DCPD Unsaturated Polyester Production
Unsaturated Polyester Resin Production Costs Report | Issue D | Q4 2024
| Report Details |
| 70 kta United States-based plant | Q4 2024 | 107 pages |
This report presents a cost analysis of a 70 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
This report presents the economics of DCPD Unsaturated Polyester production from maleic anhydride, dicyclopentadiene, monoethylene glycol, diethylene glycol and styrene using a typical batch process in the United States. The addition reaction of maleic anhydride produces a dicyclopentadiene acid maleate that condenses with glycols to form DCPD resin.
The report provides a comprehensive study of Unsaturated Polyester Resin production and related Unsaturated Polyester Resin production cost, covering three key aspects: a complete description of the Unsaturated Polyester Resin production process examined; an in-depth analysis of the related Unsaturated Polyester Resin plant capital cost (Capex); and an evaluation of the respective Unsaturated Polyester Resin plant operating costs (Opex).
The Unsaturated Polyester Resin 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 Unsaturated Polyester Resin 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 Unsaturated Polyester Resin plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
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Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
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
Pages | Tables | Images
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Updated with Q4 2024 Data
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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
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Unsaturated Polyester Resin 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 Unsaturated Polyester Resin 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 Unsaturated Polyester Resin 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 Unsaturated Polyester Resin 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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This report presents the economics of Isophthalic Unsaturated Polyester production from maleic anhydride, isophthalic acid, propylene glycol and styrene using a two-stage batch process located in the United States. In the first stage, the glycol and isophthalic acid react to produce a cleat melt. Maleic anhydride is added subsequently and the resin is completed.
Details: 70 kta United States-based plant | Q4 2024 | 107 pages | Issue A From $999 USD
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Details: 70 kta United States-based plant | Q4 2024 | 107 pages | Issue B From $999 USD
The cost analyses presented in this report target a 70 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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