Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: C
ICC - Volume: 9
ICC - Report ID: 009-C
ICC - Report Location: Germany
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Bio-Butanol Production from Raw Sugar
ICC - Show Overview: 1
ICC - Report Location ID: 2
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 009-A,009-B,009-D,009-E
ICC - Related Reports List: 028-B,197-B
ICC - Report Location Code: DEU
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ICC - Prices: {"versions":{"1":{"1":"999","2":"999","3":"999"},"2":{"1":"1799","2":"1799","3":"1799"},"3":{"1":"3099","2":"3099","3":"3099"}},"currency":"USD"}
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/009-C.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Butanol</b>. n-Butyl Alcohol, also called n-Butanol, is an aliphatic alcohol applied in the production of butyl acrylates. It may be found as compound in nature or in fusel oils obtained via fermentation. Like all butanols. it is a colorless, clear liquid at room temperature and atmospheric pressure. This alcohol is employed as solvent, as well as in plasticizers. The industrial production of n-butanol started in the first decades of the 20th century and was based on a fermentation route that also yielded acetone. Currently, its commercial production is mainly based on the hydrogenation of n-butyraldehyde obtained by the hydroformylation of propylene using synthesis gas (this route is usually called OXO process).</p> <p><b>Ethanol</b>. Ethanol, or ethyl alcohol, is a volatile, flammable, and colorless liquid (pure form). It is miscible in all proportions with water, ether, acetone, benzene, and some other organic solvents. Ethanol has been produced by the fermentation of carbohydrates for thousands of years. In the 1930s, low oil prices enabled the production of industrial ethanol through direct and indirect hydration of petroleum-derived ethylene. The rising cost of crude petroleum has prompted research into the industrial manufacture of ethanol from biomass sources. Ethanol from biomass can be produced by the fermentation of starch (from corn), sugar (from sugarcane) or waste lignocellulosic biomass (such as corn stover or switch grass). The process varies depending on the feedstock used. Due to governments’ programs and technology advances, biomass has become the lowest cost raw material for ethanol production. Currently, ethanol is almost exclusively obtained from biomass and has become a renewable-based chemical. Global concerns about sustainability and global warming have inspired research into the use of renewable ethanol for ethylene manufacture, substituting petroleum-derived ethylene.</p> <b>Acetone</b>. Acetone, also known as 2-propanone, is the simplest ketone. It is used as solvent for a wide range of organic compounds (e.g. oils, fats, resins, waxes and gums). It is also used as feedstock for the production of several chemicals, such as methyl methacrylate, bisphenol A, and methyl isobutyl ketone. The main source of acetone is the process for phenol production from cumene, which generates acetone as by-product at an approximate ratio for 0.6 kg of acetone per kg of phenol. Industrial consumers of acetone usually receive shipments in large containers made of carbon steel, tank trucks made of stainless steel or aluminum, or rail tank cars made of carbon steel or aluminum. International shipments by sea are usually made in steel barges and amount at least 2,000 metric tons.</p> <h6>Raw Material</h6> <p><b>Raw Sugar</b>. Raw sugar is a commodity product which is light brown in color and presents from 96 to 99 wt% of sucrose. Since it is not an edible product, it must undergo a refining process to become a refined sugar (more than 99.9 wt% sucrose), a product suitable to food applications. This may be accomplished in the same sugar factory where raw sugar was produced or in stand-alone refineries. It is commercialized as a granular product, and can be produced either from sugarcane or sugarbeet, depending on climate conditions. Sugarcane is cultivated in tropical and subtropical areas, while sugarbeet is more suitable to temperate zones.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/009-C.jpg
ICC - Short Description: This report examines a conventional Acetone-Butanol-Ethanol (ABE) fermentation process. This economic analysis assumes a plant located in Germany using raw sugar as feedstock, which is fermented to Butanol, acetone and ethanol by a novel strain of Clostridium. Each product is separated.
ICC - Main Product: Butanol
ICC - Plant Capacity: 90.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Bio-Butanol Production from Raw Sugar

Butanol Production Costs Report | Issue C | Q4 2024

Production Cost Report

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90 kta Germany-based plant   |   Q4 2024   |   107 pages

This report presents a cost analysis of a 90 kta (kilo metric ton per annum) Germany-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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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

Costs in Different Countries Add-on

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Butanol 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 Butanol 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 Butanol 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 Butanol 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 Butanol Production Cost Reports

Butanol Production from Ethanol

The report shows an economic analysis of the construction of an industrial plant in the United States for n-Butanol production. In the process reviewed ethanol is dimerized into n-Butanol via the Guerbet reaction. This reaction is composed by dehydrogenation, aldol condensation and hydrogenation.

Details: 80 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 80 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-Butanol Production from Corn

This report presents the economics of bio-based Butanol production from corn in the United States. The process under analysis is a conventional Acetone-Butanol-Ethanol (ABE) fermentation process. Initially, corn undergoes wet milling to separate starch, which is hydrolyzed in two steps. Glucose is fermented to produce butanol, acetone and ethanol.

Details: 90 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 90 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

Butyl Acrylate Production from Propylene and Butanol

This study concerns the production of n-Butyl Acrylate, starting from propylene and n-butanol. Chemical grade propylene is oxidized to acrolein and then to acrylic acid, which is then fed to an esterification reaction, along with n-butanol to generate Butyl Acrylate. The economic analysis performed is based on a plant located in the United States.

Details: 150 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue B   From $1,199 USD

The cost analyses presented in this report target a 150 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.

Hexamethylene Diisocyanate from HMDA (Non-Phosgene Process)

This report presents a techno-economic analysis of Hexamethylene Diisocyanate (HDI) production from hexamethylene diamine (HMDA) in the United States. The process presented in this report is a non-phosgene process similar to BASF process. Initially, HMDA reacts with urea and butanol generating a carbamate intermediate. Then, the carbamate is thermally cracked producing HDI.

Details: 20 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 20 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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