|Details: 70 kta United States-based plant | Q1 2022 | 108 pages | Buy From $999 USD|
This report presents an up-to-date, detailed cost analysis of DCPD Unsaturated Polyester Resin (UPR) production from maleic anhydride, dicyclopentadiene, monoethylene glycol, diethylene glycol and styrene. The process examined is a typical batch process. In this plant, maleic anhydride and dicyclopentadiene react, giving dicyclopentadiene acid maleate (DCPD), which condenses with the glycols to produce DCPD Resin.
This report, UPR E41A, is a best-in-class examination of Unsaturated Polyester Resin production, providing in-depth, comprehensive techno-economic analysis of the production technology examined, including:
- Process Description: raw materials and utilities consumption, products generation, labor requirements, list of equipment, characterization of site infrastructure, process flow diagram (PFD).
- Capital Cost Analysis: costs of plant construction, working capital, owners' costs, commissioning, start-up and contingency.
- Operating Cost Analysis: variable costs, fixed costs (salary, benefits & maintenance) and corporate overhead costs.
- And much more . . .