1-Butene Production from Ethylene
Butene Production Costs Report | Issue B | Q3 2024
| Report Details |
| 50 kta United States-based plant | Q3 2024 | 107 pages |
This report presents a cost analysis of a 50 kta (kilo metric ton per annum) United States-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.
Report Abstract
This study presents the costs associated with the construction of an industrial plant producing 1-Butene from ethylene in the United States. This study analyzes a process similar to the Axens/SABIC AlphaButol technology. In the process under analysis, ethylene is dimerized into butenes with high selectivity for 1-Butene. Gasoline (C6+ stream) is generated as by-product.
The report provides a comprehensive study of Butene production and related Butene production cost, covering three key aspects: a complete description of the Butene production process examined; an in-depth analysis of the related Butene plant capital cost (Capex); and an evaluation of the respective Butene plant operating costs (Opex).
The Butene 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 Butene 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 Butene plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic
The process under analysis comprises the following major sections: (1) dimerization; and (2) separation & purification.
* Dimerization. Initially, fresh ethylene and recycled ethylene are fed to the dimerization reactor, along with catalyst and co-catalyst diluted in butene. The dimerization occurs in the liquid phase, at mild conditions. Reaction heat is continuously removed by means of an external cooler. The reactor effluent, containing the 1-Butene produced, is routed to separation steps downstream.
* Separation & purification. This section comprises essentially separation and purification steps for isolating the 1-Butene produced. The dimerization reactor effluent is initially passed through a flash vessel and then through evaporators, in such a way that most of the hydrocarbons in that stream vaporize and spent catalyst is discharged. The gaseous streams are combined, liquified and passed through a distillation column, in which ethylene is separated and recycled to dimerization. Finally, in a last distillation step, 1-Butene with a purity of 99.5 wt % is separated from residual oligomers.
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Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Plant Cost Breakdowns
Plant Capacity Assessment
Process Flow Diagrams
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Butene 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 Butene 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 Butene 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 Butene 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 Butene Production Cost Reports
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This feasibility study concers 1-Butene production from raffinate-2. In this study, raffinate-2 is first subjected to a hydrogenation step before fractionation. Raffinate-3 is generated as by-product. The economic analysis is also based on a plant located in the United States.
Details: 120 kta United States-based plant | Q3 2024 | 107 pages | Issue F From $799 USD
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1-Butene from Raffinate-2 (Fractionation Followed by Isomerization)
In the process reviewed in this report, raffinate-2 is sent to a fractionation step and further subjected to an isomerization step to produce 1-Butene. The economic analysis is based on a plant located in the United States.
Details: 120 kta United States-based plant | Q3 2024 | 107 pages | Issue G From $799 USD
The cost analyses presented in this report target a 120 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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