Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 422
ICC - Report ID: 422-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Methyl Mercaptan from Natural Gas, Methanol and Sulfur (Carbon Disulfide Co-Product)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 422-C,422-B
ICC - Related Reports List: 247-F,247-D,001-A,001-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/422-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Methyl Mercaptan</b>, <b> Carbon Disulfide</b>.</p> <h6>Raw Materials</h6> <p><b>Methanol</b>, <b> Chemicals</b>, <b> Sulfur</b>, <b> Natural Gas</b>.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/422-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) H2S Synthesis; (2) CS2 Separation; (3) Methyl Mercaptan Synthesis; and (4) Methyl Mercaptan Separation.</p><p>H2S Synthesis. The process begins with pre-heating natural gas and sulfur in a furnace. The heated stream is then fed to packed bed tubular reactors where methane reacts with sulfur to produce carbon disulfide (CS2) and hydrogen sulfide (H2S). The product stream is then cooled in a waste heat boiler to recover heat as steam, and the cooled gases proceed to the CS2 Separation section.</p><p>CS2 Separation. Excess sulfur is removed from the product stream using a scrubbing system with light oil as the scrubbing fluid. The sulfur is separated from the oil and recycled to the furnace. The scrubbed stream, containing CS2 and H2S, then proceeds to an absorption step where CS2 is absorbed in light oil and separated from H2S. The absorbed CS2 is further purified through a series of distillation steps and a caustic wash, resulting in pure CS2 as a by-product.</p><p>Methyl Mercaptan Synthesis. H2S is compressed along with methanol in a two-stage compressor. The vaporized methanol is then mixed with the compressed H2S to achieve the desired molar ratio. The mixture is preheated and fed to a packed bed tubular reactor where it reacts to form methyl mercaptan (MSH) and water. The reactor effluent is cooled and sent to the purification stages.</p><p>Methyl Mercaptan Separation. The reactor effluent is first condensed, creating an organic and an aqueous condensate; the uncondensed stream being washed with methanol, which is then mixed with the aqueous condensate. Unreacted H2S is recycled to the compressor. Both condensates undergo distillation to recover Methyl Mercaptan, methanol, and remove impurities. Methyl mercaptan is further distilled, separating it from dimethyl sulfide and other components. The purified MSH is then stored as the final product.</p>
ICC - Short Description: This study presents the economics of Methyl Mercaptan production from natural gas, methanol and sulfur in the USA. In this process, sulfur and natural gas are reacted to produce hydrogen sulfide and carbon disulfide. Subsequently, hydrogen sulfide and methanol are reacted to produce Methyl Mercaptan.
ICC - Main Product: Methyl Mercaptan
ICC - Plant Capacity: 50.00
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Methyl Mercaptan from Natural Gas, Methanol and Sulfur (Carbon Disulfide Co-Product)

Methyl Mercaptan Production Costs Report | Issue A | Q4 2024

Production Cost Report

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

This report presents a cost analysis of a 50 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 Methyl Mercaptan 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 Methyl Mercaptan 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 Methyl Mercaptan 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 Methyl Mercaptan 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 Methyl Mercaptan Production Cost Reports

Methyl Mercaptan Production from Hydrogen Sulfide and Methanol

This study presents the economics of Methyl Mercaptan production from hydrogen sulfide and methanol in the USA. In this process, hydrogen sulfide and methanol are reacted to produce Methyl Mercaptan.

Details: 50 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue B   From $999 USD

The cost analyses presented in this report target a 50 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.

Methyl Mercaptan from Natural Gas, Sulfur and Methanol (H2 Intermediate)

This study presents the economics of Methyl Mercaptan production from natural gas, sulfur, and methanol in the USA. In this process, hydrogen is produced from natural gas then reacted with sulfur to obtain hydrogen sulfide. Subsequently, hydrogen sulfide and methanol are reacted to produce Methyl Mercaptan.

Details: 50 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue C   From $1,499 USD

The cost analyses presented in this report target a 50 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

Methanol Production from Natural Gas (Steam Reforming)

This study presents the economics of large-scale Methanol production from natural gas in the United States. In the process examined, natural gas is first converted into synthesis gas (syngas) by means of conventional steam reforming and then the syngas is converted into Methanol.

Details: 1,000 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 1,000 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.

Methanol Production from Natural Gas (Combined Reforming)

This study presents the economics of large-scale Methanol production from natural gas in the United States. In this process, natural gas is first converted into synthesis gas (syngas) by means of conventional steam reforming and secondary autothermal reforming. Then, the syngas is converted into Methanol.

Details: 1,700 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 1,700 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 Production from Acrolein, Methyl Mercaptan and HCN

This report presents the economics of DL-Methionine production from acrolein, methyl mercaptan, and hydrogen cyanide (HCN) in the United States. In this process, refined acrolein and methyl mercaptan are reacted to form MMP (also called methional), which is further reacted with HCN to generate DL-Methionine via a typical carbonate process.

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

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   |   Q4 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.

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