Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: C
ICC - Volume: 19
ICC - Report ID: 019-C
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Bio-Adipic Acid Production from Glucose (Fermentation Process)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 019-A,019-B,019-E,019-I,019-J,019-D,019-F,019-G,019-H
ICC - Related Reports List: 370-A,223-A,223-B
ICC - Report Location Code: USA
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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/019-C.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Fiber Grade Adipic Acid</b>. Fiber grade adipic acid is a crucial raw material in the production of nylon 6,6, a widely used synthetic fiber in textiles, carpets, and industrial materials. Its role in creating polyamide resins gives it significant value in the automotive, clothing, and packaging sectors. Fiber grade adipic acid is produced mainly through the oxidation of cyclohexane or phenol. It is handled as a crystalline solid and can be easily stored and transported. Its demand is tied closely to the growth of the synthetic fiber industry and related applications.</p> <h6>Raw Materials</h6> <p><b>Chemicals</b>. </p> <b>Glucose Syrup</b>. Glucose (C6H12O6), also known as D-glucose and dextrose, is the most abundant sugar in nature. Commercial glucose products are available in both dry and syrup forms in a variety of purities and concentrations. Glucose uses include pharmaceuticals, food, chemicals and fuels. This compound is used as raw material in fermentative processes for the production of vitamins, organic acids, antibiotics, amino acids, enzymes, and polysaccharides.</p> <b>Ammonia</b>. Ammonia (NH3) is one of the most produced synthetic chemicals worldwide. The main application of this world class commodity is in nitrogen fertilizers, followed by the synthesis of nitric acid. It is also used, to a lesser extent, in several other applications such as pulping of wood and as ingredient in household cleaners and drugs. Ammonia produced basically by the reaction between nitrogen and hydrogen, in a 1:3 stoichiometric ratio. Its production routes are related to the source of the hydrogen used, being steam reforming the main one. At atmospheric pressure, it boils at - 33 °C, so it is stored in refrigerated tanks to be kept as liquid.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/019-C.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Fermentation; and (2) Purification.</p><p>Fermentation. The culture media used in the pre-fermentation and in the fed-batch fermentation are prepared by diluting the glucose syrup and nutrients in water. The applied recombinant microorganism is propagated in an aerobic pre-fermentation step to obtain the proper inoculum concentration. When there is a sufficient mass of bacteria colony, the microorganism inoculum from the pre-fermentation step is fed into the fermentors. Fed-batch medium is continuously supplied to the fermentors, and the main fermentation is carried out under anaerobic process conditions. The pH control is made by addition of a solution of ammonia (NH3), so as to keep the pH of the fermentation broth around 7. Due to the presence of the ammonium hydroxide, most of the Adipic Acid produced is neutralized, in such a way that the broth contains Adipic Acid mainly in its conjugate base forms.</p><p>Purification. After fermentation, biomass is separated from the broth. The clarified broth then is submitted to an ultrafiltration step, used to remove the remaining contaminants. The resulting Adipic Acid solution then passes through a salt split and two successive crystallization steps for concentration and purification. The final product obtained is 99.9 wt% Adipic Acid.</p>
ICC - Short Description: This report assesses the economics of production of bio-based Adipic Acid. The process examined in this report is a fermentation process similar to BioAmber process, in which glucose is fermented to adipic acid. The process under analysis assumes a plant located in the United States.
ICC - Main Product: Adipic Acid
ICC - Plant Capacity: 150.00
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Bio-Adipic Acid Production from Glucose (Fermentation Process)

Adipic Acid Production Costs Report | Issue C | Q3 2024

Production Cost Report

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

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.

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Production Process Information

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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 Adipic Acid 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 Adipic Acid 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 Adipic Acid 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 Adipic Acid 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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This feasibility study assesses the production of Adipic Acid from benzene and propylene in the United States. In the process depicted, phenol is initially produced from benzene and propylene by means of alkylation, oxidation and cleavage. Then, phenol is hydrogenated to produce KA oil, which is then oxidized with nitric acid to produce Adipic Acid.

Details: 350 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   From $1,499 USD

The cost analyses presented in this report target a 350 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.

Fiber-Grade Adipic Acid Production from Crude Adipic Acid

This report presents the economics of high-purity Adipic Acid production starting from a crude adipic acid stream from a conventional two-stage oxidation process (similar to Invista technology). The crude stream passes through a series of purification steps that include centrifugation, crystallization and drying. The process under analysis assumes a plant located in the United States.

Details: 350 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue I   From $799 USD

The cost analyses presented in this report target a 350 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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Other Related Production Cost Reports

Nylon 6, 6 Production from Adipic Acid & HMDA (Batch Process)

This report presents the economics of Nylon 6,6 production from adipic acid and hexamethylenediamine (HMDA) via formation of hexamethylene diamonium adipate salt in the United States. The process analyzed consists of a typical batch polycondensation process.

Details: 65 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 65 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.

Nylon 6, 6 Production from Adipic Acid & HMDA (Continuous Process)

This report presents the economics of Nylon 6,6 production from adipic acid and hexamethylenediamine (HMDA) via formation of hexamethylene diamonium adipate salt in the United States. The process analyzed consists of a continuous polycondensation process.

Details: 120 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 120 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.

Glucose Syrup Production

This report presents the economics of Glucose Syrup production from shelled corn. In this process, shelled corn is passed through a wet milling process to recover the corn starch, which, in turn, passes through two subsequent hydrolysis steps for the generation of glucose. The economic analysis performed assumes a plant located in the United States.

Details: 40 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 40 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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