Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 45
ICC - Report ID: 045-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Phenol Production from Cumene
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 045-A,045-B,045-C,045-D
ICC - Related Reports List: 040-B,058-B,049-E,040-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"2":{"1":{"time":"9","price":0},"2":{"time":"4","price":"599"}},"3":{"1":{"time":"11","price":0},"2":{"time":"6","price":"599"}}},"unit":"d"}
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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/045-B.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Phenol</b>. Phenol, also known as hydroxybenzene, is an aromatic compound, comprised of an aromatic ring attached to a hydroxyl group. The major route for phenol production is based on cumene oxidation. Phenol is mainly employed in the manufacturing of bisphenol A (BPA), phenolic resins, Caprolactam and analine.</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 Material</h6> <p><b>Cumene</b>. Cumene is an intermediate chemical for the production of phenol and acetone, two important petrochemicals widely used in several chemical industries. It is produced from benzene and propylene in the liquid phase over an acidic catalyst. </p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/045-B.jpg
ICC - Short Description: This report presents a feasibility analysis of Phenol production from cumene in the United States using a typical hydroperoxidation process. In this process, cumene is oxidized with air to cumene hydroperoxide, which is then cleft to produce Phenol and acetone.
ICC - Main Product: Phenol
ICC - Plant Capacity: 200.00
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Phenol Production from Cumene

Phenol Production Costs Report | Issue B | Q2 2024

Production Cost Report

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Report Details
200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 200 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

Process Consumptions

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

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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 Phenol 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 Phenol 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 Phenol 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 Phenol 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 Phenol Production Cost Reports

Phenol Production from Benzene and Hydrogen Peroxide

This study presents the economics of Phenol production from benzene and hydrogen peroxide in the United States using a process similar to the one proposed by the Council of Scientific and Industrial Research. In this process, benzene is directly oxidized with hydrogen peroxide to Phenol, using a vanadyl pyrophosphate catalyst.

Details: 50 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $999 USD

The cost analyses presented in this report target a 50 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.

Phenol Production from Cumene

This report presents a feasibility analysis of Phenol production from cumene in the United States using a typical hydroperoxidation process. In this process, cumene is oxidized with air to cumene hydroperoxide, which is then cleft to produce Phenol and acetone.

Details: 200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   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.

Phenol Production from Benzene and Propylene

This report presents a feasibility analysis of Phenol production from cumene in the United States using a typical hydroperoxidation process. Initially this process, benzene is subjected to an alkylation reaction with propylene to produce cumene, which is oxidized with air to cumene hydroperoxide. This intermediate is then cleft to yield Phenol and acetone.

Details: 220 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $1,199 USD

The cost analyses presented in this report target a 220 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.

Phenol Production from Toluene

This study reviews the economics of a process producing Phenol from toluene. Initially, toluene is oxidized to benzoic acid intermediate in liquid phase, which is then converted to Phenol in the liquid phase in the presence of cupric and magnesium benzoates. The economic analysis presented assumes a plant constructed in the United States.

Details: 50 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $1,199 USD

The cost analyses presented in this report target a 50 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

Cumene Production from Benzene and PG Propylene

This report presents the economics of Cumene production through the alkylation of benzene with polymer grade (PG) propylene over an acid catalyst. The economic assessment assumes a plant located in the United States.

Details: 250 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   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.

Cumene from Benzene and RG Propylene (Zeolite Catalyst)

This feasibility study reviews Cumene production from benzene and refinery grade (RG) propylene via an alkylation process, which is carried out using a zeolite catalyst. The economic assessment assumes a plant located in the United States.

Details: 300 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 300 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.

Caprolactam Production from Phenol

This feasibility study examines the economics of a process producing Caprolactam from phenol located in the United States. Initially, phenol is hydrogenated to form cyclohexanone. The cyclohexanone is then submitted to an oximation reaction with hydroxylamine. Finally, the cyclohexanone oxime produced is converted to caprolactam by Beckmann rearrangement.

Details: 180 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   From $1,199 USD

The cost analyses presented in this report target a 180 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.

Cyclohexanone Production from Phenol

This report approaches the economics of producing Cyclohexanone from phenol. In the examined process, phenol undergoes a hydrogenation reaction in the liquid phase, in the presence of a palladium-based catalyst, yielding Cyclohexanone. The analysis is based on a plant located in the United States.

Details: 160 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 160 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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