4.7 Article

Proposal and energy saving analysis of novel methanol ? electricity polygeneration system based on staged coal gasification method

Journal

ENERGY CONVERSION AND MANAGEMENT
Volume 233, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.enconman.2021.113931

Keywords

Coal staged gasification method; Polygeneration system; Thermochemical regenerative process; Energy saving analysis

Funding

  1. National Key Research and Development Program of China [2016YFB0600803]
  2. National Nature Science Foundation of China [51776197]
  3. Youth Innovation Promotion Association CAS

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The coal gasification process plays a significant role in polygeneration systems and can greatly impact system performance. This study integrated a novel methanol-electricity polygeneration system using coal-steam gasification, resulting in a substantial increase in energy efficiency. Through exergy analysis and comparison of energy efficiency, the study demonstrated the system's energy saving potential and the influence of gasification processes on system performance.
The coal gasification process is one of the main exergy destruction contributors in polygeneration systems and has considerable energy saving potential. In the present study, for improving the performance of the poly generation system, the coal-steam gasification method was employed to integrate a novel methanol-electricity polygeneration system. The results indicated that the energy efficiency of the novel system was 63.3% with a chemical-to-power output ratio of 8.4, while the energy efficiency of the traditional system is 51.3% at the optimal unreacted syngas recycling ratio. Exergy analysis results revealed that the system exergy destruction in the coal?steam gasification process is 7.5% smaller than that in the GE gasification process, and eliminating the air separation unit can reduce the exergy destruction of the system by 4.3%. Additionally, the energy saving contributions of gasification process improvement and system integration were quantitatively evaluated. When the chemical-to-power output ratio increased from 1.9 to 11.9, the energy saving contributions of the system integration and gasification process improvement ranged from 9.8% to 15.1% and 11.9% to 12.9%, respectively.

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