Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 193
ICC - Report ID: 193-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Hexamethylenediamine Production from Adipic Acid
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 193-A,193-C,193-D
ICC - Related Reports List: 019-A,019-B,070-A,223-B,197-B,246-C,246-A,070-B
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"1199","2":"1199","3":"1199"},"2":{"1":"1999","2":"1999","3":"1999"},"3":{"1":"3399","2":"3399","3":"3399"}},"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/193-B.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>HMDA</b></p></b></p> <h6>Raw Materials</h6> <p><b>Hydrogen</b></p>, <p><b>Chemicals</b></p>, <p><b>Fiber Grade Adipic Acid</b></p>, <p><b>Ammonia</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/193-B.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Adiponitrile Formation; (2) Adiponitrile Separation; (3) Hydrogenation; and (4) HMDA Purification</p><p>Adiponitrile Formation. Adipic acid, ammonia, and phosphoric acid are fed to a reactor, where the adipic acid reacts with ammonia generating ammonium adipate salt, which is subsequently dehydrated in the presence of phosphoric acid to produce adiponitrile. The reactor effluent is fed to a gas-liquid separator.The liquid phase is sent to an evaporator coupled to the reactor to recover the catalyst and unreacted adipic acid while removing heavy impurities. The gas phase is sent to a distillation column from which the a crude adiponitrile stream is separated as a side product. The column bottoms stream, which is comprised of reaction intermediates, is recycled to the reactor and a top stream of water, ammonia and light impurities is sent to an ammonia recovery area for recycling the ammonia back to the reactor and discarding light ends and water.</p><p>Adiponitrile Separation. The crude adiponitrile stream is passed through a fixed-bed reactor packed with a silica-alumina catalyst to convert the hard to separate 2-cyanocyclopentylideneimine (CPI) impurity into a lighter substance. After that, two distillation steps follow to remove light and heavy impurities. Purified adiponitrile is routed to the hydrogenation section.</p><p>Hydrogenation. Adiponitrile, fresh, and recycle hydrogen are fed to a “gas-lift” reactor, where they quickly react on the surface of RaneyTM nickel catalysts yielding Hexamethylenediamine (HMDA). High catalyst concentrations are used to keep the concentration of unreacted nitriles very low. Water and caustic soda are fed to the reactor to make up for losses leaving in the crude HMDA.</p><p>HDMA Purification. Crude HMDA is passed through a distillation train, to remove water, 1,2-diaminocyclohexane (DCH), and high boilers. DCH is still sent to a column before it is purged, in which residual HDMA is recovered.</p>
ICC - Short Description: This report presents the economics of Hexamethylenediamine (HMDA) production from adipic acid. In the process examined, adipic acid is reacted with ammonia, forming ammonium adipate and adipamide, which are then dehydrated to adiponitrile intermediate. The adiponitrile is finally hydrogenated to HMDA. The economic analysis performed assumes a plant located in the United States.
ICC - Main Product: Hexamethylenediamine
ICC - Plant Capacity: 200.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Hexamethylenediamine Production from Adipic Acid

Hexamethylenediamine Production Costs Report | Issue B | Q2 2024

Production Cost Report

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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

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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

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Hexamethylenediamine 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 Hexamethylenediamine 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 Hexamethylenediamine 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 Hexamethylenediamine 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 Hexamethylenediamine Production Cost Reports

Hexamethylenediamine Production from Butadiene

This report presents the economics of Hexamethylenediamine (HMDA) production from butadiene. In the process examined, butadiene is reacted with hydrogen cyanide to generate adiponitrile intermediate, which is then hydrogenated to HMDA. The economic analysis performed assumes a plant located in the United States.

Details: 200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $1,199 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.

Hexamethylenediamine Production from Acrylonitrile

This report presents the economics of Hexamethylenediamine (HMDA) production from acrylonitrile. In the process examined,acrylonitrile is electrodimerized, followed by hydrogenation, yielding adiponitrile intermediate. The adiponitrile is then hydrogenated to HMDA. The economic analysis is based on a plant constructed in the United States.

Details: 200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $1,199 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.

Hexamethylenediamine Production from Adiponitrile

This report presents the economics of Hexamethylenediamine (HMDA) production from adiponitrile. In the process examined, adiponitrile is hydrogenated to HMDA. The economic analysis is based on a plant constructed in the United States.

Details: 200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $999 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.

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