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Plant-wide modeling and analysis of the shale gas to dimethyl ether (DME) process via direct and indirect synthesis routes

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  • Mevawala, Chirag
  • Jiang, Yuan
  • Bhattacharyya, Debangsu

Abstract

A plant-wide model of the shale gas to dimethyl ether (DME) process with integrated CO2 capture via direct and indirect synthesis routes has been developed in Aspen Plus V8.4®. In this study, models of the pre-reforming reactor, autothermal reforming (ATR) reactor and DME synthesis reactors using kinetic data have been developed. For CO2 capture, Rectisol and methyl diethanolamine (MDEA)/piperazine (PZ) technologies have been evaluated and results have been compared with the experimental data. A novel DME separation process has been developed and evaluated for efficient separation of DME, syngas, and CO2. Binary interaction parameters for the vapor-liquid equilibrium (VLE) model of the methanol-DME-CO-CO2-H2O-H2 system are regressed using the experimental data. Effects of the key parameters like CO2 recycle ratio and H2/CO ratio on the utility consumption in the syngas synthesis unit, acid gas removal (AGR) unit, DME synthesis unit and DME separation unit are studied. It is observed that the direct shale gas to DME production process operated with an optimal H2/CO ratio of 1 has a higher DME yield and overall equivalent electrical efficiency than the indirect shale gas to DME production process.

Suggested Citation

  • Mevawala, Chirag & Jiang, Yuan & Bhattacharyya, Debangsu, 2017. "Plant-wide modeling and analysis of the shale gas to dimethyl ether (DME) process via direct and indirect synthesis routes," Applied Energy, Elsevier, vol. 204(C), pages 163-180.
    • Handle: RePEc:eee:appene:v:204:y:2017:i:c:p:163-180
    DOI: 10.1016/j.apenergy.2017.06.085
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    References listed on IDEAS

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    1. Jiang, Yuan & Bhattacharyya, Debangsu, 2017. "Techno-economic analysis of direct coal-biomass to liquids (CBTL) plants with shale gas utilization and CO2 capture and storage (CCS)," Applied Energy, Elsevier, vol. 189(C), pages 433-448.
    2. Jiang, Yuan & Bhattacharyya, Debangsu, 2016. "Process modeling of direct coal-biomass to liquids (CBTL) plants with shale gas utilization and CO2 capture and storage (CCS)," Applied Energy, Elsevier, vol. 183(C), pages 1616-1632.
    3. Chen, Hsi-Jen & Fan, Chei-Wei & Yu, Chiou-Shia, 2013. "Analysis, synthesis, and design of a one-step dimethyl ether production via a thermodynamic approach," Applied Energy, Elsevier, vol. 101(C), pages 449-456.
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    Cited by:

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    4. Mevawala, Chirag & Jiang, Yuan & Bhattacharyya, Debangsu, 2019. "Techno-economic optimization of shale gas to dimethyl ether production processes via direct and indirect synthesis routes," Applied Energy, Elsevier, vol. 238(C), pages 119-134.
    5. Mevawala, Chirag & Bai, Xinwei & Hu, Jianli & Bhattacharyya, Debangsu, 2023. "Plant-wide modeling and techno-economic analysis of a direct non-oxidative methane dehydroaromatization process via conventional and microwave-assisted catalysis," Applied Energy, Elsevier, vol. 336(C).
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    9. Ewelina Pawelczyk & Natalia Łukasik & Izabela Wysocka & Andrzej Rogala & Jacek Gębicki, 2022. "Recent Progress on Hydrogen Storage and Production Using Chemical Hydrogen Carriers," Energies, MDPI, vol. 15(14), pages 1-34, July.

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