Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: C
ICC - Volume: 310
ICC - Report ID: 310-C
ICC - Report Location: Germany
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Polyethylene Furanoate Production from Raw Sugar
ICC - Show Overview: 1
ICC - Report Location ID: 2
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 310-A,310-B
ICC - Related Reports List: 001-A,002-A,005-A,005-B,001-B,002-B
ICC - Report Location Code: DEU
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ICC - Prices: {"versions":{"1":{"1":"1499","2":"1499","3":"1499"},"2":{"1":"2399","2":"2399","3":"2399"},"3":{"1":"3999","2":"3999","3":"3999"}},"currency":"USD"}
ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/310-C.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Bottle-Grade PEF</b></p>, <p><b>Methyl Levulinate</b></p>, <p><b>Methyl Acetate</b></p> <h6>Raw Materials</h6> <p><b>Methanol</b></p>, <p><b>Ethylene Glycol</b></p>, <p><b>Chemicals</b></p>, <p><b>Acetic Acid</b></p>, <p><b>Sulfuric Acid</b></p>, <p><b>Raw Sugar</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/310-C.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) MMF Production (2) FDCA Production; and (3) Polymerizations.</p><p>MMF production. Raw sugar undergoes inversion reaction, regenerating glucose and fructose.The effluent is passed through ion-exchange resins to separate both monosaccharides. The glucose is enzymatically isomerized to fructose and is recycled. The crystallized fructose is solubilized with a 95 wt.% methanol and sulfuric acid. Fructose is dehydrated to HMF and, due to the excess of methanol, most HMF is converted to MMF. The reactor effluent is sent to a distillation system to recover the solvent, methyl levulinate as by-product, and purified MMF.</p><p>FDCA production. Purified MMF is mixed with acetic acid solvent and catalyst in the oxidation reactor to be converted to FDCA. This stream is filtered to recover crude FDCA. The acetic-acid-rich liquid and catalyst are both recovered before being recycled to the process. Crude FDCA is mixed with water and hydrogen in a hydrogenation reactor, where impurities are removed. The effluent from the reactor is crystallized, and purified FDCA is recovered.</p><p>Polymerizations. MEG and FDCA are mixed and passed through two agitated and jacketed reactors, in which esterification takes place generating BHEF. The BHEF monomer is fed to an agitated, jacketed reactor, where PEF oligomers are generated. Next, the PEF oligomers condensate in a rotating disc reactor. Here, higher molecular weight PEF chains are generated. MEG is recovered from gaseous effluents and recirculated. The molten PEF is turned into amorphous PEF chips, which are treated and dried before they are crystallized, to not stick together or agglomerate. The crystallized particles are then polycondensed in a long cylindrical hopper-type vessel. The bottle-grade PEF chips are cooled down, separated from dust, homogenized and packed.</p>
ICC - Short Description: This report presents the economics of Polyethylene Furanoate (PEF) production from raw sugar and monoethylene glycol (MEG) similar to Avantium YXY in Germany. Initially, raw sugar is inverted to fructose and glucose, which is isomerized to fructose. Then, fructose is converted to methoxy methyl furan (MMF), which is oxidized to FDCA. FDCA generated and MEG are then polymerized to PEF in melt-phase and solid-state polymerization.
ICC - Main Product: Polyethylene Furanoate
ICC - Plant Capacity: 300.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Polyethylene Furanoate Production from Raw Sugar

Polyethylene Furanoate Production Costs Report | Issue C | Q2 2024

Production Cost Report

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Report Details
300 kta Germany-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 300 kta (kilo metric ton per annum) Germany-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.

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Production Process Information

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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 Polyethylene Furanoate 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 Polyethylene Furanoate 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 Polyethylene Furanoate 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 Polyethylene Furanoate 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

Other Polyethylene Furanoate Production Cost Reports

Polyethylene Furanoate Production from FDCA

This report presents the economics of Polyethylene Furanoate (PEF) production from monoethylene glycol (MEG) and 2,5-furandicarboxylic acid (FDCA). In the process under analysis, FDCA and MEG are polymerized to PEF in two polymerization steps: melt-phase polymerization and solid-state polymerization. The economic analysis provided assumes a plant located in the United States.

Details: 300 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $1,199 USD

The cost analyses presented in this report target a 300 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.

Polyethylene Furanoate Production from Glucose

This report, in turn, presents the economics of Polyethylene Furanoate (PEF) production from monoethylene glycol (MEG) and glucose syrup in the United States. In this process, a glucose is isomerized to fructose. Then, fructose is converted to methoxy methyl furan (MMF) intermediate, which is oxidized to FDCA. This process is similar to Avantium YXY. FDCA generated and MEG are then polymerized to PEF in melt-phase and solid-state polymerization.

Details: 300 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $1,499 USD

The cost analyses presented in this report target a 300 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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Details: 1,000 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

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