Polypropylene Homopolymer Via Bulk Process Cost Analysis Pp E11a PDF Download

This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a bulk phase polymerization process. The process examined is similar to the processes LyondellBasell Spheripol and Mitsui Hypol II. This process is based on the polymerization of liquid PG propylene, in loop reactors, to produce PP homopolymer. This report examines one-time costs associated with the construction of a United States-based plant and the continuing costs associated with the daily operation of such a plant. More specifically, it discusses: * Capital Investment, broken down by: - Total fixed capital required, divided in production unit (ISBL); infrastructure (OSBL) and contingency - Alternative perspective on the total fixed capital, divided in direct costs, indirect costs and contingency - Working capital and costs incurred during industrial plant commissioning and start-up * Production cost, broken down by: - Manufacturing variable costs (raw materials, utilities) - Manufacturing fixed costs (maintenance costs, operating charges, plant overhead, local taxes and insurance) - Depreciation and corporate overhead costs * Raw materials consumption, products generation and labor requirements * Process block flow diagram and description of industrial site installations (production unit and infrastructure) This report was developed based essentially on the following reference(s): "Polyolefins", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: PG Propylene, Propene, Tubular Reactor, Liquid-Phase Polymerization