Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: F
ICC - Volume: 175
ICC - Report ID: 175-F
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: 1-Butene from Raffinate-2 (Hydrogenation Followed by Fractionation)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 175-A,175-B,175-C,175-D,175-E,175-G,175-H
ICC - Related Reports List: 198-C,208-F
ICC - Report Location Code: USA
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ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/175-F.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>1-Butene</b>. 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).</p> <p><b>Raffinate-3</b>. Raffinate-3 is a byproduct of butadiene extraction from C4 streams, rich in butenes and used as a petrochemical feedstock. It is utilized in alkylation units to produce high-octane gasoline components. Collected during olefin separation processes, it is stored as a liquefied gas. Its composition makes it valuable for further processing into chemicals like MTBE and isobutylene derivatives.</p> <h6>Raw Material</h6> <p><b>Raffinate-2</b>. 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.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/175-F.jpg
ICC - Short Description: 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.
ICC - Main Product: Butene
ICC - Plant Capacity: 120.00
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1-Butene from Raffinate-2 (Hydrogenation Followed by Fractionation)

Butene Production Costs Report | Issue F | Q2 2024

Production Cost Report

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Report Details
120 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

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.

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Production Process Information

Process Consumptions

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

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Production Process Information

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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

Butenes Production from Ethylene

This report presents the economics of Butenes production from ethylene using a dimerization process similar to Lummus process. In the process under analysis, gasoline and fuel oil are generated as by-products. The economic analysis assumes a plant constructed in the United States.

Details: 200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 200 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 Production from Ethylene

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.

Details: 50 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 50 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 (Extractive Distillation)

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.

Details: 120 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   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.

Butenes Production from Propylene

This report shows the economics of Butenes production from propylene via a metathesis process. In the process examined, propylene is converted to butenes and ethylene is generated as by-product. The economic assessment assumes a plant located in the United States.

Details: 300 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 300 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 (Superfractionation)

This study approaches 1-Butene production from raffinate-2 in the United States using a typical superfractionation process. Raffinate-3 is also generated as by-product in this plant.

Details: 120 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   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   |   Q2 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.

1-Butene from Raffinate-2 (Adsorption)

This report presents a techno-economic analysis about 1-Butene production from raffinate-2 in the United States. In this study, a molecular sieve adsorption process similar to the UOP Sorbutene technology is used to extract 1-butene from the raffinate stream.

Details: 120 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue H   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

Bimodal HDPE from Ethylene and 1-Butene (Similar to UNIPOL)

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.

Details: 450 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 450 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.

LLDPE Production from Ethylene and 1-Butene (Similar to UNIPOL)

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.

Details: 450 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue F   From $799 USD

The cost analyses presented in this report target a 450 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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