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This report examines the costs related to Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-butene in the United States. The process examined in this report is a solution process similar to NOVA Chemicals SCLAIRTECH. The polymerization is carried out in a tubular reactor and a CSTR reactor.
This report presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-butene in the United States. The process examined in this report is similar to LyondellBasell Spherilene S. It comprises a small loop reactor for catalyst activation before the main reaction loop with fluid-bed reactor. Residual hydrocarbons are stripped from the product by nitrogen.
This study presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-octene in the United States. The process examined in this report is similar to NOVA Chemicals Advanced SCLAIRTECH. This process is carried out in two CSTR operating in series.
This report presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-octene in the United States. The process examined in this report is similar to Dow DOWLEX. In this technology, the polymerization is carried out in two CSTR reactors operating in series.
This report presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-octene comonomer in the United States, using a solution process similar to NOVA Chemicals SCLAIRTECH. This process uses a tubular reactor and a CSTR operating in series.
This study presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-butene in the United States, using a gas phase process similar to Univation UNIPOL and INEOS INNOVENE. This technology comprises a reaction loop consisting of a fluidized-bed reactor, a compressor and a heat exchanger. Residual hydrocarbons are removed from the product by a propane stream.
This report examines the costs related to Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-hexene in the United States, using a slurry process similar to Chevron Phillips MarTECH. In this technology, ethylene is polymerized in combination with 1-hexene in a slurry loop reactor.
It presents the economics of Linear Low Density Polyethylene (LLDPE) production from polymer grade (PG) ethylene and 1-hexene in the United States. This report examines a gas phase process similar to Univation UNIPOL and INEOS INNOVENE. The system comprises a fluidized-bed reactor, compressor and heat exchanger.