<p>The melting time of hydrogen direct reduced iron pellets (H-DRI) is a limiting factor for productivity in electric arc furnace steelmaking for fossil-free steel. The effect of material and process parameters on melting time was evaluated under laminar conditions using computational fluid dynamics. The study found that the melting time of H-DRI is primarily determined by the properties of the slag bath and its movement, with H-DRI properties being secondary. The shortest melting time was achieved by combining high temperature (&gt;&#xa0;1950 K), high viscosity foam (&gt;&#xa0;0.1&#xa0;Pa&#xa0;s), and high thermal conductivity (&gt;&#xa0;0.9 W m<sup>−1</sup> K<sup>−1</sup>) of the slag. With optimal conditions a melting time of 4.56 seconds was observed for a 10 mm diameter H-DRI, although thicker slag with lower terminal velocity was shown to have greater potential for complete melting of the pellet within the slag. Decreasing H-DRI porosity from 65 to 50&#xa0;pct with maintained mass increases melting time by 4&#xa0;pct and increasing initial temperature from 300 K to 1100 K decreases melting time by 20&#xa0;pct. Furthermore, an increased bath temperature from 1850&#xa0;K to 1950&#xa0;K results in approximately 55&#xa0;pct reduction in melting time due to increased superheat. Forced convection in the system was also found to significantly reduce the melting time for H-DRI.</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

Numerical Study on the Effect of Material Parameters and Process Conditions on the Melting Time of Hydrogen-Direct Reduced Iron

  • Jonas Svantesson,
  • Niklas Kojola,
  • Mikael Ersson

摘要

The melting time of hydrogen direct reduced iron pellets (H-DRI) is a limiting factor for productivity in electric arc furnace steelmaking for fossil-free steel. The effect of material and process parameters on melting time was evaluated under laminar conditions using computational fluid dynamics. The study found that the melting time of H-DRI is primarily determined by the properties of the slag bath and its movement, with H-DRI properties being secondary. The shortest melting time was achieved by combining high temperature (> 1950 K), high viscosity foam (> 0.1 Pa s), and high thermal conductivity (> 0.9 W m−1 K−1) of the slag. With optimal conditions a melting time of 4.56 seconds was observed for a 10 mm diameter H-DRI, although thicker slag with lower terminal velocity was shown to have greater potential for complete melting of the pellet within the slag. Decreasing H-DRI porosity from 65 to 50 pct with maintained mass increases melting time by 4 pct and increasing initial temperature from 300 K to 1100 K decreases melting time by 20 pct. Furthermore, an increased bath temperature from 1850 K to 1950 K results in approximately 55 pct reduction in melting time due to increased superheat. Forced convection in the system was also found to significantly reduce the melting time for H-DRI.