Commodity Production Costs Report
Caprolactam Production from Phenol
Caprolactam Operating Costs & Plant Construction Costs
This feasibility study examines the economics of a process producing Caprolactam from phenol located in the United States. Initially, phenol is hydrogenated to form cyclohexanone. The cyclohexanone is then submitted to an oximation reaction with hydroxylamine. Finally, the cyclohexanone oxime produced is converted to caprolactam by Beckmann rearrangement.
The report provides a comprehensive study of Caprolactam production and related Caprolactam production cost, covering three key aspects: a complete description of the Caprolactam production process examined; an in-depth analysis of the related Caprolactam plant capital cost (Capex); and an evaluation of the respective Caprolactam plant operating costs (Opex).
The Caprolactam 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 Caprolactam 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 Caprolactam 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 4 major sections: (1) Cyclohexanone production; (2) Oximation & Beckmann rearrangement; (3) Caprolactam purification; and (4) Ammonium sulfate recovery.
Cyclohexanone production. Fresh phenol is distilled, removing heavy impurities. It is fed to stirred reactors operating in series with compressed hydrogen. The reaction takes place in the liquid phase, catalyzed by palladium on carbon, yielding cyclohexanone. Purified cyclohexanone is obtained after the reactor outlet is passed through centrifugation and distillation steps.
Oximation & Beckmann rearrangement. Ammonia is oxidized yielding nitric oxide, which is absorbed in water and then hydrogenated over a palladium catalyst, in the presence of dilute sulfuric acid, producing hydroxylammonium sulfate solution. The hydroxylammonium sulfate solution reacts with purified cyclohexanone in stirred reactors, in toluene solvent, to form cyclohexanone oxime. The solution containing cyclohexanone oxime is then distilled for the removal of toluene solvent. Finally, the cyclohexanone oxime is converted to caprolactam by Beckmann rearrangement, in the presence of oleum.
Caprolactam purification. The product of rearrangement is subjected to purification steps, involving neutralization, extraction in the presence of toluene and light impurities removal. The raw caprolactam melt is transformed into crystals that are melted, solidified on cold surface and the flakes produced are packed and sent to storage facilities.
Ammonium sulfate recovery. Ammonium sulfate solution removed in neutralization steps is concentrated by means of evaporation. Then, it is crystallized, centrifuged and dried.
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 Caprolactam 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 Caprolactam 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 Caprolactam 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 Caprolactam 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
Preview our Production Cost Reports
Other Caprolactam Production Cost Reports
Caprolactam from Cyclohexane (Oximation with Hydroxylamine)
This report presents the economics of Caprolactam production from cyclohexane located in the United States. Initially, cyclohexane is oxidized to a cyclohexanol/cyclohexanone. Then, the cyclohexanol is hydrogenated to cyclohexanone, which is submitted to an oximation reaction with hydroxylamine. Finally, the cyclohexanone oxime produced is converted to Caprolactam by Beckmann rearrangement.
Details: 180 kta United States-based plant | Q3 2024 | 107 pages | Issue D | From $1,199 USD
Caprolactam Production from Butadiene and Hydrogen Cyanide
This feasibility study shows the economics of a Caprolactam production process from butadiene and hydrogen cyanide based on an industrial plant located in the United States. Hexamethylenediamine (HMDA) is generated as by-product in the process under analysis.
Details: 180 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $1,199 USD
Caprolactam Production from Butadiene, CO, Hydrogen and Ammonia
This report presents the cost associated with a plant located in the United States producing Caprolactam from butadiene, carbon monoxide, hydrogen, and ammonia. The process under analysis involves the following steps: reaction of carbon monoxide with butadiene; hydrocarbonylation; amination and cyclization.
Details: 180 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $1,499 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
Phenol Production from Cumene
This report presents a feasibility analysis of Phenol production from cumene in the United States using a typical hydroperoxidation process. In this process, cumene is oxidized with air to cumene hydroperoxide, which is then cleft to produce Phenol and acetone.
Details: 200 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD
Ammonia Production from Natural Gas (Combined Reforming)
This report presents the economics of Ammonia production from natural gas in the United States using a process similar to KBR Purifier process. In the process examined, syngas is initially produced from natural gas via a combined reforming. The syngas is purified through several steps into nitrogen and hydrogen which are synthesized to ammonia.
Details: 800 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $1,199 USD
Nylon 6 Production from Caprolactam (Batch Process)
This report presents the economics of Nylon 6 production from caprolactam. The typical process analyzed consists of a batch ring-opening polymerization of caprolactam via the hydrolytic mechanism. The economic assessment assumes a plant located in the United States.
Details: 65 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
Phenol Production from Benzene and Hydrogen Peroxide
This study presents the economics of Phenol production from benzene and hydrogen peroxide in the United States using a process similar to the one proposed by the Council of Scientific and Industrial Research. In this process, benzene is directly oxidized with hydrogen peroxide to Phenol, using a vanadyl pyrophosphate catalyst.
Details: 50 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $999 USD
Ammonia Production from Syngas
This report presents the economics of Ammonia production from synthesis gas (syngas). In this process, hydrogen, recovered from syngas feedstock, and nitrogen, recovered from air, react producing Ammonia. The economic analysis performed assumes a plant located in the United States.
Details: 800 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
Nylon 6 Production from Caprolactam (Continuous Process)
This report presents the economics of Nylon 6 production from caprolactam in the United States. The process examined is a typical continuous ring-opening polymerization of caprolactam via the hydrolytic mechanism, carried out in two stages, similar to technologies developed/licensed by Thyssenkrupp (Uhde Inventa-Fischer) and Air Liquide (Lurgi Zimmer). An aminoacid is the intermediate for condensation.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue B | 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.