催化氧化技术在橡胶废气处理中的应用  被引量:19

Application of Catalystic Oxidation Process in Treatment of Rubber Production Waste Gas

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作  者:程文红[1] 袁晓华[1] 田凤杰[1] 

机构地区:[1]中国石化北京燕山分公司,北京102500

出  处:《化工环保》2012年第2期156-159,共4页Environmental Protection of Chemical Industry

摘  要:采用催化氧化技术处理热塑性丁苯橡胶(SBS)生产装置D线后处理单元废气,废气的非甲烷总烃去除率和环己烷去除率均达到98%以上,非甲烷总烃质量浓度达到DB11/447—2007《炼油与石油化学工业大气污染物排放标准》的要求(小于100 mg/m3)。对SBS生产装置凝聚单元进行两釜流程改三釜流程后,催化氧化反应器入口非甲烷总烃质量浓度由(3.84~5.82)×103mg/m3降至(2.48~2.63)×103mg/m3,反应器出口非甲烷总烃质量浓度均小于50 mg/m3。凝聚单元改造并采用催化氧化技术处理废气后,每年节约费用约80万元。The waste gas from the post-treatment unit of D-line of the thermoplastic styrene-butadiene rubber(SBS) production plant was treated by catalytic oxidation process.The removal rates of non-methane hydrocarbons and cyclohexane in the waste gas are both over 98%,and the mass concentration of nonmethane hydrocarbons meets the emission standard DB11/447-2007 of air pollutants for petroleum refining industry(less than 100 mg/m3).After the two-reactor-process of the condensation unit of the SBS production plant was changed into the three-reactor-process,the mass concentration of non-methane hydrocarbons in the inlet of the catalytic oxidation reactor decreases from(3.84-5.82)×103mg/m3to(2.48-2.63)×103mg/m3,and that of non-methane hydrocarbons in the outlet is less than 50 mg/m3.With the process modification of the condensation unit and the waste gas treatment by catalytic oxidation process,about 800 000 yuan per year are saved.

关 键 词:挥发性有机物 热塑性丁苯橡胶 催化氧化 废气处理 

分 类 号:X701[环境科学与工程—环境工程]

 

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