1-Butene from Raffinate-2 (Extractive Distillation)
Butene Production Costs Report | Issue C | Q3 2024
| Report Details |
| 120 kta United States-based plant | Q3 2024 | 107 pages |
This report presents a cost analysis of a 120 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
In this report, the economic analysis concerns a plant located in the United States, producing 1-Butene using a conventional industrial approach for extractive distillation of raffinate-2, which also generates raffinate-3 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 Overview
Product
1-Butene. 1-butene, cis-2-butene, trans-2-butene, isobutylene and butadiene are usually coproduced as a mixture - referred to as C4 fraction - from petroleum refinery/petrochemical process. Typically, for obtaining pure 1-butene, C4 fraction is sent a selective extraction of isobutylene with sulfuric acid, butadiene selective hydrogenation and distillation for 2-butenes separation. An alternative means of producing 1-butene is the ethylene dimerization. Butenes are mainly used as alkylate and polymer gasoline, in fuel applications, and as co-monomers in the production of some polymers. 1-butene, particularly, is mostly used as a comonomer for LLDPE production, and as a comonomer for modifying high density polyethylene (HDPE).
Raw Material
Raffinate-2. Raffinate-2 is a C4 residual stream primarily consisting of 1-butene, 2-butenes, and butanes. It is obtained following the separation of 1,3-butadiene and isobutylene from mixed C4s stream (or crude C4s), which is one of the products of the naphtha steam cracking processes.
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Production Process Information
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Production Process Information
Process Consumptions
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Production Costs Datasheet
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Operating Cost Details
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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
1-Butene from Raffinate-2 (Hydrogenation Followed by Fractionation)
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
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.
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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Other Related Production Cost Reports
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This analysis 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 is similar to Univation UNIPOL process. In this process, ethylene is polymerized in combination with 1-butene in the gas-phase in a reaction loop consisting of a fluidized-bed reactor, a compressor and a heat exchanger.
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