Commodity Production Costs Report
DCPD Unsaturated Polyester Production
Unsaturated Polyester Resin Operating Costs & Plant Construction Costs
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.
Key reference(s): ?
Product
Unsaturated Polyester Resin.
Raw Materials
Ethylene Glycol, Maleic Anhydride, Dicyclopentadiene, Styrene.
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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 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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Other Unsaturated Polyester Resin Production Cost Reports
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Terephthalic Unsaturated Polyester Production
This report presents the economics of Terephthalic Unsaturated Polyester production from maleic anhydride, recycled polyethylene terephthalate, propylene glycol and styrene using a typical batch process. The economic analysis is based on a plant located in the United States.
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