共查询到20条相似文献,搜索用时 45 毫秒
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建立了烧结烟气中SO3的检测技术,包括SO3的采集装置和测定方法。实验结果表明:质量分数为80%的异丙醇适宜作为吸收液,方法的回收率为95.79%~102.80%,相对标准偏差为0.46%~1.38%。该技术能有效消除烟气中粉尘及SO2对测定的干扰,具有准确、可靠、方便等特点,可应用于烧结烟气脱硫等装置日常运行中SO3含量的测定。 相似文献
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研究表明,燃料燃烧过程中不同的SO2/SO3转化率对选择性催化还原( Selective Catalytic Reduction,SCR)烟气脱硝的最低运行温度影响大,温度变化幅度为10~15℃。对燃烧高硫煤锅炉的SCR烟气脱硝,应控制更低的SO2/SO3转化率;对燃烧低硫煤锅炉的SCR烟气脱硝,通过适当提高SO2/SO3转化率,最大催化剂用量可减少一半、烟气阻力降低一半,可大幅降低SCR烟气脱硝建设成本和运行成本。 相似文献
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SO3烟气调质系统在华润登封电厂的应用 总被引:2,自引:0,他引:2
采用SO3烟气调质的方法对华润登封电厂2号炉电除尘器进行提效改造。介绍了SO3烟气调质系统的工作原理、工艺流程、改造实施过程及改造前后的效果对比.对该技术的推广应用具有借鉴意义。 相似文献
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为了快速准确测定可再生湿法烟气脱硫过程有机胺吸收液中的p(SO2-4),建立了以茜素红为指示剂,用BaCl2直接滴定测定有机胺吸收液中p(SO2-4)的方法.实验结果表明:当试样pH为4.0 ~4.5时,方法的相对误差为0.28%-0.62%,加标回收率均在97%以上;SO2-3的存在会使p(SO2-4)的测定结果偏大... 相似文献
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James J. Cudahy 《Waste management (New York, N.Y.)》1998,18(6-8)
In the early 1980s, the Environmental Protection Agency (EPA) funded research on destruction and removal efficiencies (DREs) at eight hazardous waste incinerators. This research appeared to show that DREs of 99.99% could not be achieved at low waste feed principal hazardous organic constituent (POHC) concentrations. During the mid 1980s and 1990s however, testing at Superfund sites has indicated that DREs of 99.9999% or greater can be achieved at low waste feed POHC concentrations. This paper will summarize testing which includes 32 test runs at five Superfund sites and the EPA's incineration research facility. The tests include POHC concentrations from 6552 parts per million down to 28 parts per million at typical DREs of 6–9 s or greater. 相似文献
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电除尘器除尘效率影响因素及应对措施 总被引:1,自引:0,他引:1
对影响电除尘器除尘效率的诸多因素作了介绍,分析了影响除尘效率的原因,并在此基础上介绍了应对措施。讨论了今后提高电除尘器除尘效率的研究方向。 相似文献
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水平潜流人工湿地脱氮性能研究 总被引:1,自引:0,他引:1
试验研究了植物、季节变化对水平潜流人工湿地脱氮性能的影响及湿地去除污染物的沿程趋势.结果表明,潜流湿地脱氮、降解有机物性能与植物生长、季节变化密切相关,相关程度为脱氮大于降解有机物.潜流湿地降解有机物的主要场所位于湿地前、中部.湿地对COD的去除率在46.43%~90.85%间变化.潜流湿地对有机物降解、硝化与反硝化反应具有沿程同步性.种植芦苇的潜流人工湿地的TN去除率可以达到94.57%,芦苇湿地的脱氮性能明显好于空白湿地.潜流人工湿地具有良好的降解有机物和脱氮性能. 相似文献
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An experimental study of the behavior of endocrine-disrupting chemicals (EDCs) in leachate treatment processes (aeration, coagulation and sedimentation, activated carbon adsorption, and advanced oxidation) was conducted and removal efficiencies were evaluated. Among target EDCs, concentrations of BPA (1800 times), DBP (10 times), BBP (40 times), and DEHP (30 times) in leachate are more than ten times higher than those in surface water. BPA, DBP, and BBP can be treated by aeration and DEHP, by advanced oxidation processes. BPA could not be effectively removed by coagulation and sedimentation because most of BPA partitioned in the supernatant. DEHP could hardly be treated by aeration. The removal ratios of DEHP were approximately 50–70% if the generated sediment was removed completely. The removal ratios of DEHP in leachate of 100 m3/d with 100 kg of activated carbon were 50–70%, assuming a complete mixing model. The concentration of DEHP was decreased to below one-tenth in 120 min by advanced oxidation processes. 相似文献
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燃煤电厂电除尘器增效改造的途径 总被引:2,自引:1,他引:1
根据国家烟尘排放控制标准要求和我国目前的除尘设备状况,提出几种对火电厂原有电除尘器进行增效改造的途径,从理论上和技术上作出了比较详细的探讨。 相似文献
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G. Yuan D. Chen L. Yin Z. Wang L. Zhao J.Y. Wang 《Waste management (New York, N.Y.)》2014,34(6):1045-1050
In this research a gas–liquid fluidized bed reactor was developed for removing chlorine (Cl) from polyvinyl chloride (PVC) to favor its pyrolysis treatment. In order to efficiently remove Cl within a limited time before extensive generation of hydrocarbon products, the gas–liquid fluidized bed reactor was running at 280–320 °C, where hot N2 was used as fluidizing gas to fluidize the molten polymer, letting the molten polymer contact well with N2 to release Cl in form of HCl. Experimental results showed that dechlorination efficiency is mainly temperature dependent and 300 °C is a proper reaction temperature for efficient dechlorination within a limited time duration and for prevention of extensive pyrolysis; under this temperature 99.5% of Cl removal efficiency can be obtained within reaction time around 1 min after melting is completed as the flow rate of N2 gas was set around 0.47–0.85 Nm3 kg?1 for the molten PVC. Larger N2 flow rate and additives in PVC would enhance HCl release but did not change the final dechlorination efficiency; and excessive N2 flow rate should be avoided for prevention of polymer entrainment. HCl is emitted from PVC granules or scraps at the mean time they started to melt and the melting stage should be taken into consideration when design the gas–liquid fluidized bed reactor for dechlorination. 相似文献
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A pilot biotrickling filter (BTF) packed with ZX02 fibrous balls as packing material was tested for the treatment of ammonia (NH3) released from a composting plant of dairy manure. In order to investigate the effects of three compost aeration modes (mode Co-I, Co-II and In-II) on the NH3 removal efficiency, a field experiment was continuously carried out for more than eight months. The results demonstrated that under the intermittent aeration mode (In-II), the NH3 removal efficiency reached 99.2 ± 0.1% when the inlet NH3 concentration was 7.5-32.3 mg m−3 (9.8-42.5 ppmv). The maximum and critical elimination capacity of the biotrickling filter was 22.6 and 4.9 g NH3 m−3 h−1, respectively. The effluent concentration of NH3 was lower than 1.0 mg m−3, which meets the first class discharge standards of GB14554-93. When the concentration of free ammonia in the trickling liquid was varied from 0.1 to 0.4 mg L−1, the nitrification yield was between 47.9% and 103.8%. In addition, the optimum liquid tricking velocity (LTV) of the biotrickling filter was 0.5 m3 m−2 h−1 for low inlet concentrations and 2.2 m3 m−2 h−1 for high inlet concentrations. Therefore, the use of the biotrickling filter for the compost under the third aeration mode (In-II) yielded an effective optimum NH3 removal and reduced the nitrogen loss in the compost. 相似文献
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C. G. Whitworth S. Babko-Malyi D. M. Battleson S. J. Olstad 《Waste management (New York, N.Y.)》1998,18(6-8)
The United States Department of Energy (DOE) sponsored a series pilot-scale plasma incineration tests of simulated mixed wastes at the MSE Technology Applications, Inc. technology development test facility in Butte, MT. One of the objectives of the test series was to assess the ability of an electrically heated afterburner to destroy organic compounds that may be present in the off-gases resulting from plasma incineration of mixed wastes. The anticipated benefit of an electrically heated afterburner was to decrease total off-gas volume by 50% or more, relative to fossil fuel-fired afterburners. For the present test series, feeds of interest to the DOE Mixed Waste Focus Area (MWFA) were processed in a plasma centrifugal furnace while metering selected organic compounds upstream of the electrically heated afterburner. The plasma furnace was equipped with a transferred-mode torch and was operated under oxidizing conditions (10–15% oxygen at the stack). Feeds consisted of various mixtures of soil, plastics, Portland cement, silicate fines, diesel fuel, and scrap metals. Benzene, chloroform, and 1,1,1-trichloroethane were selected for injection as simulates of organics likely to be present in DOE mixed wastes, and because of their relative rankings on the US Environmental Protection Agency (EPA) thermal stability index. The organic compounds were injected into the off-gas system at a nominal concentration of 2000 ppmv. The afterburner outlet gas stream was periodically sampled, and analyzed by gas chromatography/mass spectrometry. For the electrically heated afterburner, at operating temperatures of 1800–1980°F (982–1082°C), organic compound destruction and removal efficiencies (DREs) for benzene, chloroform, and 1,1,1-trichloroethane were found to be >99.99%. The electrically heated afterburner was also operated at temperatures well below the design operating temperature, in order to assess the sensitivity of the afterburner to temperature swings. At 1300–1320°F (704–716°C) DREs for benzene and 1,1,1-trichloroethane were still >99.99%, while the DRE for chloroform was slightly degraded to 99.977%. At 820–850°F (438–454°C) the DRE for 1,1,1-trichloroethane remained >99.99%, while the DREs for benzene and chloroform were substantially degraded, in the order expected from the EPA thermal stability index. For comparison, analogous tests were performed using a conventional natural gas fired afterburner, with similar results. The natural gas fired afterburner yielded DREs greater than 99.99% for 1,1,1-trichloroethane, chloroform, and benzene, when operated at 1600–1820°F (871–993°C) and 1350°F (732°C). Similarly to the electrically heated afterburner, at 850°F (454°C) DREs were substantially degraded for chloroform and benzene. At normal operating temperatures both the electrically heated afterburner and the natural gas fired afterburner gave acceptable DREs (>99.99%), for the three injected organic compounds. DREs remained acceptable for both units even when operated at substantially reduced temperatures. 相似文献