Commodity Production Costs Report
Hexamethylenediamine Production from Butadiene
Hexamethylenediamine Operating Costs & Plant Construction Costs
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): ?

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.
Report in PDF Format
Download & Explore Anytime
Access in Various Devices
Print & Read Comfortably
Share With Co-workers
Up-to-date Report
Professional report based on Q3 2024 economic data, ensuring timely evaluations.
Multiple Use Cases
Ideal for investment screening, feasibility studies, cost estimates, and research planning.
Proven Methodology
Developed using a consistent methodology honed over a decade, ensuring reliable cost analyses.
Report Editions
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 Adipic Acid
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.
Details: 200 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $1,199 USD

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 | Q3 2024 | 107 pages | Issue C | From $1,199 USD

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 | Q3 2024 | 107 pages | Issue D | From $999 USD
Could Not Find the Report You Need?
Obtain a Bespoke Report
Get a report targeting the process in which you are interested
See Offer Details
Understand Bespoke Reports and how you can easily order them
Check Editions & Pricing
Complete a brief form and see a quotation for your Bespoke Report
Other Related Production Cost Reports

Butadiene Production from Butenes
This study presents the economics of 1,3-Butadiene (BD) production from mixed butenes in a plant assumed to be erected in the United States. In this process, which is similar to TPC/UOP Oxo-D, butenes are catalytically dehydrogenated to produce the Butadiene product. Raffinate is obtained as by-product.
Details: 240 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

Hydrogen Production from Natural Gas (Partial Oxidation Process)
This study provides a techno-economic study of Hydrogen production from natural gas in the United States. In this analysis, natural gas is submitted to a thermal partial oxidation process, producing syngas, which is passed through a shift converter to enrich the Hydrogen output.
Details: 25 MM Nm3/y United States-based plant | Q3 2024 | 107 pages | Issue C | From $799 USD

Nylon 6, 6 Production from Adipic Acid & HMDA (Continuous Process)
This report presents the economics of Nylon 6,6 production from adipic acid and hexamethylenediamine (HMDA) via formation of hexamethylene diamonium adipate salt in the United States. The process analyzed consists of a continuous polycondensation process.
Details: 120 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

Hexamethylene Diisocyanate from HMDA (Non-Phosgene Process)
This report presents a techno-economic analysis of Hexamethylene Diisocyanate (HDI) production from hexamethylene diamine (HMDA) in the United States. The process presented in this report is a non-phosgene process similar to BASF process. Initially, HMDA reacts with urea and butanol generating a carbamate intermediate. Then, the carbamate is thermally cracked producing HDI.
Details: 20 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

Hydrogen Cyanide from Ammonia and Natural Gas (Without Air)
This report provides the economics of Hydrogen Cyanide production in the United States using a direct synthesis method similar to BMA (Blausäure-Methan-Ammoniak) process, which involves the reaction of ammonia and methane (natural gas) without air.
Details: 60 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

Butadiene Production from n-Butane
This report presents the economics of 1,3-Butadiene (BD) production from n-butane. In the process, n-butane undergoes a dehydrogenation reaction process similar to Lummus Catadiene, generating a C4s stream which is purified to obtain 1,3-Butadiene. The economic analysis is based on a plant located in the United States.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD

Hydrogen Production from Natural Gas (Steam Reforming)
This report provides an economic analysis of Hydrogen production from natural gas in the United States using a steam reforming process. Initially, methane present in natural gas is cracked with steam generating syngas. Then, the carbon monoxide from syngas is reacted with steam, producing carbon dioxide and additional hydrogen.
Details: 1000 MM Nm3/y United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD

Hydrogen Cyanide from Ammonia and Natural Gas (With Air)
This study provides the economics of Hydrogen Cyanide production in the United States using a direct synthesis method similar to Andrussow process, which involves the reaction of ammonia, methane (natural gas), and air to produce HCN.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
+800 Reports Developed, Targeting +250 Commodities
Vast Report Library
858 independent and up-to-date reports examining embryonic and established production processes.
Free Sample Reports
Quickly understand the structure and depth of content of our professional reports.