煤炭工程 ›› 2022, Vol. 54 ›› Issue (10): 176-181.doi: 10.11799/ce202210033

• 研究探讨 • 上一篇    下一篇

不同负载方式金属离子催化条件下浮选尾煤-松枝共热解气体产物研究

冯来宏,李继升,殷裁云,顾雷雨,徐浩,孙福龙   

  1. 华能煤炭技术研究有限公司
  • 收稿日期:2022-01-16 修回日期:2022-03-03 出版日期:2022-10-14 发布日期:2023-01-06
  • 通讯作者: 冯来宏 E-mail:285728294@qq.com

Effects of three different loading methods of iron, calcium and potassium ions on gas phase products of flotation tailings and pine branch co-pyrolysis

feng laihong   

  • Received:2022-01-16 Revised:2022-03-03 Online:2022-10-14 Published:2023-01-06
  • Contact: feng laihong E-mail:285728294@qq.com

摘要: 为实现浮选尾煤高价值利用,以沙曲选煤厂浮选尾煤为原料,利用固定床反应器,采用不同负载方式的铁、钙、钾离子对浮选尾煤与松枝共催化热解制备富氢燃料气。结果表明:添加催化剂后,浮选尾煤与松枝共热解试验半焦产率明显降低,气体产率显著增长,表明催化剂的添加对共热解气体产物产率和热值具有促进作用,其促进作用由强到弱依次为:Fe系催化剂>Ca系催化剂>K系催化剂。负载方式会不同程度地促进催化热解产气,就气体产物热值而言,由强到弱依次为负载型>浸渍混合型>机械混合型|对于目标气体H2而言,由强到弱依次为浸渍型>负载型>机械混合型|对于目标气体CO,催化剂负载方式无明显影响。添加K系催化剂对CH4产率呈抑制趋势|催化剂对CO2产率的抑制作用由强到弱为K系催化剂>Ca系催化剂>Fe系催化剂。

关键词: 浮选尾煤高价值利用, 生物质共热解, 负载型催化剂, 改性煤矸石, 金属离子

Abstract: Flotation tailings is mainly stockpiled in coking coal preparation plants in China, which has caused serious environmental pollution, and its high-value application is imminent. In this paper, the flotation tail coal of Shanxi Coking Coal Group was selected as raw material, and the hydrogen rich fuel gas was prepared by co-catalytic pyrolysis of flotation tailings and pine branch after loading iron, calcium and potassium ions in different load methods in a fixed bed reactor. The results show that after the addition of catalyst, the semi-coke yield of flotation tailings and pine branch co-pyrolysis test decreases significantly, and the gas yield increases significantly, indicating that the addition of catalyst has a positive role in promoting the gas product yield and calorific value of co-pyrolysis. In general, iron-series catalyst > calcium-series catalyst > potassium-series catalyst. The different preparation methods of catalysts also have different effects on the co-pyrolysis gas products. As for the calorific value of gas products, the order from strong to weak is loading type > impregnation mixing type > mechanical mixing type; For the H2 yield of the target gas product, the order from strong to weak is impregnation mixing type > loading type > mechanical mixing type; There is no significant difference in the load methods of the catalyst for the CO yield of the target gas product; As for the yield of the target gas product CH4, the addition of potassium-series catalyst inhibited it; For the CO2 yield of the target gas product, the inhibitory effect of the catalyst on it from strong to weak is potassium-series catalyst > calcium-series catalyst > iron-series catalyst. These experimental results hope to provide industrial reference for the high-value application of the co-catalytic pyrolysis system of flotation tailings and pine branch.

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