Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: G
ICC - Volume: 19
ICC - Report ID: 019-G
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Adipic Acid Production from Benzene and Propylene
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 019-A,019-B,019-C,019-D,019-E,019-F,019-G,019-H,019-I,019-J
ICC - Related Reports List: 019-I,230-B,364-B,230-A,036-D,036-C
ICC - Report Location Code: USA
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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/019-G.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Adipic Acid</b>. Adipic Acid is one of the most commercially important aliphatic dicarboxylic acids, produced on a very large scale at several locations worldwide. </p> <p><b>Acetone</b>. Acetone, also known as 2-propanone, is the simplest ketone. It is used as solvent for a wide range of organic compounds (e.g. oils, fats, resins, waxes and gums). It is also used as feedstock for the production of several chemicals, such as methyl methacrylate, bisphenol A, and methyl isobutyl ketone. The main source of acetone is the process for phenol production from cumene, which generates acetone as by-product at an approximate ratio for 0.6 kg of acetone per kg of phenol. Industrial consumers of acetone usually receive shipments in large containers made of carbon steel, tank trucks made of stainless steel or aluminum, or rail tank cars made of carbon steel or aluminum. International shipments by sea are usually made in steel barges and amount at least 2,000 metric tons.</p> <h6>Raw Materials</h6> <p><b>Propylene</b>. Propylene, the main raw material consumed, is a colorless gas at room temperature. It is a low-boiling, flammable, and highly volatile gas, with molecular formula C3H6. Propylene reacts vigorously with oxidizing materials. It may be mildly irritating to the nose, throat, and respiratory tract; propylene has low acute toxicity from inhalation. PG Propylene has been mainly produced as ethylene manufacturing co-product (via steam cracking of paraffinic hydrocarbons) and by-product of petroleum refining (separation from refinery gas). Most recently, amid a tight propylene market, new and novel lower-cost chemical processes for on-purpose propylene production have emerged.</p> <b>Benzene</b>. Benzene (C6H6) is a flammable and volatile liquid. As the most simple aromatic hydrocarbon, it is used as an intermediate to produce many important chemicals, such as styrene (raw material for polystyrene and synthetic rubber), cyclohexane (used in nylon production), alkylbenzenes (used in detergent industry), aniline (used to produce dyes and polyurethanes), and chlorobenzenes. Also, benzene is used to produce pharmaceuticals, specialty chemicals, plastics, and pesticides. It occurs naturally in crude oil and coal tar. </p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/019-G.jpg
ICC - Short Description: 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.
ICC - Main Product: Adipic Acid
ICC - Plant Capacity: 350.00
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Adipic Acid Production from Benzene and Propylene

Adipic Acid Production Costs Report | Issue G | Q2 2024

Production Cost Report

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

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

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

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Production Process Information

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Production Costs Datasheet

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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 Cyclohexane

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.

Details: 350 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $1,199 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.

Bio-Adipic Acid Production from Glucose (Chemical Catalytic Process)

This report shows a feasibility study of Bio-Adipic Acid production from glucose syrup in a plant located in the United States. The route examined is a two-step catalytic process similar to Rennovia process. In this process, glucose is first oxidized to produce glucaric acid, which is then hydrogenated to produce Adipic Acid.

Details: 150 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 150 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.

Bio-Adipic Acid Production from Glucose (Fermentation Process)

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.

Details: 150 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 150 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.

Bio-Adipic Acid Production from Raw Sugar

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 raw sugar is fermented to adipic acid. The process under analysis assumes a plant located in Germany.

Details: 150 kta Germany-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 150 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.

Adipic Acid Production from Benzene (Cyclohexane Intermediate)

This report presents the economics of Adipic Acid production from benzene in the United States using a two-stage oxidation process similar to Invista process. In this process, benzene is hydrogenated to cyclohexane, which is then oxidized to produce adipic acid with KA oil as intermediate.

Details: 350 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   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.

Adipic Acid Production from Phenol

It presents the economics of Adipic Acid production from phenol in the United States using a typical hydrogenation process. In the process examined, 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   |   Q2 2024   |   107 pages   |   Issue F   From $1,199 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.

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   |   Q2 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.

Adipic Acid Production from Benzene (Cyclohexene Intermediate)

This report presents the economics of Adipic Acid production from benzene in the United States using a two-stage oxidation process similar to Asahi Kasei process. In this process, benzene is partially hydrogenated to cyclohexene. Cyclohexene is then hydrated to produce cyclohexanol. The alcohol generated is finally oxidized to produce adipic acid.

Details: 350 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue H   From $1,199 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   |   Q2 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.

Adipic Acid Production from KA Oil

This report presents the economics of Adipic Acid production from a mixture of cyclohexanone and cyclohexanol (known as KA oil) in the United States. The process portrayed comprises the oxidation of the KA oil with nitric acid to produce Adipic Acid. A mixture of adipic, glutaric, and succinic acids is generated as by-product.

Details: 350 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue J   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

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   |   Q2 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.

Benzene Production from Pygas (Extractive Distillation Process)

This report examines the costs related to Benzene production from pyrolysis gasoline (pygas) in the United States using a typical extractive distillation process. Initially, pygas is fractionated into 3 hydrocarbon cuts. The C6s fraction is then fed to an extractive distillation system, using N-formylmorpholine (NFM) as solvent. to recover benzene.

Details: 250 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 250 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.

Benzene Production from Pygas (Hydrodealkylation Process)

This analysis presents the economics of Benzene production from pyrolysis gasoline (pygas) in the United States using a typical hydrodealkylation process. Initially, pygas is fractionated into 3 hydrocarbon cuts. The C6-C8 fraction is then directed to the hydrodealkylation step, in which the aromatics content in the process stream are converted into benzene

Details: 250 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 250 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.

Propylene Production from Ethylene and Butenes

This report presents the economics of Polymer Grade (PG) Propylene production from ethylene and raffinate-2. The process under analysis consists in a metathesis process similar to Lummus Technology's Olefins Conversion Technology (OCT). The economic analysis performed assumes a plant located in the United States.

Details: 350 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   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.

Propylene Production from Propane (Moving-Bed Reactor)

This study presents the economics of Polymer Grade (PG) Propylene production from propane. The process consists in the dehydrogenation of propane, carried out in a moving-bed reactor, similar to UOP Oleflex. The economic analysis performed assumes a plant located in the United States.

Details: 550 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 550 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.

Adiponitrile Production from Adipic Acid and Ammonia

This report presents the economics of Adiponitrile production from adipic acid and ammonia. In the process examined, adipic acid is reacted with ammonia in the presence of a phosphoric acid based catalyst to generate adiponitrile. The economic analysis performed assumes a plant located in the United States.

Details: 190 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $999 USD

The cost analyses presented in this report target a 190 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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