Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 266
ICC - Report ID: 266-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: FDCA Production from Glucose
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 266-B,266-C,266-D
ICC - Related Reports List: 370-A,001-A,005-B,001-B,310-A,005-A
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"1199","2":"1199","3":"1199"},"2":{"1":"1999","2":"1999","3":"1999"},"3":{"1":"3399","2":"3399","3":"3399"}},"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/266-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>FDCA</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>Chemicals</b></p>, <p><b>Glucose Syrup</b></p>, <p><b>Acetic Acid</b></p>, <p><b>Sulfuric Acid</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/266-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Furans Production; (2) MMF Purification; and (3) FDCA Production.</p><p>Furans production. The glucose content of the feed is first enzymatically isomerized to fructose, and the effluent is passed through ion-exchange resins to separate unreacted glucose from the fructose. The former is recycled to the isomerization reactor and the latter is sent to the furans conversion reactor. There, crystallized fructose is solubilized with a 95 wt.% methanol aqueous solution and sulfuric acid. The reaction is conducted at 50 bars and 200ºC. Fructose is dehydrated to hydroxyl methyl furan (HMF) and, due to the excess of methanol, most HMF is converted to MMF, which is more stable than HMF.</p><p>MMF purification. The reactor effluent is then sent to a distillation system to recover the solvent and separate the MMF from other impurities. Methanol and water are recovered and returned to the furans conversion area, while methyl levulinate is recovered as a byproduct. Also, a heavies stream is recovered to be used as boiler fuel, and finally, purified MMF is recovered and directed to the FDCA production area.</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 is purified using two distillation columns. Catalyst is also recovered, but it must be reactivated 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 from the solid materials. The liquid effluent is a waste stream. </p><p></p>
ICC - Short Description: This report presents the economics of 2,5-Furandicarboxylic Acid (FDCA) production from glucose syrup via a furan process similar to Avantium YXY technology. Initially, glucose is enzymatically isomerized into fructose, which is dehydrated in the presence of methanol, yielding methoxymethylfurfural (MMF). Finally, MMF is oxidized to FDCA. The economic analysis assumes a plant constructed in the United States.
ICC - Main Product: FDCA
ICC - Plant Capacity: 270.00
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FDCA Production from Glucose

FDCA Production Costs Report | Issue A | Q3 2024

Production Cost Report

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270 kta United States-based plant   |   Q3 2024   |   107 pages

This report presents a cost analysis of a 270 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.

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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 FDCA 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 FDCA 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 FDCA 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 FDCA 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 FDCA Production Cost Reports

FDCA Production from Raw Sugar

This report presents the costs associated with the construction of a plant producing FDCA from raw sugar (sucrose) in Germany. Initially, sucrose is hydrolyzed into glucose and fructose and the glucose obtained is enzymatically isomerized into fructose. It is then dehydrated in ionic liquid medium, yielding hydroxymethylfurfural, which is finally oxidized to FDCA. The process examined is based in a non-commercial route.

Details: 90 kta Germany-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $1,199 USD

The cost analyses presented in this report target a 90 kta (kilo metric ton per annum per annum) Germany-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

Solid FDCA Production from HMF

This analysis presents a process, in which hydroxymethylfurfural (HMF) is oxidized to generate 2,5-Furandicarboxylic Acid (FDCA). FDCA is recovered from the reaction product in solid form. The economic analysis is based on a plant located in the United States.

Details: 270 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 270 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   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

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