Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: C
ICC - Volume: 36
ICC - Report ID: 036-C
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Benzene Production from Pygas (Extractive Distillation Process)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 036-D,036-E,036-G,036-H,036-I,036-J,036-A,036-B,036-F
ICC - Related Reports List: 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-C.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Benzene</b></p>, <p><b>Crude C5s</b></p>, <p><b>Crude C7+</b></p>, <p><b>Crude C6</b></p> <h6>Raw Materials</h6> <p><b>Pygas</b></p>, <p><b>Chemicals</b></p>, <p><b>Hydrogen</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/036-C.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Benzene Purification; and (2) Hydrogen Purification.</p><p>Benzene Purification. First, the pyrolysis gasoline, a hydrocarbons stream with carbon chains ranging from C5 to C12, is separated into three hydrocarbons cut. Both the light and heavy cuts are sold to nearby facilities. The intermediate cut, containing C6 hydrocarbons, is then fed with hydrogen to a pretreatment reactor. There, diolefinic material in the pyrolysis gasoline is hydrotreated in the presence of catalysts (cobalt molybdate on alumina). The diolefins in the pyrolysis gasoline feed are converted to olefins, which are then saturated. Also, thiophene and other sulfur compounds in the pyrolysis gasoline are converted to H2S. The regenerated aromatic stream is subjected to a extractive distillation. In the extractive distillation process, N-formylmorpholine (NFM) is mixed with the feed stream in order to alter the vapour pressure of the components to be separated. The solvent lowers the vapour pressure of benzene in the feed stream more than the other non-aromatic hydrocarbons. Given the shift in the vapour pressures, benzene is recovered alongside with the solvent fed to column. The rich-benzene solvent is fed to a stripping column to recover the solvent, through the column's bottom, and benzene, through the column's top.</p><p>Hydrogen Purification. Hydrogen stream is fed to the bottom of a multi-stage absorber column. The absorption is conducted in a counter-current flow. The purpose is to remove residual hydrocarbons from the hydrogen-rich feed stream, avoiding the build-up of impurities in the process. The washed hydrogen-rich gas is compressed and heated, before being directed to pretreatment reactor.</p>
ICC - Short Description: 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.
ICC - Main Product: Benzene
ICC - Plant Capacity: 250.00
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Benzene Production from Pygas (Extractive Distillation Process)

Benzene Production Costs Report | Issue C | Q3 2024

Production Cost Report

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250 kta United States-based plant   |   Q3 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

Plant Capital Cost Summary

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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

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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 (Selective Toluene Disproportionation)

It presents the economics of a selective toluene disproportionation process (STDP) for Benzene production in the United States. In the STDP, toluene is converted into benzene and xylenes (mainly, p-xylene). The reaction is carried out with a zeolitic catalyst, in a hydrogen atmosphere to minimize coke formation and side reactions.

Details: 250 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   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 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   |   Q3 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

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.

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   |   Q3 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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