化工进展 ›› 2020, Vol. 39 ›› Issue (7): 2606-2611.DOI: 10.16085/j.issn.1000-6613.2019-1792

• 化工过程与装备 • 上一篇    下一篇

废食用菌棒循环流化床气化试验

董磊1,2(), 常加富1, 杜巍涛1, 刘全美1, 董玉平3(), 徐鹏举1   

  1. 1.山东百川同创能源有限公司,山东 济南 250101
    2.山东省生物质能源工程技术研究中心,山东 济南 250101
    3.山东大学高效洁净机械制造教育部重点实验室,山东 济南 250061
  • 出版日期:2020-07-05 发布日期:2020-07-10
  • 通讯作者: 董玉平
  • 作者简介:董磊(1977—),男,高级工程师,从事固体废弃物能源化利用技术与工程应用研究。E-mail:cjf6886@126.com
  • 基金资助:
    公益性行业(农业)科研专项(201503135)

Experiment of gasification of edible fungi residues in circulating fluidized-bed

Lei DONG1,2(), Jiafu CHANG1, Weitao DU1, Quanmei LIU1, Yuping DONG3(), Pengju XU1   

  1. 1.Shandong Baichuan Tongchuang Energy Co. , Ltd. , Jinan 250101, Shandong, China
    2.Biomass Energy Engineering Technology Research Center of Shandong Province, Jinan 250101, China
    3.Key Laboratory of High Efficiency and Clean Mechanical Manufacture, Ministry of Education, Shandong University, Jinan 250061, Shandong, China
  • Online:2020-07-05 Published:2020-07-10
  • Contact: Yuping DONG

摘要:

废菌棒是食用菌生产过程中产生的残余废弃物,其再利用对于资源节约与环境保护具有重要意义。本文采用循环流化床气化炉对废菌棒进行了气化试验,分别研究空气当量比、水蒸气配比对气化炉运行温度、气化燃气组分与热值、焦油含量、气化效率及碳转化率等气化特性的影响规律。结果表明:空气当量比由0.20增大至0.35时,循环流化床运行温度与碳转化率升高,气化燃气中的CO2体积分数增大,CO与焦油含量及气化燃气热值下降,气化效率呈现先增大后减小的趋势;空气当量比为0.26时气化效率达到最大74.86%,此时燃气热值为5.59MJ/m3。以空气为主气化介质,采用水蒸气作为辅助气化剂,可以改善气化燃气品质,提升气化效率。当空气当量比为0.26、水蒸气配比为0.2时,废菌棒具有较好的空气-水蒸气气化特性,燃气热值与气化效率分别达到最大值6.14MJ/m3与83.73%。

关键词: 生物质, 气化, 循环流化床, 废菌棒, 合成气

Abstract:

There are many wasted fungus inoculation bag residues in the process of edible fungi production. The recycle of edible fungi residues is important for conserving resources and protecting the environment. A circulating fluidized bed gasification pilot plant was built to study the effect of air equivalence ratio and steam/biomass ratio of raw materials on gasification characteristics, including reaction temperature, gas composition, calorific value, tar content in produced gas, gasification efficiency, and carbon conversion rate. The results showed that the operating temperature of circulating fluidized bed gasifier, carbon conversion rate and the content of CO2 increased with the increase of air equivalence ratio (from 0.20 to 0.35), while the content of CO, calorific value and tar content decreased. The gasification efficiency increased first and then decreased. When air equivalence ratio was 0.26, the gasification efficiency reached the maximum of 74.86% and calorific value reached 5.59MJ/m3. The results also showed that gas quality and gasification efficiency were improved with air as main gasifying agent and steam assisted. When the operation conditions were 0.26 of air equivalence ratio and 0.2 of steam/biomass ratio, gas calorific value and gasification efficiency reached to maximum value of 6.14MJ/m3 and 83.73%, respectively.

Key words: biomass, gasification, circulating fluidized bed, wasted fungus inoculation bag, syngas

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