (OSBL) costs; plant cost breakdown per discipline
Operating Costs Summary
Summary presenting the operating variable costs and the total operating cost of the Ethylene Glycol production plant studied
Operating Cost Details
Detailing of utilities costs, operating fixed costs and depreciation
Plant Capacity Assessment
Comparative analysis of capital investment and operating costs for different Ethylene Glycol plant capacities
Production Process Information
Block Flow Diagram, descriptions of process unit (ISBL) and site infrastructure (OSBL)
Process Consumptions
Raw materials and utilities consumption figures, by-products credits, labor requirements
Process Diagrams
Process flow diagrams (PFD), equipment list and industrial site configuration
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The cost analyses presented in this report target a 150 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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