Commodity Production Costs Report
BPA from Acetone and Phenol (Ion-Exchange Resin Catalyst)
Bisphenol A Operating Costs & Plant Construction Costs
This report presents a techno-economic analysis of Bisphenol A (BPA) production in the United States, via a process similar to Dow's QBIS technology. In this process, BPA is produced by the reaction of acetone with phenol catalyzed by a cation-exchange resin.
The report provides a comprehensive study of Bisphenol A production and related Bisphenol A production cost, covering three key aspects: a complete description of the Bisphenol A production process examined; an in-depth analysis of the related Bisphenol A plant capital cost (Capex); and an evaluation of the respective Bisphenol A plant operating costs (Opex).
The Bisphenol A 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 Bisphenol A 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 Bisphenol A 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
BPA. Bisphenol A is a high volume production organic compound, synthesized from phenol and acetone. It has been produced in commercial since the 1950's and is mostly used in the production of polycarbonate plastic and epoxy resins. Nowadays its use in products with contact with food has been decreasing, mostly in the United States, due to a rising concern on the negative health effects it might cause.
Raw Materials
Acetone. Acetone, also known as 2-propanone, is the simplest ketone. It is used as solvent for a wide range of organic compounds (e.g. oils, fats, resins, waxes and gums). It is also used as feedstock for the production of several chemicals, such as methyl methacrylate, bisphenol A, and methyl isobutyl ketone. The main source of acetone is the process for phenol production from cumene, which generates acetone as by-product at an approximate ratio for 0.6 kg of acetone per kg of phenol. Industrial consumers of acetone usually receive shipments in large containers made of carbon steel, tank trucks made of stainless steel or aluminum, or rail tank cars made of carbon steel or aluminum. International shipments by sea are usually made in steel barges and amount at least 2,000 metric tons.
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 Bisphenol A 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 Bisphenol A 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 Bisphenol A 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 Bisphenol A 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 Bisphenol A Production Cost Reports
BPA from Acetone and Phenol (Hydrogen Chloride Catalyst)
This report presents the economics of Bisphenol A (BPA) production in the United States via a condensation reaction of acetone with phenol catalyzed by hydrogen chloride.
Details: 30 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
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Other Related Production Cost Reports
Polycarbonate Production from BPA and DPC
This study presents the economics of Polycarbonate (PC) production from bisphenol A (BPA) and diphenyl carbonate (DPC) in the United States, via a typical melt process. In this process, DPC is transesterified with BPA to form PC and phenol as by-product. The reaction is conducted in oligomerization and polymerization.
Details: 200 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 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
Acetone Production from Isopropanol
This feasibility study presents the economics of Acetone production from isopropanol using a liquid phase dehydrogenation process. The economic analysis presented in the study assumes a plant located in the United States.
Details: 30 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $999 USD
Acetone Production from Propylene (Single-Step Process)
This report approaches the economics of Acetone production from propylene in the United States. In the process examined, a direct propylene oxidation is carried out in the presence of palladium chloride and copper chloride, yielding Acetone.
Details: 80 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $999 USD
Polycarbonate Production from BPA and Phosgene
This report presents the economics of Polycarbonate (PC) production from bisphenol A (BPA) and phosgene in the United States, via a typical interfacial process. In this process, BPA, dissolved in a caustic soda solution, is reacted with phosgene, in an organic solution, at the interface of the two phases. The carbonate oligomers produced are then polycondensed to Polycarbonate.
Details: 200 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
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