Commodity Production Costs Report
C4 to C12+ Linear Alpha Olefins from Ethylene (Zirconium Catalyst)
Linear Alpha Olefins Operating Costs & Plant Construction Costs
This report presents the economics of LAO production from ethylene in the United States. In this case, C4 to C12+ linear alpha-olefins are obtained via a process similar to Alpha-SABLIN process (jointly developed by SABIC and Linde). This process employs a bubble-column type reactor in which a homogenous catalyst system is introduced together with a solvent.
The report provides a comprehensive study of Linear Alpha Olefins production and related Linear Alpha Olefins production cost, covering three key aspects: a complete description of the Linear Alpha Olefins production process examined; an in-depth analysis of the related Linear Alpha Olefins plant capital cost (Capex); and an evaluation of the respective Linear Alpha Olefins plant operating costs (Opex).
The Linear Alpha Olefins production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Linear Alpha Olefins plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Linear Alpha Olefins plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Key reference(s): ?

Product
C4 to C12+ Linear Alpha Olefins. Linear alpha olefins (C4 to C12+) are important intermediates used in the production of synthetic lubricants, detergents, and plastics. Their even-numbered carbon chains make them highly reactive and versatile in applications ranging from polyethylene production to surfactants in personal care products. Linear alpha olefins are typically produced through the oligomerization of ethylene. They are stored and transported as liquids and are a key component in the petrochemical industry, particularly in the manufacture of polymers and lubricants.
Raw Material
Ethylene. Ethylene is known as a key building block for the petrochemical industry, being one of the largest-volume petrochemical produced worldwide. It is widely used as chemical intermediate in the production of several end products, including plastics, resins and fibers. Ethylene is largely produced by thermal cracking of petroleum-based feedstocks, in the presence of steam. It is stored in a liquid state under high pressure or at low temperatures. However, ethylene is, most of times, directly supplied to its consumers.
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Linear Alpha Olefins production plant examined.
Plant Capital Cost Details
Detailing of fixed capital (ISBL, OSBL & Owner’s Cost), working capital and additional capital requirements.
Plant Cost Breakdowns
Breakdown of Linear Alpha Olefins process unit (ISBL) costs and infrastructure (OSBL) costs; plant cost breakdown per discipline.
Operating Costs Summary
Summary presenting the operating variable costs and the total operating cost of the Linear Alpha Olefins production plant studied.
Operating Cost Details
Detailing of utilities costs, operating fixed costs and depreciation.
Plant Capacity Assessment
Comparative analysis of capital investment and operating costs for different Linear Alpha Olefins plant capacities.
Production Process Information
Block Flow Diagram, descriptions of process unit (ISBL) and site infrastructure (OSBL).
Process Consumptions
Raw materials and utilities consumption figures, by-products credits, labor requirements
Process Diagrams
Process flow diagrams (PFD), equipment list and industrial site configuration
Other Linear Alpha Olefins Production Cost Reports

C4 to C30+ Linear Alpha Olefins Production
This report provides the economics of Linear Alpha Olefins (LAO) production from ethylene in the United States. The process examined in this report produces LAOs ranging from C4 to C30+ using a process similar to Chevron Phillips process. Ethylene is initially submitted to oligomerization, and this reaction effluent is subjected to a transalkylation reaction.
Details: 400 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

C4 to C16+ Linear Alpha Olefins Production
This study presents a techno-economic analysis of LAO production from ethylene in the United States. In this report, a process similar to INEOS process is analyzed, producing linear alpha-olefins ranging from C4 to C16+, mainly C6 to C10. Ethylene oligomerization is carried out in a reaction with triethylaluminum produced on site, increasing the chain of the alkyls bonded aluminum.
Details: 400 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $799 USD

C4 to C12+ Linear Alpha Olefins from Ethylene (Iron Complex Catalyst)
This report approaches an economic analysis of LAO production from ethylene in the United States. The process examined in this report produces C4 to C12+ linear alpha-olefins via ethylene oligomerization, following a process similar to DuPont Versipol process.
Details: 400 kta United States-based plant | Q3 2024 | 107 pages | Issue E | From $799 USD
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Other Related Production Cost Reports

Ethylene Production from Ethane
This report presents the economics of Polymer Grade (PG) Ethylene production from ethane in the United States. In the process under analysis, ethane is thermally cracked in pyrolysis furnaces through the use of steam, yielding Ethylene. A hydrogen-rich gas is generated as by-product.
Details: 1200 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

Ethylene Production from Naphtha (Low Severity Steam Cracking)
This report presents the economics of a naphtha-based steam cracker, equipped with an electricity cogeneration unit. In this process, naphtha is thermally cracked at low severity conditions, maximizing propylene to Ethylene ratio. The analysis is based on a plant located in Germany.
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UHVI Polyalphaolefins Production
This report assesses the economics of industrial Ultra High Viscosity Index (UHVI) Polyalphaolefins (PAO) production, assuming a plant located in the United States.
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