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Thermal degradation and kinetic analysis of organic constituents in coal-gasification wastewater with a novel treatment

机译:一种新的煤气化废水有机成分的热降解和动力学分析

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The traditional treatment of coal-gasification wastewater produces high solvent and operation cost, secondary pollution and long processing cycle. The aim of the paper was to attempt an alternative approach of wastewater treatment in coal gasification process. With wastewater being heated and sprayed into the gasifier, water participates in the water-gas shift reaction; meanwhile, organic constituents in wastewater are thermally degraded in specific conditions. In the study, thermal degradation and kinetic analysis of COD and NH3-N from Lurgi coal-gasification wastewater were conducted experimentally. The results showed that COD degradation can be divided into three reaction regions: 200-600, 600-1000 and 1000-1200 degrees C. Also, NH3-N degradation can be divided as 200-400, 400-800 and 800-1200 degrees C. The reaction temperature, oxygen concentration and reaction residence time can improve organic constituents' degradation rate. The COD and NH3-N degradation rate ranks in the order oxidative inert reductive. It is because increasing oxygen concentration indicates more free radical generation and aromatic hydrocarbon polymerization was weakened. In addition, NO conversion with NH3 occurs within a narrow temperature window (800-1000 degrees C). Thus, NO concentration reached the peak 230 mg/m(3) at 800 degrees C and then reduced with the increase in reaction temperature. Furthermore, a pseudo-first-order reaction model was implemented to analyse the kinetics of COD and NH3-N degradation rate. The results of the present study indicate that the proposed wastewater treatment is feasible and can be preferable reference for further practical application.
机译:煤气化废水的传统治疗产生了高溶剂和运营成本,二次污染和长加工周期。本文的目的是尝试煤气化过程中废水处理的替代方法。将废水加热并喷洒到气化炉中,水参与水 - 气体换档反应;同时,废水中的有机成分在特定条件下热降解。在实验中进行了研究,通过LURGI煤气化废水进行鳕鱼和NH3-N的热降解和动力学分析。结果表明,COD劣化可分为三个反应区:200-600,600-1000和1000-1200℃。此外,NH3-N降解可分为200-400,400-800和800-1200度C.反应温度,氧浓度和反应停留时间可以提高有机成分的降解速率。 COD和NH3-N的降解速率在氧化顺序>惰性>还原时排列。这是因为增加氧浓度表明更自由基产生,芳族烃聚合削弱。此外,在窄温度窗口(800-1000℃)内不会发生与NH3的转化。因此,在800℃下没有浓度达到峰230mg / m(3),然后随着反应温度的增加而降低。此外,实施了伪一阶反应模型以分析COD和NH3-N降解率的动力学。本研究结果表明,所提出的废水处理是可行的,可以对进一步的实际应用进行优选参考。

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