Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 19
ICC - Report ID: 019-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Adipic Acid Production from Cyclohexane
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 019-B,019-C,019-E,019-I,019-J,019-D,019-F,019-G,019-H
ICC - Related Reports List: 223-B,047-B,223-A,047-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"2":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"3":{"1":{"time":"7","price":0},"2":{"time":"3","price":"299"}}},"unit":"d"}
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/019-A.jpg
ICC - Process Overview Text: ProductsFiber Grade Adipic Acid,Liquid AGS MixtureRaw MaterialsChemicals,Cyclohexane,Nitric Acid
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/019-A.jpg
ICC - Process Schematic Text: The process under analysis comprises two major sections: (1) First oxadation step; and (2) Second oxidation step.Fist oxidation step. Initially, cyclohexane is fed to the first of several staged air oxidation vessels, along with meta-boric acid. The cyclohexane is oxidized in the liquid-phase to cyclohexyl hydroperoxide (CHHP). In the presence of boric acid, the cyclohexyl hydroperoxide is trapped as cyclohexyl perborate ester, which in turn reacts with cyclohexane yielding borate ester and cyclohexanol. The borate ester formed is relatively stable, in such a way that the generation of undesired by-products is minimized. Next, the ester is hydrolyzed, yielding cyclohexanol and boric acid, which is dehydrated and recycled to the oxidation. Subsequently, CHHP still present in the oxidation product is decomposed by another oxidation reaction over a fixed bed of cobalt catalysts, yielding a cyclohexanol-cyclohexanone mixture (KA oil).Second oxidation step. The KA oil is then reacted with nitric acid in the presence of copper/vanadium catalyst to form Adipic Acid. While this second oxidation is very exothermic, a high ratio of nitric acid to KA oil is employed, so that the nitric acid also works as heat sink, avoiding uncontrollable reactions. The oxidation reaction is extremely quick; it is carried out in two converters, operating at different temperatures. Most of the KA oil is oxidized in the first, low-temperature converter, with the remainder being converted in the high-temperature converter downstream. Nitrogen oxides and nitrogen gas are released from the reaction. While this can be viewed as nitric acid losses, NO2 and NO are recovered, further oxidized, and recycled as nitric acid. After separation of water and monobasic acids from the oxidation product, crystallization under vacuum, and centrifugation, a crude Adipic Acid is obtained. Finally, the crude Adipic Acid is re-dissolved in water, recrystallized, centrifuged, and dried, yielding fiber-grade Adipic Acid.
ICC - Short Description: This report presents a cost analysis of Adipic Acid production from cyclohexane in the United States. The process examined is a two-stage oxidation process, in which cyclohexane is initially oxidized with air to produce KA oil (mixture of cyclohexanone and cyclohexanol), and further oxidized with nitric acid to produce Adipic Acid.
ICC - Main Product: Adipic Acid
ICC - Plant Capacity: 350.00
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Petrochemicals

Adipic Acid Production from Cyclohexane

Adipic Acid Production Costs Report | Issue A | Q3 2024

Production Cost Report

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

This report presents a cost analysis of a 350 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

Labor Requirements

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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

Costs in Different Countries Add-on

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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

Other Adipic Acid Production Cost Reports

Adipic Acid Production from Benzene and Propylene

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

Cyclohexane from Benzene and Hydrogen (Liquid-Phase Process)

This feasibility study shows the economics of Cyclohexane production from benzene using a liquid phase hydrogenation process in the presence of a nickel-based catalyst. The economic analysis presented is based on a plant constructed in the United States.

Details: 200 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 200 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.

Cyclohexane from Benzene and Hydrogen (Vapor-Phase Process)

This feasibility study shows the economics of Cyclohexane production from benzene using a vapor phase hydrogenation process in the presence of a nickel-based catalyst. The economic analysis presented is based on a plant constructed in the United States.

Details: 200 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $999 USD

The cost analyses presented in this report target a 200 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 (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.

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