Polycarbonate Production from BPA, Phenol and Phosgene
Polycarbonate Production Costs Report | Issue H | Q3 2024
| Report Details |
| 150 kta United States-based plant | Q3 2024 | 107 pages |
This report presents a cost analysis of a 150 kta (kilo metric ton per annum) United States-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.
Report Abstract
It presents the economics of Polycarbonate (PC) production from bisphenol A (BPA), phenol and phosgene in the United States, via a typical melt process integrated with a diphenyl carbonate (DPC) production unit. Initially, phenol is phosgenated to produce DPC. Then, the DPC is transesterified with BPA and polycondensed to generate PC.
The report provides a comprehensive study of Polycarbonate production and related Polycarbonate production cost, covering three key aspects: a complete description of the Polycarbonate production process examined; an in-depth analysis of the related Polycarbonate plant capital cost (Capex); and an evaluation of the respective Polycarbonate plant operating costs (Opex).
The Polycarbonate 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 Polycarbonate 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 Polycarbonate plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic
The process under analysis comprises four major sections: (1) DPC synthesis; (2) DPC purification; (3) Polymerization; (4) Polycarbonate finishing.
Diphenyl carbonate synthesis. Initially, phenol is reacted with phosgene to produce diphenyl carbonate (DPC). The phosgenation reaction is carried out in three fixed bed reactors filled with gamma-alumina connected in series. The product from phosgenation mainly containing phenol and diphenyl carbonate is directed to the DPC purification. The waste gas coming from the phosgenation, mostly containing HCl and inert gases, is fed to a HCl recovery unit, where hydrochloric acid with a concentration of 32 wt% is obtained as by-product.
DPC purification. The effluent from the DPC synthesis is fed to a set of distillation columns for the purification of diphenyl carbonate and recovery of unconverted phenol, which is recycled to the DPC synthesis.
Polymerization. Purified diphenyl carbonate, bisphenol A and sodium dihydrogen phosphite are mixed and heated to form a melt, which is subsequently fed to a oligomerization step, where low molecular weight oligomers are generated. The oligomers are directed to more severe conditions, then polymerization is completed in two CSTR operating in series. Polymerization is interrupted by addition of n-butyl tosylate, which deactivates the catalyst. Phenol and other by-products are continuously removed and sent to a distillation column, where phenol is withdrawn from overhead and recycled to the DPC synthesis.
Polycarbonate finishing. The polymer melt is filtered, and a mix of additives is added. The mixture is homogenized and pelletized. Finally, the Polycarbonate pellets are conveyed to homogenization system and fed to the packing system.
Up-to-date PDF 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.
Compact
$1,199 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Pages | Tables | Images
Read-only Online PDF Format
Updated with Q3 2024 Data
DETAILED
$1,999 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Pages | Tables | Images
Downloadable PDF Format
Updated with Q3 2024 Data
PREMIUM
MOST POPULAR
$3,399 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Plant Cost Breakdowns
Plant Capacity Assessment
Process Flow Diagrams
Costs in Different Countries Add-on
Pages | Tables | Images
Print-enabled PDF Format Add-on
Updated with Q3 2024 Data
Share with Co-workers
Technical Support via Email
Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Polycarbonate 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 Polycarbonate 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 Polycarbonate 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 Polycarbonate 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 Polycarbonate Production Cost Reports
Polycarbonate Production from Phenol & Acetone
This report analyses the economics of Polycarbonate (PC) production from phenol, acetone and phosgene in the United States. Initially, BPA is manufactured by condensation of phenol with acetone. Then, BPA is reacted with phosgene at the interface of a two-phase mixture. The carbonate oligomers produced are then polycondensed to Polycarbonate resin.
Details: 250 kta United States-based plant | Q3 2024 | 107 pages | Issue E From $1,199 USD
The cost analyses presented in this report target a 250 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
Polycarbonate Production from Phenol, Acetone and Methanol
This report presents the economics of Polycarbonate (PC) production from phenol, acetone, and methanol in the United States. BPA is manufactured by condensation of phenol with acetone. To form diphenyl carbonate (DPC), methanol is carbonylated producing dialkyl carbonate which is reacted with phenol. The DPC and BPA are transesterified and polycondensed to generate PC.
Details: 150 kta United States-based plant | Q3 2024 | 107 pages | Issue F From $1,499 USD
The cost analyses presented in this report target a 150 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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 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
The cost analyses presented in this report target a 50 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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
The cost analyses presented in this report target a 200 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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
The cost analyses presented in this report target a 30 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
BPA from Acetone and Phenol (Ion-Exchange Resin Catalyst)
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.
Details: 200 kta United States-based plant | Q3 2024 | 107 pages | Issue B From $799 USD
The cost analyses presented in this report target a 200 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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
The cost analyses presented in this report target a 100 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
+800 Reports Developed, Targeting +250 Commodities
Best-in-Class Reports
Analysis of capital and operating costs of commodity production processes. Prices starting at $799 USD
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