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This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a gas phase polymerization process. The process examined is similar to the processes INEOS Innovene and JPP HORIZONE. This process is based on the polymerization of gaseous PG propylene in horizontal 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): US Patent 6069212, originally issued to BP Amoco in 2000 (assigned to INEOS in 2007) Keywords: PG Propylene, Propene, Gas-Phase Reactor, Tubular Reactor, Japan Polypropylene Corporation, JNC Petrochemical Corporation
This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a gas phase process. The process examined is similar to the processes INEOS Innovene and JPP HORIZONE. This process is based on the polymerization of gaseous PG propylene in horizontal stirred-bed reactors. This report was developed based essentially on the following reference(s): US Patent 6069212, originally issued to BP Amoco in 2000 (assigned to INEOS in 2007) Keywords: PG Propylene, Propene, Gas-Phase Reactor, Tubular Reactor, Japan Polypropylene Corporation, JNC Petrochemical Corporation
This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a gas phase process. The process examined is similar to CB&I Lummus Novolen process. This process is based on the polymerization of gaseous PG propylene in vertical stirred-bed reactors. This report was developed based essentially on the following reference(s): US Patent 5639822, issued to BASF in 1997 (assigned to Novolen Technology Holdings in 2001) Keywords: PG Propylene, Propene, Gas-Phase Reactor, Vertical Stirred-Bed
This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a gas phase process The process examined is similar to LyondellBasell Spherizone process. This process is based on the polymerization of PG propylene in a multi-zone circulating reactor. This report was developed based essentially on the following reference(s): US Patent 20020061264, originally issued to Montell Technology in 2002 (assigned to LyondellBasell in 2003) Keywords: PG Propylene, Propene, MZCR, Gas-Phase Reactor, Bimodal
This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a gas phase process The process examined is similar to Grace UNIPOL process. This process is based on the polymerization of gaseous PG propylene in fluidized-bed reactors. This report was developed based essentially on the following reference(s): US Patent 6005049, originally issued to Union Carbide in 1999 (assigned to Grace in 2014) Keywords: PG Propylene, Propene, Dow, Gas-Phase Reactor, Fluidized Bed Reactor
This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a hybrid (slurry/gas phase) process. The process examined is similar to Borealis BORSTAR process. This process is based on a dual reactor system (slurry and gas phase reactors) to produce PP homopolymer. This report was developed based essentially on the following reference(s): (1) US Patent 6339136, issued to Borealis in 2002 (2) US Patent 6559348, issued to Borealis in 2003 Keywords: PG Propylene, Propene, Dual Reactor System, Slurry Reactor, Tubular Reactor, Loop Reactor
This report presents a cost analysis of Polypropylene (PP) homopolymer production from polymer grade (PG) propylene using a bulk phase 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 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
This report presents a cost analysis of Polypropylene (PP) impact copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to LyondellBasell Spherizone process. This process is based on the polymerization of PG propylene and ethylene in a multi-zone circulating reactor. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Ethene, MZCR, Gas-Phase Reactor, Bimodal
This report presents a cost analysis of Polypropylene (PP) impact copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to Grace UNIPOL process. This process is based on the polymerization of gaseous PG propylene and ethylene in fluidized-bed reactors. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Ethene, Dow, Gas-Phase Reactor, Fluidized Bed Reactor
This report presents a cost analysis of Polypropylene (PP) impact copolymer production from polymer grade (PG) propylene and ethylene using a gas phase polymerization process. The process examined is similar to the processes INEOS Innovene and JPP HORIZONE. This report was developed based essentially on the following reference(s): Keywords: PG Propylene, Propene, Ethene, Gas-Phase Reactor, Tubular Reactor, Japan Polypropylene Corporation, JNC Petrochemical Corporation