Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 247
ICC - Report ID: 247-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: DL-Methionine from Methional and Hydrogen Cyanide
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 247-B,247-C,247-D,247-F,247-G,247-E,247-H
ICC - Related Reports List: 361-B,361-A,265-A,265-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/247-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>DL-Methionine</b></p></b></p> <h6>Raw Materials</h6> <p><b>Carbon Dioxide</b></p>, <p><b>Hydrogen Cyanide</b></p>, <p><b>Methional</b></p>, <p><b>Potassium Carbonate</b></p>, <p><b>Ammonia</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/247-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) Hydantoin Production; (2) Hydantoin Hydrolysis; (3) DLM Production and Filtration; and (4) Drying</p><p>Hydantoin production. An aqueous solution of MMP, HCN, of carbon dioxide and ammonia is fed to the hydantoin primary reactor. A gas stream containing CO2, NH3 and impurities leaves the reactor and is washed with MMP and water in a scrubbing column. Purified CO2 leaves the overheads and is used in DLM production. The mixture leaving the reactor is fed to the hydantoin secondary reactor, where the reaction is completed.</p><p>Hydantoin hydrolysis. The hydantoin product stream and potassium carbonate (K2CO3) are fed to the hydrolysis reactive column. CO2 and NH3 are liberated in the overhead stream of the column and recycled to the hydantoin primary reactor. The bottom stream containing potassium methioninate (KMET) is sent to DLM production. The K2CO3 is obtained from the regeneration of a potassium bicarbonate (KHCO3) solution from DLM filtration. This occurs in a decarbonator, where CO2 is separated in the overheads and directed to the DLM reactor.</p><p>DLM production and filtration. The KMET stream and recycled CO2 are fed to the DLM reactor, forming KHCO3 and DLM. The DLM is fed to two vacuum crystallizers. Next, DLM crystals are directed to a vacuum filter. The resulting filtrate containing KHCO3 is sent to the decarbonator.</p><p>Drying. The methionine cake is directed to a dryer. The evaporated water is fed to a wash column and reused in methionine washing during filtration. Methionine product (99 wt%) is obtained and sent to packaging and storage in warehouses.</p><p></p>
ICC - Short Description: This report provides the economics of DL-Methionine production from methional and hydrogen cyanide (HCN) in the United States via a typical carbonate process. Initially, methional is reacted with HCN, ammonia and carbon dioxide to produce 5-(2-methylmercaptoethyl)-hydantoin (MMEH), which is hydrolyzed to potassium methioninate (KMET). Finally, the KMET is acidified, liberating methionine.
ICC - Main Product: Methionine
ICC - Plant Capacity: 150.00
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DL-Methionine from Methional and Hydrogen Cyanide

Methionine Production Costs Report | Issue A | Q3 2024

Production Cost Report

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150 kta United States-based plant   |   Q3 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 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 Methionine 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 Methionine 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 Methionine 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 Methionine 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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Methionine Hydroxy Analog from Acrolein, Methyl Mercaptan and HCN

This study presents the economics of Methionine Hydroxy Analog production from acrolein, methyl mercaptan, and hydrogen cyanide (HCN) in the United States. In this process, acrolein and methyl mercaptan are reacted to form methional. The methional reacts with HCN to produce hydroxy methylthiobutyronitrile (HMBN) intermediate, which is hydrolyzed to Methionine Hydroxy Analog.

Details: 150 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue F   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.

DL-Methionine from Propylene, Methyl Mercaptan and HCN

This study presents the economics of an integrated process for DL-Methionine production starting from propylene in the USA. Initially, propylene is oxidized to acrolein, which is then reacted with methyl mercaptan to generate methional. Finally, methional is reacted with hydrogen cyanide (HCN) to form methionine via a typical carbonate process.

Details: 150 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   From $1,499 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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Other Related Production Cost Reports

Hydrogen Cyanide from Ammonia and Natural Gas (With Air)

This study provides the economics of Hydrogen Cyanide production in the United States using a direct synthesis method similar to Andrussow process, which involves the reaction of ammonia, methane (natural gas), and air to produce HCN.

Details: 100 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   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.

Hydrogen Cyanide from Ammonia and Natural Gas (Without Air)

This report provides the economics of Hydrogen Cyanide production in the United States using a direct synthesis method similar to BMA (Blausäure-Methan-Ammoniak) process, which involves the reaction of ammonia and methane (natural gas) without air.

Details: 60 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   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.

Methional Production from Acrolein and Methyl Mercaptan

This report presents the economics of Methional production from acrolein and methyl mercaptan in the United States, via a typical reaction in the presence of triethanolamine.

Details: 40 kta United States-based plant   |   Q3 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.

Methional Production from Propylene and Methyl Mercaptan

This report presents the economics of Methional production from propylene and methyl mercaptan in the United States, via a typical process. In the process examined, propylene is oxidized to acrolein, which is then reacted with methyl mercaptan to generate Methional.

Details: 40 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $1,199 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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