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This report presents the economics of Bimodal High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-butene in the United States, using a slurry process similar to LyondellBasell Hostalen and Mitsui CX. The polymerization is carried out in three CSTRs using hexane as diluent and a high-activity Ziegler catalyst system.
Details: 350 kta United States-based plant | Q1 2026 | Issue A | Detailed | Printable
Companion Reports:
This report analyses the economics of Bimodal High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-hexene in the United States, using a gas-phase process similar to LyondellBasell Spherilene. In this process, ethylene and 1-hexene are copolymerized using two fluidized-bed reactors in series.
Details: 350 kta United States-based plant | Q1 2026 | Issue B | Detailed | Printable
Companion Reports:
This report presents the economics of Bimodal High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-butene in the United States. The process examined in this report uses a slurry loop process similar to Borealis BORSTAR. The reaction system consists of a slurry loop and a gas phase reactor.
Details: 350 kta United States-based plant | Q1 2026 | Issue D | Detailed | Printable
Companion Reports:
This report analyses the economics of Bimodal High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-hexene in the United States. The process examined in this report uses two slurry loop reactors, similar to Chevron Phillips’ MarTECH Advanced Dual Loop (ADL) and INEOS INNOVENE S.
Details: 450 kta United States-based plant | Q1 2026 | Issue E | Detailed | Printable
Companion Reports:
This report presents the economics of High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene in the United States, using a slurry loop process similar to Chevron Phillips MarTECH and INEOS INNOVENE S. In this process, the monomers are polymerized in a single loop reactor.
Details: 450 kta United States-based plant | Q1 2026 | Issue F | Detailed | Printable
Companion Reports:
It presents the economics of High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene in the United States. The process examined in this report uses a gas phase process similar to LyondellBasell Spherilene. The polymerization is conducted in a single fluidized-bed reactor.
Details: 450 kta United States-based plant | Q1 2026 | Issue G | Detailed | Printable
Companion Reports:
This report analyses the economics of High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene in the United States. The process examined in this report is similar to Univation UNIPOL and INEOS INNOVENE G. In this process, ethylene is polymerized in the gas-phase in a reaction loop consisting of a fluidized-bed reactor, a compressor and a heat exchanger.
Details: 450 kta United States-based plant | Q1 2026 | Issue H | Detailed | Printable
Companion Reports:
This report examines the costs related to High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene in the United States. The process examined in this report uses a solution process similar to NOVA Chemicals Advanced SCLAIRTECH. The polymerization is carried out in two continuous-stirred-tank reactors (CSTR)
Details: 350 kta United States-based plant | Q1 2026 | Issue I | Detailed | Printable
Companion Reports:
This report analyses the economics of High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-butene in the United States. The process examined in this report uses a gas-phase polymerization in a single reactor similar to LyondellBasell Spherilene S.
Details: 450 kta United States-based plant | Q1 2026 | Issue J | Detailed | Printable
Companion Reports:
This report analyses the economics of Bimodal High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-butene in the United States, using a gas-phase process similar to LyondellBasell Spherilene. In this process, ethylene and 1-butene are copolymerized using two fluidized-bed reactors in series.
Details: 450 kta United States-based plant | Q1 2026 | Issue K | Detailed | Printable
Companion Reports:
This report analyses the economics of Bimodal High Density Polyethylene (HDPE) production from polymer grade (PG) ethylene and 1-octene in the United States, using a gas-phase process similar to LyondellBasell Spherilene. In this process, ethylene and 1-octene are copolymerized using two fluidized-bed reactors in series.
Details: 400 kta United States-based plant | Q1 2026 | Issue L | Detailed | Printable
Companion Reports:
Summary
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Bimodal HDPE from Ethylene and 1-Butene (Similar to UNIPOL)
Detailed Edition | Q1 2026
450 kta @ Q1 2026
Downloadable PDF
$1,599 -
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Subtotal$1,599 USD
Summary
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Bimodal HDPE from Ethylene and 1-Butene (Similar to UNIPOL) Report
Production Costs Report | Detailed Edition$1,599 -
Total$1,599 USD