Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: C
ICC - Volume: 7
ICC - Report ID: 007-C
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Bio-Acrylic Acid Production from Glucose (Single-Step Process)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 007-A,007-B,007-D,007-E,007-F,007-H,007-K,007-M,007-G,007-I,007-J,007-L
ICC - Related Reports List: 359-A,219-B,370-A
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"799","2":"799","3":"799"},"2":{"1":"1599","2":"1599","3":"1599"},"3":{"1":"2699","2":"2699","3":"2699"}},"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/007-C.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>Glacial Acrylic Acid</b></p></b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Glucose Syrup</b></p>, <p><b>Corn Steep Liquor</b></p>, <p><b>Soda Ash</b></p>, <p><b>Extractant Solvent</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/007-C.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Fermentation; (2) Product Treatment and Purification; and (3) Components Recovery.</p><p>Fermentation. Fermentation media is prepared by mixing glucose, corn steep liquor and water recovered downstream, and fed to agitated fermentors. The pH control is made by addition of make-up and recycled sodium carbonate. The fermentation broth is centrifugated to separate cells and other suspended solids. The supernatant of the centrifugation, containing sodium acrylate, is sent to Liquid-Liquid Extraction, while the retentate is partially recycled to the fermentors, with the remainder being disposed.</p><p>Product Treatment and Purification. The sodium acrylate solution from Cells Separation is sent to L-L Extraction, where it is contacted in countercurrent flow with an extractant solvent. An aqueous phase containing sodium bicarbonate and residual sodium acrylate is directed to Sodium Carbonate (Na2CO3) tegeneration. An organic phase containing the extractant and acrylic acid is passed through a flash unit to remove most of the dissolved carbon dioxide (CO2), and then routed to Water Removal Column. In this column, water is removed, and a bottom product is sent to the Acrylic Acid Column. Glacial acrylic acid (99.7 wt.% purity) is obtained as the column overhead, while the extractant solvent is recovered from the bottom and routed to back extraction. </p><p>Components Recovery. In back extraction, the solvent is contacted in countercurrent with hot water, obtaining two phases: an aqueous phase containing impurities and unconverted glucose, disposed as wastewater, and an organic phase containing the solvent, sent to CO2 Compression and Absorption. Part of the carbon dioxide streams released throughout the process is also fed to this area. The solution formed is used as the extractant in the liquid-liquid extraction. The sodium bicarbonate solution from L-L Extraction is decomposed at high temperatures in the Na2CO3 Regeneration, producing carbon dioxide and dissolved sodium carbonate. The solution is passed through a sequence of evaporation steps for partial water removal and recycled as a neutralization component in the fermentation process.</p><p></p>
ICC - Short Description: This report shows a feasibility study of bio-based Acrylic Acid production from glucose syrup in a plant assumed to be located in the United States. The process is based on the fermentation route of glucose, yielding Acrylic Acid, similar to the speculative process proposed by the Delft University of Technology.
ICC - Main Product: Acrylic Acid
ICC - Plant Capacity: 150.00
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Bio-Acrylic Acid Production from Glucose (Single-Step Process)

Acrylic Acid Production Costs Report | Issue C | Q4 2024

Production Cost Report

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150 kta United States-based plant   |   Q4 2024   |   107 pages

This report presents a cost analysis of a 150 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

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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 Acrylic Acid 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 Acrylic Acid 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 Acrylic Acid 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 Acrylic Acid 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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Glacial Acrylic Acid from Crude Acrylic Acid (Distillation)

This analysis presents the costs associated with the construction of an industrial plant in the United States, for crude acrylic acid purification via distillation to produce Glacial Acrylic Acid.

Details: 120 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue I   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.

Acrylic Acid Production from Natural Gas

This report presents the economics of Ester-Grade Acrylic Acid (EAA) production from natural gas in the United States. Initially, methane in the natural gas feed is cracked to acetylene which is reacted carbon monoxide generated by feed combustion, yielding Acrylic Acid.

Details: 150 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue K   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.

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Details: 120 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue B   From $799 USD

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The cost analyses presented in this report target a 3 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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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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