Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: E
ICC - Volume: 375
ICC - Report ID: 375-E
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Dimethyl Ether Production from Synthesis Gas (Direct Method)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 375-A,375-G,375-J,375-B,375-C,375-D,375-F,375-H,375-I
ICC - Related Reports List: 275-B,275-A
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/375-E.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Dimethyl Ether</b>. Dimethyl Ether (a.k.a. DME), is the simplest aliphatic ether, containing only two carbon atoms. This organic compound has been used in the production of the methylating agent dimethyl sulfate, as an aerosol propellant, coolant and in a number of other applications. More recently, DME has attracted considerable attention as a synthetically produced alternative to diesel, able to produce clean energy in the future.</p> <h6>Raw Material</h6> <p><b>Synthesis Gas</b>. Synthesis gas is a gas mixture mainly composed of carbon monoxide (CO) and hydrogen (H2). It is a raw material for the production of various products, such as methanol, hydrogen, carbon monoxide, dimethyl ether, oxo alcohols and many other chemicals. Syngas may be produced from both fossil sources (e.g. coal, petroleum or natural gas) and renewable materials, such as biomass or wood. Synthesis gas is produced industrially via different routes including steam methane reforming, partial oxidation, and dry reforming. Its composition can significantly vary from the production method used. </p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/375-E.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) DME Synthesis; and (2) Purification.</p><p>DME synthesis. The syngas provided via a pipeline from a nearby facility is compressed to 50 bar and then fed to a fixed-bed synthesis reactor, in which it is directly converted to DME. Such direct synthesis of DME is carried out in the presence of a bifunctional zeolite-based catalyst system (Cu-Zn-Al/ZSM-5 catalyst). The reactor outlet gas is mainly comprised of DME, methanol, CO2 and unconverted hydrogen and CO.</p><p>Purification. The effluent from DME synthesis is cooled, and DME and methanol are separated from the gases by condensation. The separated gas is partially recycled to the DME synthesis, with a small purge. The DME-methanol condensate stream is then passed through distillation columns. In the CO2 column, absorbed gases – mostly carbon dioxide, unconverted carbon monoxide and methane present in the syngas feed – are removed from the DME and burned for fuel. In the DME column, DME product is purified from methanol and directed to storage facilities located outside battery limits. Finally, wastewater is separated in the methanol column and the methanol obtained is recycled to the DME synthesis.</p>
ICC - Short Description: The report presents the economics of Dimethyl Ether (DME) production from synthesis gas (syngas) through a one-step process. In this process, syngas is reacted in the presence of a bifunctional catalyst that supports methanol syntheses and the subsequent dehydration of methanol to DME within a single reactor. The economic analysis performed assumes a plant located in the United States.
ICC - Main Product: Dimethyl Ether
ICC - Plant Capacity: 150.00
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Dimethyl Ether Production from Synthesis Gas (Direct Method)

Dimethyl Ether Production Costs Report | Issue E | 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

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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 Dimethyl Ether 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 Dimethyl Ether 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 Dimethyl Ether 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 Dimethyl Ether 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 Dimethyl Ether Production Cost Reports

Dimethyl Ether Production from Natural Gas & CO2 (Direct Method)

The report presents the economics of Dimethyl Ether (DME) production from natural gas and carbon dioxide (CO2). In the process under analysis, natural gas is reformed with CO2 yielding synthesis gas (syngas). Syngas is then fed to a one-step process for DME generation - syngas conversion into methanol and methanol dehydration into DME are carried out in a single reaction step. The economic analysis performed assumes a plant located in the United States.

Details: 110 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   From $1,499 USD

The cost analyses presented in this report target a 110 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.

Dimethyl Ether from CO2-Rich Natural Gas (CO2 Removal Pre-Treatment)

This report presents the economics of Dimethyl Ether (DME) production from natural gas with high CO2 content in the United States. The process under analysis consists of four major steps. The first step comprises an amine treatement of natural gas for the removal of CO2. In the second step, natural gas is fed to a combined reforming process producing synthesis gas (syngas) which is, subsequently, converted into methanol. The final step consists of the catalytic dehydration of methanol to generate DME.

Details: 1,020 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue I   From $5,000 USD

The cost analyses presented in this report target a 1,020 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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Isononanol Production from Octenes (Rhodium Catalyst)

This report presents an economic study of Isononanol production from octenes in the presence of a rhodium catalyst. It assumes a plant located in the United States using a process similar to Johnson Matthey OXO alcohols process. Initially, octenes are submitted to hydroformylation to form the respectives C9 aldehydes. The aldehydes are then hydrogenated to the corresponding C9 alcohols.

Details: 220 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

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Details: 220 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 220 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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