The effect of aeration rate and feedstock density on biodrying performance for wet refuse-derived fuel quality improvement

Tanik Itsarathorn, Sirintornthep Towprayoon, Chart Chiemchaisri, Suthum Patumsawad, Awassada Phongphiphat, Abhisit Bhatsada, Komsilp Wangyao
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Abstract

This study investigates the effect of aeration rate and feedstock density on the biodrying process to improve the quality of type 2 wet refuse-derived fuel. The aeration rate and feedstock density were varied to investigate these parameters’ effect on the system’s performance. The experiments used 0.3 m3 lysimeters with continuous negative ventilation and five days of operation. In Experiment A, aeration rates of 0.4, 0.5, and 0.6 m3/kg/day were tested with a feedstock bulk density of 232 kg/m3. In Experiment B, the optimum aeration rates determined in Experiment A (0.5 and 0.6 m3/kg/day) were used, and the feedstock density was varied (232 kg/m3, 250 kg/m3, and 270 kg/m3). The results showed that an aeration rate of 0.5 m3/kg/day was the most efficient for a feedstock density of 232 kg/m3; when the aeration rate was increased to 0.6 m3/kg/day, a feedstock density of 250 kg/m3 was the most effective. However, a feedstock density of 270 kg/m3 was not found to be practical for use in the quality improvement system. When the feedstock density is increased, the water in the feedstock and the water resulting from the biodegradation process cannot evaporate due to the feedstock layer’s low porosity, and the system requires an increased aeration rate. Furthermore, the increase in density scaled with increased initial volatile solid content, initial organic content, and initial moisture content, which significantly impacted the final moisture content based on multivariate regression analysis.
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曝气率和进料密度对改善湿式垃圾衍生燃料质量的生物干燥性能的影响
为了提高2型湿式垃圾衍生燃料的质量,研究了曝气率和进料密度对生物干燥过程的影响。研究了曝气率和进料密度对系统性能的影响。实验采用0.3 m3渗血仪,连续负通气,操作5天。在实验A中,曝气率分别为0.4、0.5和0.6 m3/kg/d,原料堆积密度为232 kg/m3。试验B采用试验A确定的最佳曝气速率(0.5和0.6 m3/kg/d),料密度分别为232 kg/m3、250 kg/m3和270 kg/m3。结果表明:当进料密度为232 kg/m3时,曝气速率为0.5 m3/kg/d时效率最高;当曝气量增加到0.6 m3/kg/d时,250 kg/m3的进料密度最有效。然而,270 kg/m3的原料密度在质量改进系统中并不实用。当进料密度增加时,由于进料层孔隙率低,进料中的水分和生物降解过程产生的水分无法蒸发,系统需要增加曝气速率。此外,根据多元回归分析,密度的增加与初始挥发性固形物含量、初始有机含量和初始水分含量的增加成正比,对最终水分含量有显著影响。
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