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Polychlorinated dibenzo-p-dioxins and dibenzofurans in a three-stage municipal solid waste gasifier

机译:三级市政固体废物气化炉中的多氯二苯并对二恶英和二苯并呋喃

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The quantified emissions of polychlorinated dibenzo-p-dioxins and polychlorinated dibenzofuran (PCDD/Fs) have not yet been reported comprehensively with the whole gasifier system. In this study, the emission characteristics of PCDD/Fs concentration, toxicity equivalent quantity, reaction mechanism are examined for a three-stage gasification system. This system first features the pyrolysis of municipal solid waste (MSW), next the oxidation of the pyrolysis products and as a final third step its high temperature cracking on two types of char (coal coke and rice husk char). The effect of the reduction temperature (800, 900, and 1000 degrees C) and char type have been experimentally evaluated. In general, the final I-TEQ of PCDD/Fs are controlled at a low level (0.068-0.085 ng I-TEQ/Nm(3)), due to the absence of oxygen and decomposition of PCDD/Fs during reduction at a high temperature. Meanwhile, the PCDD/Fs concentration (P = 4 to 8) decreased significantly, maintaining in a range of 132-1.58 ng/Nm(3). The decrease of 2,3,7,8-tetrachlorodibenzo-p-dioxin (TCDD), 1,2,3,7,8-pentachlorodibenzo-p-dioxin (PeCDD) and 2,3,4,7,8-pentachlorodibenzo-furan (PeCDF) collectively resulted in the decline of total I-TEQ values for coal char after reduction reaction, while the 2,3,7,8-TCDD and 1,2,3,7,8-PeCDD both increased their contribution in total I-TEQ values. The low-chlorinated PCDDs were easier to transform into high-chlorinated PCDDs for coal char during the reduction stage, which is opposite to that for rice husk char. The chlorophenol precursor routes apparently played an increasing role in PCDD/Fs formation with the reduction temperature increasing from 800 to 1000 degrees C. Furthermore, the primary PCDD/Fs formation reactions have converted from the chlorophenol precursor routes (secondary reactions) into de novo reactions for the coal char sample, while the chlorophenol precursor reactions strengthened their leading role during the reduction stage for rice husk char. (C) 2019 Elsevier Ltd. All rights reserved.
机译:尚未对整个气化炉系统中的多氯二苯并-对-二恶英和多氯二苯并呋喃(PCDD / Fs)的定量排放进行全面报道。在本研究中,研究了三级气化系统的PCDD / Fs浓度,毒性当量,反应机理。该系统首先具有城市固体废物(MSW)的热解特性,其次是热解产物的氧化,最后第三步是对两种类型的焦炭(煤焦和稻壳炭)进行高温裂解。还原温度(800、900和1000摄氏度)和焦炭类型的影响已通过实验评估。通常,由于在高浓度还原过程中不存在氧气和PCDD / Fs分解,最终将PCDD / Fs的最终I-TEQ控制在较低水平(0.068-0.085 ng I-TEQ / Nm(3))。温度。同时,PCDD / Fs浓度(P = 4至8)显着降低,维持在132-1.58 ng / Nm(3)的范围内。 2,3,7,8-四氯二苯并-对二恶英(TCDD),1,2,3,7,8-五氯二苯并-对二恶英(PeCDD)和2,3,4,7,8-五氯二苯并呋喃的减少-呋喃(PeCDF)共同导致还原反应后煤焦的总I-TEQ值下降,而2,3,7,8-TCDD和1,2,3,7,8-PeCDD均增加了其贡献I-TEQ总值。在还原阶段,煤焦的低氯化物PCDDs易于转化为高氯化物的PCDDs,与稻壳炭相反。随着还原温度从800升高到1000摄氏度,氯苯酚前体路线显然在PCDD / Fs的形成中起着越来越重要的作用。此外,主要的PCDD / Fs形成反应已从氯酚前体路线(次级反应)转变为从头反应。对于煤焦样品,氯酚前体反应在还原稻壳炭的过程中增强了其主导作用。 (C)2019 Elsevier Ltd.保留所有权利。

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