Commodity Production Costs Report
Diphenyl Carbonate from Phosgene and Phenol
Diphenyl Carbonate Operating Costs & Plant Construction Costs
This report presents the economics of Diphenyl Carbonate (DPC) production from phosgene and phenol using a typical interfacial process. The economic assessment assumes a plant located in the United States.
The report provides a comprehensive study of Diphenyl Carbonate production and related Diphenyl Carbonate production cost, covering three key aspects: a complete description of the Diphenyl Carbonate production process examined; an in-depth analysis of the related Diphenyl Carbonate plant capital cost (Capex); and an evaluation of the respective Diphenyl Carbonate plant operating costs (Opex).
The Diphenyl Carbonate 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 Diphenyl Carbonate 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 Diphenyl Carbonate 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
Diphenyl Carbonate. Diphenyl Carbonate (a.k.a. DPC, Phenyl Carbonate) is a phenol derivative, classified as an acyclic carbonate ester. It appears as a white crystalline solid, insoluble in water, but soluble in acetone, hot alcohol, benzene, carbon tetrachloride, ether, glacial acetic acid and other organic solvents. The main production route of DPC is the phosgenation of phenol, in the presence of catalysts of salts of Aluminum, Titanium, Tin, Zinc, or Iron. Another possible route, one that is being studied and otimized, is the oxidative carbonylation of phenol, carried out in the presence of paladium compounds.
Raw Materials
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.
Phosgene. Phosgene is a highly reactive and toxic gas used in the production of polyurethanes, polycarbonates, and various chemical intermediates. It is a key raw material in isocyanate production, which is essential for creating durable plastics and coatings. Phosgene is produced by reacting carbon monoxide with chlorine and is typically stored as a compressed gas. Despite its hazardous nature, it remains indispensable in polymer manufacturing due to its efficiency in forming strong carbonyl bonds.
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Ideal for investment screening, feasibility studies, cost estimates, and research planning.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Diphenyl Carbonate 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 Diphenyl Carbonate 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 Diphenyl Carbonate 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 Diphenyl Carbonate 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 Diphenyl Carbonate Production Cost Reports
Diphenyl Carbonate from Ethylene Oxide and Phenol
This study reviews the costs associated with Diphenyl Carbonate (DPC) production from ethylene oxide and phenol in the United States. The process examined is similar to Asahi Kasei process, which dimethyl carbonate (DMC) intermediate is initially produced from ethylene oxide and methanol. Then, the DMC reacts with phenol to produce phenylmethyl carbonate, followed by disproportionation to DPC.
Details: 130 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $1,199 USD
Diphenyl Carbonate from Phenol and Methanol (DMO Intermediate)
This report presents a techno-economic study about Diphenyl Carbonate (DPC) production from phenol and methanol in the United States. This process is similar to Ube process. Initially, methanol is submitted to oxidative coupling to produce dimethyl oxalate (DMO). The DMO is then transesterified with phenol to diphenyl oxalate, which undergoes decarbonylation to DPC.
Details: 130 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $1,199 USD
Diphenyl Carbonate from Phenol and Methanol (DMC Intermediate)
It presents the economics of Diphenyl Carbonate (DPC) production from phenol and methanol using a process similar to the one proposed by SABIC, located in the United States. In this process, methanol undergoes an oxidative carbonylation to form dimethyl carbonate (DMC). It reacts with phenol to produce phenylmethyl carbonate, followed by disproportionation to DPC.
Details: 130 kta United States-based plant | Q3 2024 | 107 pages | Issue D | From $1,199 USD
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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
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
Phosgene Production
This report presents the costs associated with the construction of a plant producing Phosgene from chlorine and carbon monoxide over activated carbon in the United States.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
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