Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 353
ICC - Report ID: 353-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Hydroxymethylfurfural Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Related Reports List: 009-A,370-A,009-B,138-F,138-G,266-C,266-D
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"799","2":"799","3":"799"},"2":{"1":"1599","2":"1599","3":"1599"},"3":{"1":"2699","2":"2699","3":"2699"}},"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/353-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>HMF</b></p>, <p><b>Levulinic Acid</b></p> <h6>Raw Materials</h6> <p><b>Glucose Syrup</b></p>, <p><b>Hydrochloric Acid</b></p>, <p><b>Sodium Chloride</b></p>, <p><b>Butanol</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/353-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major steps: (1) Glucose isomerization; (2) HMF production; (3) HMF purification; and (4) levulinic acid purification.</p><p>Glucose isomerization. The glucose feed is first isomerized to fructose. The isomerization reactor effluent is passed through an evaporator and then 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 biphasic reactor.</p><p>HMF production. The fructose produced is fed to the biphasic reactor, in which it is dehydrated to HMF in the presence of hydrochloric acid. To prevent HMF hydrolyses to levulinic and formic acids, the dehydration is carried out in the presence n-butanol, which forms an organic layer (biphasic system) into which the HMF formed is continuously extracted.</p><p>HMF purification. The organic layer containing the HMF product is distilled, for the removal of butanol, water, formic acid and residual HCl as distillate. This mixture is further distilled for the recovery of butanol, while the stream containing the HMF is then passed through decanters, where it is purified from water, levulinic acid and fructose. Finally, the crude HMF stream is purified from butanol and water by passing through a flash vessel and a distillation column, yielding a high-purity HMF stream.</p><p>Levulinic acid purification. The aqueous layer (water, levulinic acid and fructose), is fed to a column in which water is stripped off from the mixture and recycled. The resulting mixture is passed through an evaporator, for the recovery of residual fructose, and then through a distillation column, for the separation of levulinic acid byproduct and butanol.</p>
ICC - Short Description: This report presents the economics of Hydroxymethylfurfural (HMF) production from glucose syrup. In the process examined, glucose is enzymatically isomerized into fructose. It is then dehydrated in the presence of n-butanol, yielding HMF. The economic analysis performed assumes a plant located in the United States.
ICC - Main Product: Hydroxymethylfurfural
ICC - Plant Capacity: 65.00
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Hydroxymethylfurfural Production

Hydroxymethylfurfural Production Costs Report | Issue A | Q2 2024

Production Cost Report

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65 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 65 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

Process Consumptions

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Production Costs Datasheet

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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 Hydroxymethylfurfural 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 Hydroxymethylfurfural 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 Hydroxymethylfurfural 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 Hydroxymethylfurfural 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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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.

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