Commodity Production Costs Report
Aniline Production from Phenol
Aniline Operating Costs & Plant Construction Costs
This study reviews the economics of a typical ammonolysis process for Aniline production from phenol. In this process, phenol is transformed into Aniline with ammonia in a fixed-bed reactor. The economic analysis performed is based on a plant constructed in the United States.
The report provides a comprehensive study of Aniline production and related Aniline production cost, covering three key aspects: a complete description of the Aniline production process examined; an in-depth analysis of the related Aniline plant capital cost (Capex); and an evaluation of the respective Aniline plant operating costs (Opex).
The Aniline 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 Aniline 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 Aniline 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): ?
Product
Aniline. Aniline is an important organic compound used primarily in the production of polyurethane foam, rubber processing chemicals, and dyes. Its versatility in chemical synthesis makes it a key intermediate for several industrial applications. Aniline is produced by the hydrogenation of nitrobenzene. It is stored as a liquid at room temperature and requires careful handling due to its toxicity.
Raw Materials
Ammonia. Ammonia (NH3) is one of the most produced synthetic chemicals worldwide. The main application of this world class commodity is in nitrogen fertilizers, followed by the synthesis of nitric acid. It is also used, to a lesser extent, in several other applications such as pulping of wood and as ingredient in household cleaners and drugs. Ammonia is produced basically by the reaction between nitrogen and hydrogen, in a 1:3 stoichiometric ratio. Its production routes are related to the source of the hydrogen used, being steam reforming the main one.
Phenol. Phenol, also known as hydroxybenzene, is an aromatic compound, comprised of an aromatic ring attached to a hydroxyl group. The major route for phenol production is based on cumene oxidation. Phenol is mainly employed in the manufacturing of bisphenol A (BPA), phenolic resins, Caprolactam and analine.
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Aniline 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 Aniline 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 Aniline 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 Aniline 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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Other Aniline Production Cost Reports
Aniline Production from Nitrobenzene (Vapor-Phase Hydrogenation)
This report presents the economics of Aniline production from nitrobenzene and hydrogen in the United States through a process similar to BASF's vapor phase nitrobenzene hydrogenation. In this process, nitrobenzene is reduced to Aniline.
Details: 330 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
Aniline Production from Benzene
This report presents the economics of Aniline production from benzene, nitric acid and hydrogen in the United States. In this report, benzene is nitrated with mixed acid (nitric and sulfuric) to produce mononitrobenzene (MNB). Then, MNB is submitted to a liquid phase hydrogenation, being reduced to Aniline.
Details: 350 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $1,199 USD
Aniline Production from Nitrobenzene (Liquid-Phase Hydrogenation)
This report examines the costs related to the Aniline production from nitrobenzene and hydrogen in the USA. In this process, nitrobenzene is submitted to a liquid phase hydrogenation, being reduced to Aniline.
Details: 350 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD
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Other Related Production Cost Reports
MDI Production from Aniline (Carbonylation Process)
This report presents the economics of Methylene Diphenyl Diisocyanate (MDI) production from aniline and formaldehyde using a typical oxidative carbonylation process located in the USA. In this process, aniline undergoes oxidative carbonylation to give ethyl phenylcarbamate (EPC). Then, the EPC reacts with formaldehyde to form diphenylene diurethane (MDU). Finally, MDU is thermally decomposed to MDI.
Details: 50 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $1,199 USD
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
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
MDI Production from Aniline (Phosgenation Process)
This study presents the costs associated with the construction of a plant producing MDI from aniline and formaldehyde in the USA. In this study aniline reacts with formaldehyde to form a mixture of diphenyl methane diamine and polymeric amines. Then, this mixture reacts with phosgene to produce MDI and polymeric MDI. The phosgene used is generated from chlorine in an on-site unit.
Details: 50 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $1,499 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
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