Mucha Jarosław, Zarzycki Roman
Department of Pipelines and Sewage Pipelines, Faculty of Civil Engineering, Architecture and Environmental Engineering, Technical University of Łódź, al. Politechniki 6, 90-924 Łódź, Poland.
Water Res. 2008 Jun;42(12):3025-32. doi: 10.1016/j.watres.2007.11.012. Epub 2007 Nov 19.
The authors propose a new technique to analyse a complex process of wet oxidation of excess sewage sludge by separating thermohydrolysis that results in the separation of sewage sludge into hydrolysates: solid and liquid products, from the basic process of oxidation of the two products. Wet oxidation kinetics was studied at different temperatures of both products based on the measurement of total organic carbon during the process with the use of a PARR high-pressure reactor. Decomposition of the liquid product leads to the formation of non-degradable and gaseous final products, while degradation of the solid product-via an intermediate liquid product-also leads to the formation of final and gaseous products. Solution of the kinetic equations that describe the dependence of relative organic carbon concentration on time is well illustrated by experimental results. On the basis of fitting theoretical curves to the experimental results, the kinetic parameters of the process were determined.
作者提出了一种新的技术,通过将热水解(导致污水污泥分离成水解产物:固体和液体产物)与两种产物的基本氧化过程分离,来分析过量污水污泥的复杂湿式氧化过程。基于使用PARR高压反应器在该过程中对总有机碳的测量,研究了两种产物在不同温度下的湿式氧化动力学。液体产物的分解导致形成不可降解的气态最终产物,而固体产物通过中间液体产物的降解也导致形成最终气态产物。描述相对有机碳浓度随时间变化的动力学方程的解通过实验结果得到了很好的说明。通过将理论曲线拟合到实验结果,确定了该过程的动力学参数。