Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: D
ICC - Volume: 243
ICC - Report ID: 243-D
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Diphenyl Carbonate from Phenol and Methanol (DMC Intermediate)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 243-A,243-B,243-C,243-E
ICC - Related Reports List: 045-A,045-B,001-B,001-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"10","price":0},"2":{"time":"5","price":"599"}},"2":{"1":{"time":"10","price":0},"2":{"time":"5","price":"599"}},"3":{"1":{"time":"12","price":0},"2":{"time":"7","price":"599"}}},"unit":"d"}
ICC - Prices: {"versions":{"1":{"1":"1199","2":"1199","3":"1199"},"2":{"1":"1999","2":"1999","3":"1999"},"3":{"1":"3399","2":"3399","3":"3399"}},"currency":"USD"}
ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/243-D.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Diphenyl Carbonate</b>. 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.</p> <h6>Raw Materials</h6> <p><b>Methanol</b>. Methanol is one of the most important chemical raw materials, used as a solvent, starting material in the production of chemicals and in the fuel sector. Currently, more than 95% of commercial methanol is synthetically produced from synthesis gas, or syngas, which is a mixture of hydrogen and carbon monoxide. </p> <b>Phenol</b>. 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.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/243-D.jpg
ICC - Short Description: 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.
ICC - Main Product: Diphenyl Carbonate
ICC - Plant Capacity: 130.00
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ICC - Images Count: {"versions":{"1":"9","2":"13","3":"22"}}
ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Diphenyl Carbonate from Phenol and Methanol (DMC Intermediate)

Diphenyl Carbonate Production Costs Report | Issue D | Q2 2024

Production Cost Report

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Report Details
130 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 130 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.

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Production Process Information

Process Consumptions

Labor Requirements

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Operating Cost Summary

Production Costs Datasheet

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Production Process Information

Process Consumptions

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Production Costs Datasheet

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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

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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

Other Diphenyl Carbonate Production Cost Reports

Diphenyl Carbonate from Phosgene and Phenol

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.

Details: 130 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 130 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.

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   |   Q2 2024   |   107 pages   |   Issue B   From $1,199 USD

The cost analyses presented in this report target a 130 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.

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   |   Q2 2024   |   107 pages   |   Issue C   From $1,199 USD

The cost analyses presented in this report target a 130 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.

Diphenyl Carbonate Production from Phenol and Carbon Monoxide

This feasibility study reviews Diphenyl Carbonate (DPC) production from phenol. The process under analysis is an oxidative carbonylation process, which involves the direct reaction of phenol with carbon monoxide to form DPC. The economic analysis is based on a plant constructed in the United States.

Details: 130 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   From $999 USD

The cost analyses presented in this report target a 130 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.

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Other Related Production Cost Reports

Methanol Production from Natural Gas (Steam Reforming)

This study presents the economics of large-scale Methanol production from natural gas in the United States. In the process examined, natural gas is first converted into synthesis gas (syngas) by means of conventional steam reforming and then the syngas is converted into Methanol.

Details: 1,000 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 1,000 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.

Methanol Production from Natural Gas (Combined Reforming)

This study presents the economics of large-scale Methanol production from natural gas in the United States. In this process, natural gas is first converted into synthesis gas (syngas) by means of conventional steam reforming and secondary autothermal reforming. Then, the syngas is converted into Methanol.

Details: 1,700 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 1,700 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 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   |   Q2 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   |   Q2 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.

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