Polypropylene Random Copolymer Production Cost Analysis Pp E36a
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Polypropylene Random Copolymer Production - Cost Analysis - PP E36A
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to CB&I Lummus Novolen process. This process is based on the polymerization of gaseous PG propylene and PG ethylene in vertical stirred-bed reactors. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Gas-Phase Reactor, Vertical Stirred-Bed
Polypropylene Random Copolymer Production - Cost Analysis - PP E36A
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to CB&I Lummus Novolen process. This process is based on the polymerization of gaseous PG propylene and PG ethylene in vertical stirred-bed reactors. 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): Keywords: PG Propylene, Propene, Gas-Phase Reactor, Vertical Stirred-Bed
Polypropylene Random Copolymer Production - Cost Analysis - PP E31A
This report presents a cost analysis of Polypropylene (PP) Random Copolymer production from polymer grade (PG) propylene and ethylene 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 and PG ethylene in loop reactors. 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): Keywords: PG Propylene, Propene, Tubular Reactor, Liquid-Phase Polymerization