Commodity Production Costs Report

Hexamethylenediamine Production from Butadiene

Hexamethylenediamine Operating Costs & Plant Construction Costs

200 kta United States-based plant | 107 Pages | Issue A | Q3 2024
Starting at $1,199 USD | See Report Editions Prices

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.

The report provides a comprehensive study of Hexamethylenediamine production and related Hexamethylenediamine production cost, covering three key aspects: a complete description of the Hexamethylenediamine production process examined; an in-depth analysis of the related Hexamethylenediamine plant capital cost (Capex); and an evaluation of the respective Hexamethylenediamine plant operating costs (Opex).

The Hexamethylenediamine production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Hexamethylenediamine plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Hexamethylenediamine plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.

Key reference(s): ?

Hexamethylenediamine Production Cost Report Process Schematic

The process under analysis comprises four major sections: (1) Hydrocyanation; (2) Adiponitrile Separation; (3) Hydrogenation; and (4) HDMA Purification.

Hydrocyanation. In the first reaction stage, butadiene is fed to the reactor, along with hydrogen cyanide. This reaction produces different isomers of pentenenitriles and branched butenenitriles. Catalyst and unconverted reactants are separated from reaction mixture and recycled to the reactor. As the hydrocyanation of branched butene nitriles does not yield adiponitrile, they must also be separated from linear nitriles prior to second hydrocyanation step. Separation is accomplished in a distillation column and separated branched nitriles are further treated for recovery of 2-methyl-3-butenenitrile (2M3BN). 2M3BN is fed into an isomerization reactor, where it is converted to useful 3-pentenenitrile (3PN), which is mixed with the linear pentenenitriles previously obtained and fed to the second hydrocyanation reactor. The reactor is also fed with fresh HCN, as well as fresh and recycled catalyst solution. Adiponitrile is the main product formed in the reaction, but some yield losses may occur due to the formation of by-products.

Adiponitrile Separation. First, catalyst is separated from reaction mixture and recycled to the reactor. The product stream is passed through three distillation steps to recover mononitriles, dinitriles and dimers as well as other high boiling compounds. Purified adiponitrile is routed to the hydrogenation section.

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 so as to make up for losses leaving in the crude HMDA.

HDMA Purification. Crude HMDA is passed through a distillation train, so as to remove water, 1,2-diaminocyclohexane (DCH) and high boilers. DCH is still sent to a column, in which residual HDMA is recovered, before it is purged.

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 90 Pages | 28 Tables | 13 Images

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Table of Contents


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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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  • 107 Pages | 34 Tables | 22 Images
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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

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