Scholarlink

<p>The increasing global energy demand,&#xa0;the decline in fossil fuels and the growing amount of municipal solid waste are major environmental and socioeconomic issues, calling for advanced techniques to recycle waste into energy. Here, we review the thermochemical valorization of household, industrial and agricultural waste, with focus on municipal solid waste composition, fuel production, fuel characteristics, legislation and standards. Processes include pyrolysis, gasification, and incineration, e.g. in cement kilns. We found that refuse-derived fuel has a calorific value of 8–20&#xa0;MJ kg<sup>−1</sup>, a moisture content of 8–40% and an ash content of 4–20%. Optimized refused-derived fuel pyrolysis can yield up to 67.9 wt% liquid oil, while gasification produces syngas with heating values up to 10.9 MJ m<sup>−3</sup>. In cement kilns, co-processing achieves thermal substitution rates of 50–60% in rotary kilns and 80–100% in calciners. Limitations comprise variability in the composition of the feedstock, tar formation and control of emissions.</p>

错误：搜索内容不能为空，请输入英文关键词
错误：关键词超出字数限制，请精简
高级检索

Thermochemical conversion of waste into energy: a review

  • 期刊论文

  • 出版模式：

    开放获取

  • 发表日期：

    2025年11月3日

查看全文
  • Cui Quan,
  • Voninirina Safidy Ravelomanantsoa,
  • Leire Olazar,
  • Laura Santamaria,
  • Gartzen Lopez,
  • Li Liu,
  • Ningbo Gao

摘要

The increasing global energy demand, the decline in fossil fuels and the growing amount of municipal solid waste are major environmental and socioeconomic issues, calling for advanced techniques to recycle waste into energy. Here, we review the thermochemical valorization of household, industrial and agricultural waste, with focus on municipal solid waste composition, fuel production, fuel characteristics, legislation and standards. Processes include pyrolysis, gasification, and incineration, e.g. in cement kilns. We found that refuse-derived fuel has a calorific value of 8–20 MJ kg−1, a moisture content of 8–40% and an ash content of 4–20%. Optimized refused-derived fuel pyrolysis can yield up to 67.9 wt% liquid oil, while gasification produces syngas with heating values up to 10.9 MJ m−3. In cement kilns, co-processing achieves thermal substitution rates of 50–60% in rotary kilns and 80–100% in calciners. Limitations comprise variability in the composition of the feedstock, tar formation and control of emissions.