Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: D
ICC - Volume: 173
ICC - Report ID: 173-D
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Bio-Butadiene Production from Glucose (Aerobic Fermentation)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 173-A,173-B,173-C,173-E,173-F,173-H,173-G,173-I,173-J
ICC - Related Reports List: 234-A,370-A,206-B
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/173-D.jpg
ICC - Process Overview Text: <h6>Product</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> <h6>Raw Materials</h6> <p><b>Chemicals</b>. </p> <b>Glucose Syrup</b>. Glucose (C6H12O6), also known as D-glucose and dextrose, is the most abundant sugar in nature. Commercial glucose products are available in both dry and syrup forms in a variety of purities and concentrations. Glucose uses include pharmaceuticals, food, chemicals and fuels. This compound is used as raw material in fermentative processes for the production of vitamins, organic acids, antibiotics, amino acids, enzymes, and polysaccharides.</p> <b>Dodecane</b>. Dodecane is a liquid alkane hydrocarbon with the chemical formula C12H26.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/173-D.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Fermentation; (2) Fermentation broth treatment; and (3) Butadiene purification.</p><p>Fermentation. The culture media is prepared by diluting the glucose syrup and nutrients in water. A genetically re-engineered yeast is propagated in an aerobic pre-fermentation step to obtain the proper inoculum concentration. The fermentation is carried out in fed-batch mode and under aerobic process conditions, in agitated fermenters equipped with internal coil. The fermentation step generates fermenter off-gas, which comprises the crude Butadiene product, and fermentation broth.</p><p>Fermentation broth treatment. After fermentation, cell biomass is separated from the fermentation broth. The clarified broth then is submitted to an ultrafiltration step, used to remove the remaining contaminants. The resulting aqueous stream may be discarded as waste water.</p><p>Butadiene purification. Initially, off-gas is compressed and cooled. The compressed gas is fed in a absorber column, where N-dodecane solvent absorbs the Butadiene. In the next column, In the Stripper Column, Butadiene is separated from the solvent. The recovered solvent is fed into a decanter for water removal before being recycled to first column. The Butadiene-containing stream is transferred into the Adsorption System. There, The oxygenates are removed by adsorption in adequate media. The oxygenate-free crude Butadiene is further purified in a last distillation column for heavy ends impurities separation. Butadiene with purity >99.7 wt% is recovered.</p>
ICC - Short Description: It presents the economics of bio-based 1,3-Butadiene (BD) production from glucose syrup in the United States using a direct aerobic fermentation process similar to the one proposed by Global Bioenergies.
ICC - Main Product: Butadiene
ICC - Plant Capacity: 165.00
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Bio-Butadiene Production from Glucose (Aerobic Fermentation)

Butadiene Production Costs Report | Issue D | Q2 2024

Production Cost Report

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165 kta United States-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 165 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

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Labor Requirements

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Production Costs Datasheet

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Production Process Information

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Production Costs Datasheet

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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

Other Butadiene Production Cost Reports

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   |   Q2 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   |   Q2 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   |   Q2 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   |   Q2 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.

Glucose Syrup Production

This report presents the economics of Glucose Syrup production from shelled corn. In this process, shelled corn is passed through a wet milling process to recover the corn starch, which, in turn, passes through two subsequent hydrolysis steps for the generation of glucose. The economic analysis performed assumes a plant located in the United States.

Details: 40 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 40 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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