Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: B
ICC - Volume: 173
ICC - Report ID: 173-B
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Butadiene Production from Butenes
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 173-A,173-C,173-D,173-E,173-F,173-H,173-G,173-I,173-J
ICC - Related Reports List: 206-B,234-A
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"2":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"3":{"1":{"time":"7","price":0},"2":{"time":"3","price":"299"}}},"unit":"d"}
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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/173-B.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Butadiene</b>. Butadiene is a commodity mainly produced as a byproduct of ethylene crackers. More specifically, it is extracted from the C4 hydrocarbons stream in naphtha-based crackers. The largest single use of butadiene is in the production of SBR and styrene-butadiene latexes.</p> <p><b>Raffinate</b>. Raffinate is a byproduct of olefin production used as a feedstock for fuel blending and petrochemical synthesis. It is a critical source of light hydrocarbons for alkylation and polymerization processes. Raffinate is stored as a pressurized gas or liquid. Its mixture of butenes and butanes makes it valuable in the manufacture of gasoline additives and synthetic rubber.</p> <h6>Raw Materials</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> <b>Chemicals</b>. </p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/173-B.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Reaction; (2) Crude Butadiene Recovery; and (3) Purification.</p><p>Reaction. Butenes feed is vaporized and mixed with steam and compressed air before being fed to the reactor. Butenes react with oxygen, forming Butadiene and water. The excess heat generated by the exothermic reaction is used to generate part of the steam fed to the reactor. The reaction product comprises Butadiene, unreacted C4s (saturated and unsaturated), reaction side products (e.g. aldehydes), as well as steam, nitrogen, unreacted oxygen and carbon dioxide.</p><p>Crude Butadiene Recovery. The Butadiene-rich mixture from the reactor is quenched with water in a quench tower. Part of the water collected from the bottom of this column (comprising the quench water and condensate) is recycled to the top of the tower. The balance is used in the aldehyde separator downstream. The overhead Butadiene-rich gas is compressed and fed to the aldehyde separator, where it is scrubbed with water from quench tower bottoms. The aldehyde-free overheads is injected in the bottom of an absorber column, where a lean oil stream absorbs hydrocarbons from the gaseous reaction product. The oil/hydrocarbon mixture is further fed to a degasser column, where light compounds are separated as overhead gas. A crude Butadiene stream is obtained after the oil is separated from the C4 mixture in a stripper column.</p><p>Purification. The crude Butadiene, which still contains butane and butenes, is then subjected to extractive distillation in the presence of N-methylpyrrolidinone (NMP) used as solvent, yielding high purity Butadiene as the final product. Butane and butenes separated from the Butadiene are sold as raffinate by-product.</p>
ICC - Short Description: This study presents the economics of 1,3-Butadiene (BD) production from mixed butenes in a plant assumed to be erected in the United States. In this process, which is similar to TPC/UOP Oxo-D, butenes are catalytically dehydrogenated to produce the Butadiene product. Raffinate is obtained as by-product.
ICC - Main Product: Butadiene
ICC - Plant Capacity: 240.00
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Butadiene Production from Butenes

Butadiene Production Costs Report | Issue B | Q3 2024

Production Cost Report

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240 kta United States-based plant   |   Q3 2024   |   107 pages

This report presents a cost analysis of a 240 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

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 Butadiene 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 Butadiene 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 Butadiene 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 Butadiene 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

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Butadiene from Crude C4s (DMF Extraction)

It presents the economics of 1,3-Butadiene extraction from a crude C4s stream in the United States. The process examined in this report is similar to Nippon Zeon. In this process, dimethyl-formamide is used as a solvent in order to extract twice 1,3-Butadiene from the crude C4 stream.

Details: 200 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   From $999 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.

Bio-Butadiene Production from Glucose (Anaerobic Fermentation)

It presents the economics of bio-based 1,3-Butadiene (BD) production from glucose syrup in the United States using an anaerobic fermentation process.

Details: 165 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue I   From $799 USD

The cost analyses presented in this report target a 165 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

Polychloroprene Production from Butadiene and Chlorine

This study provides an economic analysis of Polychloroprene production starting from butadiene and chlorine, based on a plant located in the United States. In the first step, butadiene is chlorinated, generating dichlorobutenes, which are subjected to an isomerization to convert them to 3,4-dichloro-1-butene. It is then dehydrochlorinated, forming chloroprene. Finally, chloroprene is polymerized to the respective rubber.

Details: 50 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $1,199 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.

Emulsion Styrene Butadiene Rubber Production

This report presents the economics of SBR production starting from butadiene and styrene. The analysis encompasses a plant located in the United States, employing a typical cold emulsion process for generating a non-oil extended, non-staining grade of emulsion SBR (similar to 1502). In this process, an emulsion comprising water, styrene and butadiene is polymerized into a latex, which is then coagulated to form the SBR.

Details: 140 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 140 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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