Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 338
ICC - Report ID: 338-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Paracetamol Production from Nitrobenzene
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 338-A,338-C,338-D
ICC - Related Reports List: 293-B,010-B,070-A,070-B,293-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"5","price":0},"2":{"time":"2","price":"299"}},"2":{"1":{"time":"5","price":0},"2":{"time":"2","price":"299"}},"3":{"1":{"time":"7","price":0},"2":{"time":"4","price":"299"}}},"unit":"d"}
ICC - Prices: {"versions":{"1":{"1":"1999","2":"1999","3":"1999"},"2":{"1":"2999","2":"2999","3":"2999"},"3":{"1":"4799","2":"4799","3":"4799"}},"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/338-B.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Paracetamol</b></p>, <p><b>Acetic Acid</b></p>, <p><b>Aniline</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Ammonia</b></p>, <p><b>Sulfuric Acid</b></p>, <p><b>Nitrobenzene</b></p>, <p><b>Acetic Anhydride</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/338-B.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Nitrobenzene reduction; (2) PAP separation and purification; (3) PAP acetylation; and (4) Paracetamol purification</p><p>Nitrobenzene reduction. The nitrobenzene (NB) is reacted with hydrogen in the presence of sulfuric acid and a platinum on activated carbon catalyst to produce p-aminophenol (PAP). Besides PAP, o-aminophenol, aniline and 4,4'-diaminodiphenyl ether are also generated as by-products. The reaction is stopped before depletion of NB so two phases are present at the end. An organic phase, comprised of unreacted NB and the catalyst, which is recycled back to the reactor, and an aqueous phase containing PAP and by-products.</p><p>PAP separation and purification. The aqueous phase is fed to the middle of an extraction column. An aniline-toluene mixture is used to extract the 4,4'-diaminodiphenyl ether. An aqueous sulfuric acid solution is fed at the top of the column to recover PAP extracted. Toluene is fed to the bottom of the column to extract the aniline from the aqueous PAP solution. Aniline is recovered from the top organic stream to be sold as by-product. The bottom aqueous stream is fed to a crystallizer, to purify the PAP, which is then centrifuged and dried.</p><p>PAP acetylation. The PAP is dissolved in an acetic acid solution and fed to a reactor along with acetic anhydride. An acetylation reaction is carried out by heating the mixture of PAP with acetic anhydride, yielding crude Paracetamol.</p><p>Paracetamol purification. The crude Paracetamol is treated with decolorizing charcoal. The product is further purified by crystallization/centrifugation steps, and subsequently dried, ground under a dry air atmosphere, packed and stored. The liquor separated during centrifugation is sent to extraction step to recover acetic acid, as by-product.</p>
ICC - Short Description: This report approaches the production of Paracetamol from nitrobenzene and acetic anhydride in the United States. In this process, nitrobenzene is contacted with hydrogen in the presence of dilute sulfuric acid, generating 4-aminophenol (PAP) and aniline by-product. The PAP is then acetylated to produce Paracetamol.
ICC - Main Product: Paracetamol
ICC - Plant Capacity: 20.00
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ICC - Images Count: {"versions":{"1":"9","2":"13","3":"22"}}
ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Paracetamol Production from Nitrobenzene

Paracetamol Production Costs Report | Issue B | Q4 2024

Production Cost Report

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

This report presents a cost analysis of a 20 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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Production Costs Datasheet

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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 Paracetamol 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 Paracetamol 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 Paracetamol 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 Paracetamol 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

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Details: 20 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue A   From $1,999 USD

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Acetic Anhydride Production from Acetic Acid and Acetone

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The cost analyses presented in this report target a 800 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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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.

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