Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: J
ICC - Volume: 36
ICC - Report ID: 036-J
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Benzene Production from Naphtha
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-H,036-I,036-A,036-B,036-F
ICC - Related Reports List: 293-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":"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/036-J.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Benzene</b></p>, <p><b>Gasoline</b></p>, <p><b>Paraxylene</b></p>, <p><b>LPG</b></p> <h6>Raw Materials</h6> <p><b>Naphtha</b></p>, <p><b>Chemicals</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/036-J.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Naphta Hydrotreatment & Reforming; (2) Aromatics Separation; (3) Toluene Disproportionation; (4) Paraxylene Recovery</p><p>Naphta Hydrotreatment & Reforming. Initially, the naphtha feedstock is treated with hydrogen under high temperature and pressure conditions to remove impurities that act as poison for the catalysts downstream. The treated naphtha is then sent to catalytic reforming, where paraffins and naphthenes are converted to aromatics. The product from reforming is then sent to the aromatics separation section.</p><p>Aromatics Separation. The reformate is fed to a reformate splitter, where a C7- fraction is obtained as the top product and a C8+ heavier fraction as the bottom product. The C7- fraction is fed to a sulfolane extraction unit for aromatics recovery. The aromatic extract is sent to a column to recover the Benzene as the top product. The bottom of this column is fed to a second column where toluene is separated as distillate, while the bottom stream is fed to the xylene splitter, where xylenes are separated as the top product from C9+ aromatics, that exit from the bottom. These heavy aromatics are fed to a fourth column, where a C9 fraction is produced as overhead and then mixed with the toluene stream to be sent to the toluene disproportionation section.</p><p>Toluene Disproportionation. The toluene and C9 aromatics mix is then fed to a reactor to be converted into xylenes and benzene via disproportionation reaction. The product from the disproportionation unit is then recycled to the benzene column.</p><p>Paraxylene Recovery. The mixed xylenes produced as the top product of the xylene splitter are fed to an adsorption unit, where paraxylene is separated and purified. The separated raffinate stream is fed to an isomerization step, where ortho- and metaxylene, as well as ethylbenzene, are isomerized into paraxylene. The reactors effluent is sent to the deheptanizer, where C7 and lighter components are removed as the overhead product, while a mixed xylenes stream exits from the bottom and returns to the xylene splitter.</p>
ICC - Short Description: This study provides the economics of Benzene production from naphtha in the United States using an integrated aromatics complex, which involves the co-production of p-Xylene. In this process, naphtha is reformed, and the reformate is separated into Benzene, xylenes and toluene, which undergoes disproportionation, forming the other two products.
ICC - Main Product: Benzene
ICC - Plant Capacity: 450.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Benzene Production from Naphtha

Benzene Production Costs Report | Issue J | Q4 2024

Production Cost Report

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450 kta United States-based plant   |   Q4 2024   |   107 pages

This report presents a cost analysis of a 450 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

Process Consumptions

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Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

Plant Cost Breakdowns

Plant Capacity Assessment

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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   |   Q4 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 Production from Toluene & Heavy Aromatics

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).

Details: 250 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue H   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

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   |   Q4 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   |   Q4 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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