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采用单相活性污泥法对焦化废水进行了试验研究。研究结果表明:当进水NH_3—N浓度为300mg/L左右,COD为1200~1500mg/L,酚浓度为100~380mg/L,CN~-为10~30mg/L,在系统总水力停留时间为27h和混合液回流比为400%的条件下,出水各项污染指标均达到国家排放标准。 相似文献
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焦化废水生物处理技术研究 总被引:5,自引:0,他引:5
采用PACT—硝化—-反硝化工艺,处理焦化废水。结果表明,排放水的COD可降至100 mg/l、NH_3-N浓度可达15mg/l,基本达到排放标准。该工艺适合于现有焦化厂废水处理设备的改造。 相似文献
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针对某企业焦炉烟气,新建一套脱硫脱硝除尘装置,焦炉烟气经过处理后,烟气中颗粒物、二氧化硫、氮氧化物以排放浓度满足《炼焦化学工业污染物排放标准》(GB16171-2012)大气污染物排放限值的要求。即:SO2排放浓度小于50mg/Nm^3,NOx排放浓度小于500mg/Nm^3,同时要求处理后烟气中颗粒物排放浓度小于30mg/Nm^3,氨含量排放浓度小于8ppm。 相似文献
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提高焦化废水生化处理效果途径 总被引:11,自引:0,他引:11
结合国内外文献,对焦化废水中有害物质的去除问题进行了综合分析,从而提出了3种提高焦化废水生化处理效果的有效技术,1.延时曝气;2.AS-PACT;3.强化处理。 相似文献
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蒋蔚琪 《石油化工环境保护》2006,29(1):12-14
在对比冷切焦水处理工艺的三种流程基础上,总结冷焦水密闭处理流程的优越性,对冷切焦水处理流程进行了一定程度的探讨。 相似文献
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Waste plastics recycling process using coke ovens 总被引:3,自引:0,他引:3
Kenji?KatoEmail author Seiji?Nomura Hiroshi?Uematsu 《Journal of Material Cycles and Waste Management》2003,5(2):98-101
The Japan Iron and Steel Federation (JISF), as its voluntary energy-saving action plan, proposed a 10% energy reduction by 2010 with 1990 as the basis. Further, it has suggested an additional 1.5% energy saving by the use of waste plastics as a metallurgical raw material. The amount of processing of waste plastics which corresponds to this amount of energy conversion is about 1 million t scale during 1 year. Conventional known methods for recycle-processing of waste plastics include, for example, the method of injection into a blast furnace to use waste plastics as an iron-ore reducing agent instead of coal. On the other hand, the coking process is considered to be suitable as a waste plastic recycling facility because the process involves coal carbonization in a high-temperature and reducing atmosphere. Carbonization tests with mixed waste plastics were conducted with laboratory equipment and in actual coke ovens. As a result, it was confirmed that the waste plastics recycling process using coke ovens is feasible. Therefore, a waste plastics recycling process using coke ovens was started as a chemical recycling technology at Nippon Steel. 相似文献
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氧化塘深度处理焦化废水的初步研究 总被引:10,自引:0,他引:10
焦化废水经过常规的二级处理后,COD和NH3-N往往难到达到国家排放标准,以活性污泥法处理焦化废水的出水水质为依据,采用氧化塘深度处理焦化废水,其COD和NH3-N均可达到国家排放标准。因此,只要只要条件控制得当,运用氧化塘处理低浓度焦化废水可以获得较好处理效果。 相似文献