Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 250
ICC - Report ID: 250-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: L-Lysine-HCl Production from Glucose
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 250-B,250-C
ICC - Related Reports List: 138-F,370-A,138-G
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/250-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>L-Lysine-HCl</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>Ammonium Sulfate</b></p>, <p><b>Hydrochloric Acid</b></p>, <p><b>Ammonia</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/250-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) fermentation; (2) product recovery; and (3) product concentration, drying and packaging.</p><p>Fermentation. The culture media used in fermentation is prepared by mixing process water, glucose and nutrients. The fermentation is performed in fed-batch mode and under aerobic conditions. At the batch phase, the microorganism seed is fed into the fermenters, which were previously filled with the fermentation batch medium. After glucose exhaustion, the batch phase is finished and the fed-batch phase is started, during which, glucose and nutrients are continuously supplied until the desired L-Lysine concentration is achieved. At the end of the fermentation, the broth is sent to a buffer tank to provide a continuous flow in the further process steps.</p><p>Product recovery. The fermentation broth is sent to an ultrafiltration system for the removal of cell debris and other suspended solids. Subsequently, the liquor from ultrafiltration is fed to ion exchange columns, where L-Lysine is selectively adsorbed. The L-Lysine adsorbed is eluted from the ion exchange resins by washing with an aqueous ammonia solution.</p><p>Product concentration, drying and packaging. The L-Lysine eluate from ion exchange columns is mixed with mother liquor from product filtration and concentrated by evaporation. The concentrated lysine solution is acidified with hydrochloric acid, and free L-Lysine is converted to L-Lysine-HCl. Subsequently, the L-Lysine-HCl solution is sent to the crystallizer, and lysine salt is filtered. The mother liquor is recycled to the evaporator and the wet cake is conveyed to dryers. Final dry L-Lysine-HCl (98.5 wt%) is obtained and sent to packaging line before being stored in bags.</p>
ICC - Short Description: This feasibility study approaches an economic analysis of L-Lysine Monohydrochloride (or L-Lysine-HCl) production from glucose syrup in the United States using a conventional fermentation process. The L-Lysine-HCl is recovered via ion-exchange absorption and crystallization.
ICC - Main Product: Lysine
ICC - Plant Capacity: 100.00
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L-Lysine-HCl Production from Glucose

Lysine Production Costs Report | Issue A | Q2 2024

Production Cost Report

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Report Details
100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 100 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

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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

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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 Lysine 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 Lysine 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 Lysine 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 Lysine 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 Lysine Production Cost Reports

L-Lysine-HCl Production from Raw Sugar

This report presents the economics of Lysine production from raw sugar (sucrose). Sucrose is initially hydrolyzed into glucose and fructose (invert sugar). The invert sugars are then fermented to produce L-Lysine, which is recovered as L-Lysine-HCl. The economic analysis provided assumes a plant located in Germany.

Details: 100 kta Germany-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 100 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.

L-Lysine Sulfate Production from Glucose

This report approaches the economics of L-Lysine Sulfate production from glucose syrup. In the process examined, glucose syrup is submitted to fed-batch fermentation to produce L-Lysine. The economic analysis provided assumes a plant located in the United States.

Details: 100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 100 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

Hydrochloric Acid Production from Hydrogen and Chlorine

This study analysis the economics of Hydrochloric Acid (HCl) production from hydrogen and chlorine in the United States. The process examined is a typical synthesis of Hydrogen Chloride via the direct reaction of the elements. In this process, hydrogen and chlorine, undergo a direct reaction forming hydrogen chloride, which is subsequently passed through an absorber to produce a 35 wt% hydrochloric acid as final product.

Details: 60 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue F   From $799 USD

The cost analyses presented in this report target a 60 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.

Hydrochloric Acid from Sodium Chloride (Sodium Hydroxide as Co-Product)

This report presents the economics of Hydrochloric Acid production via an integrated plant comprising: 1) a typical chlor-alkali electrolysis process using membrane cells; and 2) the production of Hydrochloric Acid from hydrogen and chlorine. A 35 wt% Hydrochloric Acid solution is obtained as the final product and 50 wt% caustic soda is obtained as co-product in this process. The analysis is based on plant located in the United States.

Details: 170 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue G   From $1,199 USD

The cost analyses presented in this report target a 170 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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