Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: H
ICC - Volume: 36
ICC - Report ID: 036-H
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Benzene Production from Toluene & Heavy Aromatics
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 036-C,036-D,036-E,036-G,036-I,036-J,036-A,036-B,036-F
ICC - Related Reports List: 039-A,039-B,047-A,293-A
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/036-H.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Benzene</b></p>, <p><b>Mixed Xylenes</b></p>, <p><b>C10+ Aromatics</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Toluene</b></p>, <p><b>C9 Aromatics</b></p>, <p><b>Hydrogen</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/036-H.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Transalkylation; and (2) Fractionation.</p><p>Transalkylation. Fresh toluene and heavy aromatics feeds, toluene and heavy aromatics recovered downstream, fresh hydrogen and hydrogen-rich recycle gas are combined and preheated by heat-exchange with effluent from reactor. Subsequently, the feed stream is fed to a fired heater, where it is vaporized and raised to the reaction temperature. The feed stream is sent down-flow over a fixed bed of zeolitic catalyst, where the transalkylation / disproportionation reactions take place. The reactions yield a mixture composed primarily of benzene, toluene and mixed xylenes. The effluent from the reactor is cooled in such a way that substantially all of the hydrocarbons boiling above methane are condensed.</p><p>Fractionation. The liquid stream containing Benzene and other transalkylation / disproportionation reaction products, as well as entrained hydrogen, is routed to a gas-liquid separator, in which the hydrogen is removed. The gaseous stream is compressed and mixed to fresh hydrogen. The liquid effluent is fed to a column in which remaining gas and low-boiling hydrocarbons are stripped off from the stream. The aromatics concentrate is then submitted to a clay treatment, in such a way that impurities (e.g. trace olefins) are removed by polymerization and absorption. The treated stream is passed through a series of four distillation columns, where benzene, toluene, concentrated xylenes and C9 and C10 Aromatics are recovered. Toluene and C9 Aromatics are recycled.</p>
ICC - Short Description: This report shows the costs associated with Benzene production from toluene and heavy aromatics in the United States using a typical transalkylation process. In this process, toluene and heavy aromatics are converted to Benzene and xylenes (co-product).
ICC - Main Product: Benzene
ICC - Plant Capacity: 250.00
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Benzene Production from Toluene & Heavy Aromatics

Benzene Production Costs Report | Issue H | Q2 2024

Production Cost Report

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250 kta United States-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 250 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 Benzene 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 Benzene 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 Benzene 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 Benzene 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 Benzene Production Cost Reports

Benzene from Toluene (Conventional Toluene Disproportionation)

This report also presents the economics of Benzene production from toluene in the United States. This assessment depicts a conventional toluene disproportionation process (TDP).

Details: 400 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue F   From $799 USD

The cost analyses presented in this report target a 400 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 from Toluene (Hydrodealkylation)

This study presents the economic analysis for the construction of an industrial plant for Benzene production from toluene in the United States. This study reviews a toluene hydrodealkylation (THDA) technology similar to Houdry's Detol. In this process, toluene is converted over a fixed-bed catalyst into Benzene.

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

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Other Related Production Cost Reports

Toluene Production from Reformate

This report presents the economics of Toluene production from reformate. The reformate is submitted to a typical sulfolane liquid-liquid extraction, giving a mixture of aromatics, which is further processed to yield pure Toluene. Benzene and mixed xylenes are produced as by-products. The economic analysis presented is based on a plant constructed 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.

Toluene Production from Pygas

This study presents the economics of Toluene production from pyrolysis gasoline (pygas) in the United States using a typical liquid-liquid extraction process.

Details: 400 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 400 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 (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   |   Q2 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.

Nitrobenzene Production from Benzene (NORAM)

This report presents the economics of Nitrobenzene production from benzene and nitric acid in the United States. The process analyzed in this report is similar to NORAM's adiabatic benzene nitration process, which uses a plug-flow nitrator containing jet-impingement elements.

Details: 530 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 530 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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