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ACS Catalysis· 2015Q1

Methanol to Olefins (MTO): From Fundamentals to Commercialization

Peng Tian, Yingxu Wei, Mao Ye, Zhongmin Liu

Short summary

A 2010 coal-to-olefin plant in China, developed by DICP, demonstrates the successful commercialization of Methanol-to-Olefins (MTO) technology.

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Key points

  • DICP developed MTO technology, enabling the world's first coal-to-olefin plant in 2010.
  • Process development involved studies on reaction mechanism, molecular sieve synthesis, and catalyst scale-up.
  • Reactor selection, scale-up, process demonstration, and commercialization were critical steps.
  • Future research directions include fundamental challenges and catalyst improvements.

AI-generated from the title and abstract; the full text is not read.

Abstract

High Resolution Image Download MS PowerPoint Slide The methanol-to-olefins (MTO) reaction is an interesting and important reaction for both fundamental research and industrial application. The Dalian Institute of Chemical Physics (DICP) has developed a MTO technology that led to the successful construction and operation of the world’s first coal to olefin plant in 2010. This historical perspective gives a brief summary on the key issues for the process development, including studies on the reaction mechanism, molecular sieve synthesis and crystallization mechanism, catalyst and its manufacturing scale-up, reactor selection and reactor scale-up, process demonstration, and commercialization. Further challenges on the fundamental research and the directions for future catalyst improvement are also suggested.

The authors' abstract, as published at the source. ACS Catalysis, 2015 · DOI ↗

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Field: Inorganic Chemistry

Inorganic ChemistryChemistry