Commodity Production Costs Report

Dimethyl Ether Production from Methanol

Dimethyl Ether Operating Costs & Plant Construction Costs

180 kta United States-based plant | 107 Pages | Issue A | Q3 2024
Starting at $799 USD | See Report Editions Prices

This report presents the economics of Dimethyl Ether (DME) production from methanol. The process under analysis is the conventional dehydration process, in which methanol is reacted in the presence of a catalyst, yielding DME and water. Unconverted methanol contained in the reactor effluent is recovered reused in the process. The economic analysis performed assumes a plant located in the United States.

The report provides a comprehensive study of Dimethyl Ether production and related Dimethyl Ether production cost, covering three key aspects: a complete description of the Dimethyl Ether production process examined; an in-depth analysis of the related Dimethyl Ether plant capital cost (Capex); and an evaluation of the respective Dimethyl Ether plant operating costs (Opex).

The Dimethyl Ether 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 Dimethyl Ether 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 Dimethyl Ether plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.

Key reference(s): ?

Dimethyl Ether Production Cost Report Process Schematic

The process under analysis comprises two major sections: (1) DME synthesis; and (2) DME purification.

DME Synthesis. Pure methanol is vaporized, superheated and then fed to an adiabatic fixed-bed reactor packed with activated alumina. In the reactor the dehydration reaction of methanol takes place, yielding DME.

DME purification. The reactor effluent, mainly comprising DME product, water and unreacted methanol, is cooled in heat integrations with methanol feed heating and superheating and fed to a distillation column, where DME product is obtained from the column top. The unconverted methanol and water are removed by the column bottoms and sent to a second column for methanol recovery, which is recycled to the synthesis section. Also from the DME column, a gaseous waste stream is taken from the top and scrubbed with methanol before being vented to the atmosphere.

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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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 80 Pages | 22 Tables | 9 Images

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Table of Contents


Features
  • 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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 90 Pages | 28 Tables | 13 Images

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Updated with Q3 2024 Data

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Table of Contents


Features
  • 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
  • See All Features

  • 107 Pages | 34 Tables | 22 Images
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  • Updated with Q3 2024 Data
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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

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Dimethyl Ether Production from Synthesis Gas (Direct Method)

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.

Details: 150 kta United States-based plant | Q3 2024 | 107 pages | Issue E | From $1,199 USD

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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

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Dimethyl Ether from CO2-Rich Natural Gas (Steam & CO2 Reforming)

This report presents the economics of Dimethyl Ether (DME) production from CO2-rich natural gas in the United States. The integrated process under analysis consists of three major steps. Initially, synthesis gas (syngas) is produced from natural gas, CO2 and water via a promising reforming process that combines dry and steam reforming. Then, the syngas is converted into methanol. The final step consists of the catalytic dehydration of methanol to generate DME.

Details: 1020 kta United States-based plant | Q3 2024 | 107 pages | Issue J | From $5,900 USD

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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: 1700 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD

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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: 1000 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD

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