大气污染物综合排放标准的编制技术方法

我国《大气污染综合排放标准》规定了33种大气污染物的排放限值和执行要求。标准提出了一个污染源必须同时遵守最高允许排放浓度;最高允许排放速率和无组织排放监控浓度限值三项限制指标。以众多企业的排放数据和“最佳实用治理技术”为依据制定排放浓度限值;以环境质量要求和全国大部分地区的中性气象条件为依据,经计算后确定排放速率限值;以污染源周界环境空气浓度达到质量标准要求确定无组织排放限值。经过一定范围的调查检验后,表明该标准具有基本适宜的宽严程度。     

Pollutant emission characteristics of rice husk combustion in a vortexing fluidized bed incinerator

Rice husk with high volatile content was burned in a pilot scale vortexing fluidized bed incinerator. The fluidized bed incinerator was constructed of 6 mm stainless steel with 0.45 m in diameter and 5 m in height. The emission characteristics of CO, NO, and SO2 were studied. The effects of operating parameters, such as primary air flow rate, secondary air flow rate, and excess air ratio on the pollutant emissions were also investigated. The results show that a large proportion of combustion occurs at the bed surface and the freeboard zone. The SO2 concentration in the flue gas decreases with increasing excess air ratio, while the NOx concentration shows reverse trend. The flow rate of secondary air has a significant impact on the CO emission. For a fixed primary air flowrate, CO emission decreases with the secondary air flowrate. For a fixed excess air ratio, CO emission decreases with the ratio of secondary to primary air flow. The minimum CO emission of 72 ppm is attained at the operating condition of 40% excess air ratio and 0.6 partition air ratio. The NOx and SO2 concentrations in the flue gas at this condition are 159 and 36 ppm, which conform to the EPA regulation of Taiwan.     

Emissions of SO2, NO and N2O in a circulating fluidized bed combustor during co-firing coal and biomass

This paper presents the experimental investigations of the emissions of SO2, NO and N2O in a bench scale circulating fluidized bed combustor for coal combustion and co-firing coal and biomass. The thermal capacity of the combustor is 30 kW. The setup is electrically heated during startup. The influence of the excess air, the degree of the air staging, the biomass share and the feeding position of the fuels on the emissions of SO2, NO and N2O were studied. The results showed that an increase in the biomass shares resulted in an increase of the CO concentration in the flue gas, probably due to the high volatile content of the biomass. In co-firing, the emission of SO2 increased with increasing biomass share slightly, however, non-linear increase relationship between SO2 emission and fuel sulfur content was observed. Air staging significantly decreased the NO emission without raising the SO2 level. Although the change of the fuel feeding position from riser to downer resulted in a decrease in the NO emission level, no obvious change was observed for the SO2 level. Taking the coal feeding position R as a reference, the relative NO emission could significantly decrease during co-firing coal and biomass when feeding fuel at position D and keeping the first stage stoichiometry greater than 0.95. The possible mechanisms of the sulfur and nitrogen chemistry at these conditions were discussed and the ways of simultaneous reduction of SO2, NO and N2O were proposed.     

羟基乙叉二膦酸镀铜废液的处理及Cu~(2+)的高附加值资源化回收

采用Na BH4还原法将羟基乙叉二膦酸(HEDP)镀铜废液中的Cu~(2+)制备成纳米铜粉,并采用聚丙烯酰胺(PAM)对还原反应后的废液进行絮凝处理。研究了n(Cu~(2+))∶n(Na BH4)、还原反应温度、还原反应时间及PAM添加量对废液中剩余Cu~(2+)质量浓度的影响,并对回收的纳米铜粉进行了XRD和TEM表征。实验结果表明:当n(Cu~(2+))∶n(Na BH4)=4∶6、还原反应温度为50℃、还原反应时间为2 h时,废液中剩余Cu~(2+)质量浓度降低至1.1 mg/L,Cu~(2+)还原率达99.99%;可获得粒径为20~45 nm的近球型、高纯度、由多晶组成的纳米铜粉;当PAM添加量为10 mg/L时,废液中剩余Cu~(2+)质量浓度降至0.35 mg/L以下,达到GB 21900—2008《电镀污染物排放标准》(小于0.5 mg/L)的要求。     

Mg3MnxAl1-xCO3类水滑石衍生NSR催化剂的制备及其性能评价

采用共沉淀法合成了三元类水滑石Mg_3Mn_xAl_(1-x)CO_3,通过高温煅烧得到其衍生氧化物Mg_3Mn_xAl_(1-x)O_m,再经浸渍负载Pt或BaO后制得新型NO_x存储/再还原(NSR)催化剂。XRD及SEM表征结果显示,当Mn与Al的摩尔比(Mn/Al)大于1时所制备的Mg_3Mn_xAl_(1-x)O_m有杂晶相出现且发生团聚,结合NO_x存储性能评价结果,确定最优Mn/Al为1。BaO负载不利于NO_x的存储,而当Pt负载量为1%(w)时NO_x存储性能最优,250℃条件下的存储量由负载前的0.52 mmol/g提升至0.61 mmol/g。CO_2与NO_x之间存在较强的竞争吸附。负载1%Pt催化剂的NSR性能评价结果表明,8个稀燃-富燃循环后NO_x的去除率为68%,表明催化剂的还原性能仍需加强。     

深圳大运会期间大气中多环芳烃的特征及消减情况研究

深圳大运会期间,利用大流量主动采样器对深圳市5个点位进行大气样品采集,检测其气相及颗粒相中总的多环芳烃(PAHs)浓度以及与2010年夏季的监测数据进行比较,研究PAHs通过各种空气质量保障措施实施后的消减情况.结果表明,大运期间5个点位∑PAHs变化范围为15.80~62.09ng/m3,平均值30.77ng/m3,与2010年夏季相比,PAHs平均消减28%;大运期间PAHs单体中均以3~4环为主,平均占总浓度的88%;通过特征分子比值法推断大运期间机动车尾气排放是PAHs的主要来源,但是柴油车尾气排放和燃煤电厂废气排放的贡献比率增加;大运期间∑BaPeq比2010年夏季降低36%,BaP浓度以及∑BaPeq浓度都低于我国环境空气中对BaP的限值标准;呼吸致癌风险评价表明,大运期间为每百万人致癌3.8例,2010年夏季为每百万人致癌7.3例,致癌风险下降48%.     

以化学抑制法研究污水生物处理过程中N2O的释放源

采用化学抑制法,研究了不同曝气量下污水生物处理过程中N2O的释放源.结果表明,缺氧段中, N2O的主要释放源为硝酸盐异化成氨反应,而反硝化反应消耗N2O.好氧段中N2O释放源受曝气量的影响很大,当曝气量适中时(65L/h), N2O释放源主要为硝化细菌反硝化作用;而当曝气量偏高(105L/h)或偏低(25L/h)时,同步硝化-反硝化反应是主要的N2O释放源.同时硝化细菌反硝化反应也能够产生少量N2O.     

青藏高原阶段性隆升对亚洲干旱半干旱区冬季粉尘循环的影响

粉尘是大气气溶胶的主要成分之一,对大气能量平衡起着关键作用。一般来讲,黄土高原（LP）粉尘主要来源于北方沙漠区,但有关中国东部及其周边地区粉尘来源的争论仍在继续。为此,本文对比分析了亚洲主要粉尘源区如中亚（CA）和中蒙（CM）粉尘循环对青藏高原阶段性隆升的响应,探讨了CA和CM粉尘排放对下游的贡献。利用美国大气研究中心（NCAR）最新发布的通用地球系统模式（CESM 1.0）,进行了改变青藏高原海拔高度为现在10%,20%,30%?…100%的9个数值试验。分析结果表明,随着青藏高原阶段性隆升中亚和中蒙干旱区冬季降水均线性减弱,与前人研究结果一致。青藏高原阶段性隆升阻塞西风环流使其减弱从而引起中亚粉尘释放减弱;而青藏高原阶段性隆升引起亚洲冬季风加强,促使中蒙粉尘释放加强,与中亚相反。模拟结果与地质记录对比进一步证实了中蒙粉尘源区对黄土高原、中国东部及临近区域粉尘沉降的贡献。     

加卸荷条件下岩石力学特性与声发射特征

为了探究真三轴复杂应力变化条件下岩石强度及破坏模式,通过真三轴卸荷扰动测试系统对砂岩试件进行不同第二主应力加卸荷试验,讨论在加卸荷过程中岩石的力学特性及声发射特征。试验结果表明:第二主应力的增加对试件的承载能力起到先增强后弱化的效果;不同第二主应力加卸荷声发射能量及累计振铃计数变化趋势大体一致,耗散能量比在载荷达到岩石损伤强度时突增;声发射能量峰值提前于试件轴向应力跌落,声发射能量和累计振铃计数大幅突增可作为岩石破坏的前兆;在低载荷下岩石中活动主要是裂隙压密与发育,在达到岩石损伤强度后岩石中的活动主要是裂纹贯通形成破裂面,砂岩试件声发射定位点集中区域与试件主要破裂面基本吻合。     

磁化荷电水雾最佳降尘参数确定实验研究*

为实现对煤尘的有效防控,进一步提高磁化水降尘性能,提出磁化荷电喷雾降尘技术,通过研究液滴在磁化、荷电情况下的受力,揭示磁化荷电喷雾降尘机理;通过自主搭建的动、静态综合除尘实验平台,研究不同磁化强度、荷电电压下溶液表面张力和雾滴粒径的变化规律,进而确定最佳雾化参数。研究结果表明:磁化荷电后的溶液表面张力和雾滴粒径随磁化强度、荷电电压的增大呈现先下降而后上升,最后趋于平稳。荷电电压为9 kV、磁化强度为350 mT时达到最佳效果,此时,与清水相比全尘降尘效率达到92.79%、提高69.63%,呼尘降尘效率达到78.59%、提高94.01%。磁化荷电的溶液表面张力降低,破碎时所做表面功更小,雾化后液滴粒径更小更均匀,与尘粒接触面积增大,可提高捕尘效率,改善矿井环境。