Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 254
ICC - Report ID: 254-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: 3-Hydroxypropionic Acid Production from Glucose
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 254-B
ICC - Related Reports List: 370-A,007-M,070-B,070-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/254-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>3-Hydroxypropionic Acid</b></p></b></p> <h6>Raw Materials</h6> <p><b>Glucose Syrup</b></p>, <p><b>Corn Steep Liquor</b></p>, <p><b>Ammonia</b></p>, <p><b>Salt-Splitting Solvent</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/254-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Fermentation; (2) Separation; and (3) Purification.</p><p>* Fermentation. The culture media used in the pre-fermentation and in the fed-batch fermentation are prepared by diluting the glucose syrup (fermentable carbon source) and nutrients (source of nitrogen, vitamins and minerals) in water. The main fermentation is carried out in fed-batch mode and under aerobic process conditions. The pH control is made by addition of a solution of ammonia, so as to keep the pH of the fermentation broth around 7. Due to the presence of the ammonium hydroxide, most of the 3-Hydroxypropionic Acid produced is neutralized to 3-hydroxypropionate, in such a way that the broth contains 3-Hydroxypropionic Acid mainly in its conjugate base form.</p><p>* Separation. After fermentation, cell debris and other suspended solids are removed from the broth by ultrafiltration. The permeate is pumped to Evaporators, while the retentate – mostly biomass/water – is disposed. The concentrated broth is fed to an agitated vessel operating under vacuum, along with tricaprylamine (organic solvent) and dodecanol (cosolvent). The mixture is heated so that the ammonium salt of the 3-Hydroxypropionic Acid splits, producing ammonia and 3-HP. The liquid stream from the Salt-Splitting is then back-extracted in countercurrent contact with hot water, yielding an aqueous phase rich in 3-HP and a 3-HP-lean organic phase. </p><p>* Purification. The rich aqueous solution of 3-HP is subjected to a demineralization step for removal of inorganic cations and anions from the solution and then concentrated. The concentrated 3-HP solution is finally fed to two wiped film evaporators operating in series, under vacuum, for product purification. The final product obtained in this process is an aqueous solution containing 60 wt% of 3-Hydroxypropionic Acid.</p>
ICC - Short Description: This report presents the economics of 3-Hydroxypropionic Acid (3-HPA) production from glucose syrup using a fermentation process similar to the one developed by Cargill. The main fermentation is carried out in fed-batch mode and under aerobic conditions. The economic analysis provided assumes a plant located in the United States.
ICC - Main Product: 3-Hydroxypropionic Acid
ICC - Plant Capacity: 200.00
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3-Hydroxypropionic Acid Production from Glucose

3-Hydroxypropionic Acid Production Costs Report | Issue A | Q2 2024

Production Cost Report

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

This report presents a cost analysis of a 200 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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Production Process Information

Process Consumptions

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Production Costs Datasheet

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Operating Cost Details

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the 3-Hydroxypropionic 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 3-Hydroxypropionic 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 3-Hydroxypropionic 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 3-Hydroxypropionic 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

Other 3-Hydroxypropionic Acid Production Cost Reports

3-Hydroxypropionic Acid Production from Raw Sugar

This report presents the economics of 3-Hydroxypropionic Acid (3-HPA) production from raw sugar using a fermentation process similar to the one developed by Cargill. Raw sugar (sucrose) is hydrolyzed into glucose and fructose (invert sugars), which are then fermented in fed-batch mode and under aerobic conditions. The economic analysis provided assumes a plant located in the Germany.

Details: 200 kta Germany-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 200 kta (kilo metric ton per annum per annum) Germany-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

Acrylic Acid Production from 3-Hydroxypropionic Acid

This report presents the economics of Acrylic Acid production from 3-hydroxypropionic acid (3-HP). 3-HP is submitted to a dehydration reaction to generate Glacial Acrylic Acid. The reaction is carried out in vapor phase in a reactor column. The economic analysis approaches a plant located in the United States.

Details: 150 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue M   From $799 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.

Ammonia Production from Syngas

This report presents the economics of Ammonia production from synthesis gas (syngas). In this process, hydrogen, recovered from syngas feedstock, and nitrogen, recovered from air, react producing Ammonia. The economic analysis performed assumes a plant located in the United States.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 800 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.

Ammonia Production from Natural Gas (Combined Reforming)

This report presents the economics of Ammonia production from natural gas in the United States using a process similar to KBR Purifier process. In the process examined, syngas is initially produced from natural gas via a combined reforming. The syngas is purified through several steps into nitrogen and hydrogen which are synthesized to ammonia.

Details: 800 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $1,199 USD

The cost analyses presented in this report target a 800 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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