Methyl Mercaptan from Natural Gas, Sulfur and Methanol (H2 Intermediate)
Methyl Mercaptan Production Costs Report | Issue C | Q2 2024
Report Details |
50 kta United States-based plant | Q2 2024 | 107 pages | Delivered in PDF |
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.
Report Abstract
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.
The report provides a comprehensive study of Methyl Mercaptan production and related Methyl Mercaptan production cost, covering three key aspects: a complete description of the Methyl Mercaptan production process examined; an in-depth analysis of the related Methyl Mercaptan plant capital cost (Capex); and an evaluation of the respective Methyl Mercaptan plant operating costs (Opex).
The Methyl Mercaptan production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Methyl Mercaptan plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Methyl Mercaptan plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic
Hydrogen Synthesis. In a partial oxidation (POX) reactor, natural gas is partially oxidized with air, forming carbon monoxide and hydrogen, with steam added to promote a CO shift reaction that generates additional hydrogen and carbon dioxide. Next, a water-gas shift is promoted by adding more steam to the POX reactor outlet stream, reacting with the remaining carbon monoxide to produce more hydrogen and carbon dioxide. Water is removed via condensation, and carbon dioxide and other impurities are removed using a pressure swing adsorption (PSA) system, leaving pure hydrogen to be used for H2S production.
H2S Synthesis. In a packed bed reactor, hydrogen is bubbled into molten sulfur, forming a reaction mixture that passes through a catalyst bed, generating H2S. The stream leaving the reactor is quenched, then cooled in heat exchangers to recover vaporized sulfur. The H2S proceeds to methyl mercaptan synthesis.
Methyl Mercaptan Synthesis. First, vaporized methanol is mixed with H2S to form a feed stream with the desired molar ratio. The mixture is then 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.
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 MSH Synthesis reactor feed. 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.
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Production Process Information
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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
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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 from Natural Gas, Methanol and Sulfur (Carbon Disulfide Co-Product)
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.
Details: 50 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $5,500 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 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 | Q2 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.
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