Long Term Trends in Sulphur and Nitrogen Deposition in Europe and the Cause of Non-linearities

Emissions of sulphur and oxidized nitrogen compounds in Europe have been reduced following a series of control measures during the last two decades. These changes have taken place during a period in which the primary gases and the wet deposition throughout Europe were extensively monitored. Since the end of the 1970s, for example land based sulphur emissions declined by between 90 and 70% depending on the region. Over the same period the total deposition of sulphur and its partitioning into wet and dry deposition have declined, but the spatial pattern in the reduction in deposition differs from that of emission and has changed with time. Such non-linearities in the emission-deposition relationship are important to understand as they complicate the process of assessing the effects of emission reduction strategies. Observed non-linearities in terrestrial sulphur emission-deposition patterns have been identified in north west Europe due to increases in marine emissions, and are currently slowing the recovery of freshwater ecosystems. Changes in the relative amounts of SO₂ and NH₃ in air over the last two decades have also changed the affinity of terrestrial surfaces for SO₂ and have therefore changed the deposition velocity of SO₂ over substantial areas. The consequence of this effect has been the very rapid reduction in ambient SO₂ concentration in some of the major source areas of Europe, where NH₃ did not change much. Interactions between the different pollutants, generating non-linearities are now being incorporated in long-range transport models to simulate the effects of historical emission trends and to provide projections into the future. This paper identifies non-linearities in emission deposition relationships for sulphur and nitrogen compounds in Europe using data from the EMEP long-rang transport model and measured concentration fields of the major ions in precipitation and of SO₂ and NO₂ in surface air.     

湿法FGD湿烟囱工艺的问题及对策

介绍了湿法FGD湿烟囱工艺的可行性和选择该工艺时应考虑的问题，并提出了湿烟道、湿烟囱设计的基本要求。     

缺失烟囱参数估算及其应用对空气质量模拟结果的改进

针对源清单中部分点源烟囱参数缺失而采用源排放模型SMOKE(Sparse Matrix Operator Kernel Emissions)默认的烟囱参数对空气质量模型模拟结果造成的不利影响,综合考虑气象观测数据、空气质量监测数据、源排放强度以及相关标准和规范对烟囱设计的要求,分别基于最大落地浓度法和基于统计方法对2009年珠三角地区源清单中缺失烟囱参数点源的烟囱参数进行了估算,并将估算烟囱参数用在WRF/SMOKE-PRD/CMAQ空气质量模型系统分析其对模型模拟的改善情况.相比于采用SMOKE默认烟囱参数,基于最大落地浓度估算烟囱参数对NO2、NOx、SO2、PM10及O3的模拟结果均具有一定改善作用,而基于统计方法估算烟囱参数仅对SO2、O3的模拟结果有所提高.结果表明,使用基于最大落地浓度法估算得到的烟囱参数更为合理,使污染物的垂直排放分配更加合理,可以应用于空气质量模型输入源清单中缺失烟囱参数点源的估算,从而一定程度上改善空气质量模型的模拟效果.     

PE微塑料对土壤水分入渗的影响及入渗模型适宜性评价

为探究微塑料对土壤水分入渗过程的影响,通过室内土柱模拟试验,设置5组微塑料添加处理(0,1,2,4,6g/kg),研究了不同微塑料含量对湿润锋运移和累积入渗量的影响,并进一步评价了主要入渗模型在微塑料污染土壤中的适用性.结果表明,湿润锋运移速率随着微塑料含量的增加呈现出先减小后增加的特征,当含量达到T2时(微塑料含量2...     

Preparation and characterization of Fe2O3-CeO2-TiO2/γ-Al2O3 catalyst for degradation dye wastewater

In order to develop a catalyst with high activity for catalytic wet oxidation (CWO) process at room temperature and atmospheric pressure, Fe2O3-CeO2-TiO2/γ-Al2O3 catalyst was prepared by consecutive impregnation method and the prepared parameters were optimized. The structure of the catalyst was characterized by BET, XRF, SEM and XPS technologies, and the actual wastewater was used to investigate the catalytic activity of Fe2O3-CeO2-TiO2/γ-Al2O3 in CWO process. The experimental results showed that the prepared catalyst exhibited good catalytic activity when the doping amount of Ti was 1.0 wt% (the weight ratio of Ti to carriers), and the middle product, CeO2-TiO2/γ-Al2O3, was calcined in 450℃ for 2 h. The CWO experiment for treating actual dye wastewater indicated that the COD, color and TOC of actual wastewater were decreased by 62.23%, 50.12% and 41.26% in 3 h,respectively, and the ratio of BOD5/COD was increased from 0.19 to 0.30.     

烟囱颗粒污染物连续监测技术

介绍了一种烟囱颗粒物排放的实时监测装置。该装置基于光散射理论 ,使用一个半导体激光器件作为光源 ,用 4个光电元件分别测定入射光强、从测量区出射的光强及前向两个立体角的散射光能 ,使用一台微机对接收信号进行处理 ,能够实时地给出烟囱排放源的排放浓度及粒径分布。     

太湖氮磷营养盐大气湿沉降特征及入湖贡献率

2009年8月—2010年7月在太湖流域不同区域10个采样点收集降水样品230多个,测定其中不同形态N,P营养盐的质量浓度,分析太湖大气湿沉降中N,P营养盐沉降特征,计算N,P营养盐湿沉降率及其占太湖河流入湖负荷的贡献率. 结果表明:湿沉降中ρ(TN)年均值为3.16 mg/L,DTN(溶解性总氮)占TN的70%以上,其中以NH₄+-N为主;湿沉降中ρ(TN)年均值最高值出现在南部湖区,最低值出现在北部湖区. 湿沉降中ρ(TP)年均值为0.08 mg/L,相对较低. 5个区域湿沉降中不同形态N的质量浓度均表现为冬季高、夏季低,而不同形态N,P的湿沉降量均为夏季最大. 南部、东部湖区TN的湿沉降率相对较大. 各采样点湿沉降中NH₄+-N沉降率约占DTN沉降率的30.4%～52.0%,NO₃--N沉降率约占DTN的31.6%;各区域间湿沉降中DTP(溶解性总磷)占TP的比例差异较大. 大气湿沉降中TN和TP的年沉降总量分别为10 868 和247 t,为同期河流入湖负荷的18.6%和11.9%,湿沉降对太湖富营养化的贡献及可能带来的水生态系统的影响不容忽视.      

滴流床催化湿式氧化苯酚的动力学

通过自行设计制作的滴流床反应器,研究了苯酚在以CuO/γ-Al₂O₃为催化剂的催化湿式氧化反应.结果表明,在相对温和的操作条件(温度180 ℃,压力3 MPa,液相流量1.668 L·h^-1,气相流量160 L·h^-1)下,苯酚的去除率均达到90%以上.苯酚的降解曲线与自催化反应的S型曲线类似,符合自由基链反应机理.所建立的活塞流拟均相反应器模型能很好地拟合苯酚催化湿式氧化反应过程.还研究了苯酚初始浓度、苯酚水溶液流量及反应温度对反应结果的影响.     

乳化液废水均相催化湿式氧化动力学

在2L高压间歇反应釜中,以高浓度难降解乳化废水为处理对象,研究了温度对铜盐均相湿式氧化的影响和动力学特征.结果表明:升高温度对加快后期反应速度更为有利,催化剂有利于中间产物氧化,在200℃催化活性最高,在进水COD48 400mg/L,反应2h去除率为86.6%;催化剂在不同温度作用下机制有所差别:200℃时3个途径反应速度均加快,中间产物加速氧化更明显;220～240℃时反应向生成中间产物方向偏移,活性降低;通用模型能较好地预测均相催化过程.     

催化湿式氧化处理造纸废水的研究

以过渡金属氧化物CuO为活性组分,采用催化湿式氧化法处理造纸废水,考察Cu负载量、催化剂用量、反应温度对废水COD去除率的影响。结果表明:固定氧气分压在2.5MPa和反应时间3h,催化剂用量为3g,Cu负载量为4%,反应温度为220℃,500mL浓度为3250mg/L造纸废水的COD去除率为90%,色度去除率为89%,pH值由9.6变为7.8。另外,对催化剂进行再生处理和稳定性测试。结果表明:450℃下活化3h,在上述相同反应条件下,对原废水的COD去除率降低为88%,重复使用9次后对废水的COD去除率仍能保持在85%左右。