The main objective is studying the fundamental aspect, by the mean of the drying kinetics, the application of forced convective drying of wastewater sludge with determination of the optimum drying conditions. The drying system is composed of two units; small samples of 2.5 g are dried in the first unit and bed of sludge weighting 250 g is dried the second unit. The experiments are performed under air temperatures varying between 80°C and 200°C. The range of the air velocity and its humidity is 1- 2 m/s and 0.005- 0.05 kgwater/kgdry air, respectively. The experiments are performed for two different sludges; activated sludge (AS) and thermalized and digested sludge (TDS). Usually, three main drying phases are observed during drying of bed of sludge. These phases are reduced to only two for small samples. Determination of the influent parameters shows that temperature of the drying air and sludge origin can profoundly influence the drying kinetic of the sludge. The exergy analysis of the two units of the drying system allows selecting 140 °C, 2 m/s, 0.05 kgwater/kgdry air as optimum drying condition with an exergy efficiency reaching 90\%.
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机译:主要目的是通过干燥动力学的方式研究基本方面,确定最佳干燥条件,然后对废水进行强制对流干燥。干燥系统由两个单元组成。在第一单元中干燥2.5 g的小样品,在第二单元中干燥重量为250 g的污泥床。实验在80°C至200°C的气温范围内进行。风速和湿度范围分别为1-2 m / s和0.005- 0.05 kg水/ kg干空气。实验是针对两种不同的污泥进行的。活性污泥(AS)和热消化污泥(TDS)。通常,在污泥床干燥期间观察到三个主要的干燥阶段。对于小样本,这些阶段减少到只有两个。进水参数的确定表明,干燥空气的温度和污泥的来源可以深刻影响污泥的干燥动力学。干燥系统两个单元的火用分析允许选择140°C,2 m / s,0.05 kg水/ kg干燥空气作为最佳干燥条件,火用效率达到90%。
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