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燃烧稀释氯化蒸汽的催化氧化器和热氧化器中多氯二苯并对二恶英和二苯并呋喃的排放。

Emissions of polychlorinated dibenzo-p-dioxins and dibenzofurans from catalytic and thermal oxidizers burning dilute chlorinated vapors.

作者信息

Hart John R

机构信息

Department of Toxic Substances Control, California EPA, 8800 Cal Center Drive, Sacramento, CA 95826, USA.

出版信息

Chemosphere. 2004 Mar;54(10):1539-47. doi: 10.1016/j.chemosphere.2003.10.017.

Abstract

Emissions of polychlorinated dibenzo-p-dioxins and dibenzofurans (dioxins) have been found from 57 field tests on the oxidation of low (a few to a few hundred) parts per million levels of chlorinated and non-chlorinated volatile organic compounds (VOCs). The oxidation occurs in catalytic oxidizers with platinum, platinum/palladium or chromium(IV) oxide combustion catalysts, or in thermal oxidizers (without a catalyst). The catalyst inlet temperatures ranged from 293 to 573 degrees C. The thermal oxidizer operating temperatures (post-flame) were from 773 to 927 degrees C. Data of the toxic dioxin and furan isomers are reported and also weighted and expressed as international toxic equivalents (TEQ) of 2,3,7,8-tetrachlorodibenzo-p-dioxin. The maximum stack emissions, 1.07 ng/m3 TEQ, occurred at 293 degrees C. Salient results of this field study are: (1) TEQ levels in the stack exponentially increase with a decrease in operating temperature, an empirical equation is TEQ (ng/dscm)=8.4 exp(-0.0084T degrees C); (2) dioxin/furan production occurs at the combustion catalyst; (3) small variations in temperature cause large changes in the congener distribution of the dioxin and furan isomers; (4) molar TEQ yields from the parent compounds fed to the oxidizers are very small (10(-9)-10(-13)); (5) catalytic and thermal oxidizers may destroy dioxins fed from the ambient air; and (6) the oxidation of chlorinated VOCs with non-chlorinated VOCs reduces emissions of dioxins, likely due to the consumption of Cl in producing HCl. Laboratory investigations are needed to understand how dioxins are formed (and emitted) under conditions of this study.

摘要

在对百万分之几至几百万分之几浓度的氯化和非氯化挥发性有机化合物(VOCs)进行氧化的57次现场测试中,发现了多氯二苯并对二恶英和二苯并呋喃(二恶英)的排放。氧化过程发生在装有铂、铂/钯或氧化铬(IV)燃烧催化剂的催化氧化器中,或热氧化器(无催化剂)中。催化剂入口温度范围为293至573摄氏度。热氧化器的操作温度(火焰后)为773至927摄氏度。报告了有毒二恶英和呋喃异构体的数据,并进行加权,以2,3,7,8-四氯二苯并对二恶英的国际毒性当量(TEQ)表示。最大烟囱排放为1.07 ng/m3 TEQ,出现在293摄氏度时。该现场研究的显著结果如下:(1)烟囱中的TEQ水平随操作温度的降低呈指数增加,经验方程为TEQ(ng/dscm)=8.4 exp(-0.0084T摄氏度);(2)二恶英/呋喃的产生发生在燃烧催化剂处;(3)温度的微小变化会导致二恶英和呋喃异构体的同系物分布发生很大变化;(4)供给氧化器的母体化合物的摩尔TEQ产率非常小(10^-9至10^-13);(5)催化氧化器和热氧化器可能会破坏从周围空气中进入的二恶英;(6)氯化VOCs与非氯化VOCs的氧化减少了二恶英的排放,这可能是由于在生成HCl的过程中消耗了Cl。需要进行实验室研究,以了解在本研究条件下二恶英是如何形成(和排放)的。

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