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Effects of Fly Ash Transition Metal Content and Flue Gas HCl/SO_2 Ratio on Mercury Speciation in Waste Combustion

机译:粉煤灰过渡金属含量和烟气中HCl / SO_2的比例对废物燃烧中汞形态的影响

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Understanding the transformation of mercury species (elemental and oxidized forms) in stationary combustion sources is of interest to both those responsible for developing control technologies and those responsible for setting regulations. Elemental mercury (Hg~0) poses a challenging flue gas control issue, and oxidized forms of mercury (Hg~(2+)) are of concern due to local deposition potential. In a previous study, mercury speciation, or more specifically oxidation of Hg~0, was studied in simulated flue gases and in the presence of three-component model fly ashes. Gas-phase studies indicated that oxidation of Hg~0 in the presence of hydrogen chloride (HCl) is rather slow, and proceeds at measurable rates only at temperatures > 700℃ and HCl concentrations in the range of 100-200 ppm. The effect of fly ash composition was investigated using a fixed-bed reactor containing different synthetic model fly ash components such as alumina (Al_2O_3), silica (SiO_2), ferric oxide (Fe_2O_3), copper oxide (CuO), and calcium oxide (CaO). Transition metal oxides, CuO and Fe_2O_3, exhibited significant catalytic activity in the surface-mediated oxidation of Hg~0 in the presence of HCl. The observed Hg~0 oxidation activities of the two oxides are possibly caused by the Deacon process in which chlorine gas (Cl_2) is produced via catalytic oxidation of HCl over these two oxides. In the present follow-up study, the effect of sulfur dioxide (SO_2) to HCl ratio on Hg~0 oxidation was investigated. The addition of SO_2 to the moist flue gas at high SO_2:HCl ratios (10:1 to 4:1) caused a decrease in oxidation of Hg~0. This is attributed to a scavenging effect of SO_2 and H_2O on Cl_2. Addition of CaO to the synthetic fly ashes also caused a drop in Hg~0 oxidation. It is possible that due to the partial removal of HCl by reaction with CaO less HCl is available for the catalytic Deacon reaction. The Hg~0 oxidation activity of a cement kiln dust (CKD) sample collected from a full-scale hazardous waste incinerator was also studied. Qualitatively, it exhibited Hg~0 oxidation catalytic behavior similar to that observed with CaO-containing model fly ashes. According to this study, only moderate oxidation of Hg~0 (40%) can be expected in cement kilns burning hazardous waste. During hazardous and municipal waste combustion, the presence of sufficiently high HCl and/or Cl_2 in the gas phase may cause the metallic oxide compounds in the fly ash to be converted into metal chlorides. Additional tests were performed using synthetic fly ashes containing cuprous chloride (CuCl). These results were compared to those obtained using CuO. It was found that CuCl is so reactive that it oxidizes Hg~0 even in the absence of HCl in the simulated flue gas. This is contrary to the behavior shown by CuO, which requires the presence of HCl in the flue gas in order for Hg~0 oxidation to occur.
机译:负责开发控制技术的人员和负责制定法规的人员都对了解固定燃烧源中汞物质(元素和氧化形式)的转化很感兴趣。元素汞(Hg〜0)构成了一个挑战性的烟道气控制问题,由于局部沉积潜力,汞的氧化形式(Hg〜(2+))受到关注。在先前的研究中,在模拟烟道气中和存在三组分模型粉煤灰的情况下,研究了汞形态,或更具体地说是Hg〜0的氧化。气相研究表明,在氯化氢(HCl)存在下Hg〜0的氧化相当缓慢,并且只有在温度> 700℃和HCl浓度在100-200 ppm范围内时,Hg〜0的氧化速率才可测量。使用固定床反应器研究粉煤灰组成的影响,该反应器包含不同的合成模型粉煤灰组分,例如氧化铝(Al_2O_3),二氧化硅(SiO_2),三氧化二铁(Fe_2O_3),氧化铜(CuO)和氧化钙(CaO )。过渡金属氧化物CuO和Fe_2O_3在HCl存在下Hg〜0的表面介导氧化中表现出显着的催化活性。观察到的两种氧化物的Hg〜0氧化活性可能是由迪肯工艺引起的,在该工艺中,通过HCl在这两种氧化物上的催化氧化生成氯气(Cl_2)。在目前的后续研究中,研究了二氧化硫(SO_2)与HCl的比例对Hg〜0氧化的影响。以高SO_2:HCl比(10:1至4:1)向湿烟道气中添加SO_2导致Hg〜0的氧化减少。这归因于SO_2和H_2O对Cl_2的清除作用。在合成粉煤灰中添加CaO也会导致Hg〜0氧化下降。由于与CaO反应可部分除去HCl,因此催化迪肯反应的HCl较少。还研究了从大型危险废物焚化炉收集的水泥窑粉尘(CKD)样品的Hg〜0氧化活性。定性地,它表现出的Hg〜0氧化催化行为与含CaO的模型飞灰相似。根据这项研究,在燃烧危险废物的水泥窑中,仅预期Hg〜0的中等氧化(40%)。在危险的市政废物燃烧过程中,气相中存在足够高的HCl和/或Cl_2可能导致粉煤灰中的金属氧化物化合物转化为金属氯​​化物。使用含有氯化亚铜(CuCl)的合成粉煤灰进行了其他测试。将这些结果与使用CuO获得的结果进行比较。结果发现,即使在模拟烟道气中不存在HCl的情况下,CuCl的反应性也很强,它会氧化Hg〜0。这与CuO所示的行为相反,后者需要在烟道气中存在HCl才能发生Hg〜0氧化。

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