镁盐复合混凝剂应用于活性染料印染废水脱色的实验研究

采用镁盐与亚铁盐混合复配对活性染料印染废水进行脱色处理.考察该复合混凝剂的组分配比、pH值和投加量对脱色率的影响,并与单一组分混凝剂的脱色效果作对比,同时初步分析了复合混凝剂的脱色机理.结果表明:复合混凝剂MgSO4-FeSO4·7H2O的脱色效果明显优于单一组分,表现出显著的协同效应;对于80 mg/L的活性黑KN-B印染废水(色度为1000倍),在复合混凝剂投加量为556 mg/L、pH值在10.9左右时,脱色率可以达到99.07%;主要脱色机理表现为镁盐和亚铁盐在高pH值的环境下共沉淀生成氢氧化物絮状物吸附溶液中的染料分子一起沉降.该吸附主要为电中和吸附.吸附等温线符合Langmuir方程,复合吸附剂的饱和吸附量达1.1614 g/g.     

Mercury contamination in vicinity of secondary copper smelters in Fuyang, Zhejiang Province, China: Levels and contamination in topsoils

In the present study, we aim to investigate the extent of soil contamination by Hg, particularly by anthropogenic Hg, and tentatively estimate the total Hg (Hg_T) accumulation in topsoils (0-15 cm) in Fuyang, Zhejiang Province—a secondary Cu smelter of China. The results show that the levels of soil Hg in the vicinity of the smelters have been substantially elevated following local smelting activities. The spatial distribution of soil Hg in this area reveals a rapid decrease as the distance from the smelter reaches 1.5 km, which is probably due to the quick deposition process of particulate Hg and reactive gaseous Hg emitted from the smelters. The total accumulation of Hg_T in the topsoils of the study area of 10.9 km² is approximately 365-561 kg and of which 346-543 kg might be contributed by anthropogenic emission alone with an annual emission of 17.3-27.2 kg Hg to the topsoils.     

Comparison of manual and automated chambers for field measurements of N2O,CH4, CO2 fluxes from cultivated land

Chamber techniques can easily be applied to field trials with multiple small plots measuring carbon- and nitrogen-trace gas fluxes. Nevertheless, such chamber measurements are usually made weekly and rarely more frequently than once daily. However, automatic chambers do allow flux measurements on sub-daily time scales. It has been hypothesized that sub-daily measurements provide more reliable results, as diurnal variations are captured better compared to manual measurements. To test this hypothesis we compared automatic and manual measurements of N₂O, CO₂ and CH₄ fluxes from tilled and non-tilled plots of a rice–wheat rotation ecosystem over a non-waterlogged period. Our results suggest that both techniques, i.e., either manual or automatic chambers of N₂O and CO₂ emissions resulted in biased fluxes. The manual measurements were adequate to capture either day-to-day or seasonal dynamics of N₂O, CO₂ and CH₄ exchanges, but overestimated the cumulative N₂O and CO₂ emissions by 18% and 31%, respectively. This was due to neglecting temperature-dependent diurnal variations of C and N trace gas fluxes. However, the automatic measurements underestimated the cumulative emissions of N₂O and CO₂ by 22% and 17%, respectively. This underestimation resulted from chamber effects upon soil moisture during rainfall processes. No significant difference was detected between the two methods in CH₄ exchanges over the non-waterlogged soils. The bias of manual chambers may be significant when pronounced diurnal variations occur. The bias of automatic measurements can only be avoided/minimized if chamber positions are frequently changed and/or if chambers are automatically opened during rainfall events. We therefore recommend using automatic chambers together with continuous measurements of soil chamber moisture to allow for soil moisture correction of fluxes or to correct flux estimates as derived by manual chambers for possible diurnal variations.     

铝塑包装废物热解过程能量平衡分析

热解是实现铝塑包装废物中有机物和金属铝分离的有效方法。利用外热式固定床反应系统对其进行热解实验,研究热解时物质与能量流向的变化趋势。结果表明:(1)铝塑包装废物最佳热解温度为723～773 K;(2)热解产生的可回收能量远大于反应所需能量,可以实现热解系统的自供热;(3)铝塑包装废物热解的净能源回收效率为62%～63%。     

一株脱硫菌的分离及脱硫动力学

从污水处理厂二沉池分离获得一株硫酸盐还原菌厌氧菌株,依据生理生化分析和16S rDNA基因序列测定该菌株被鉴定为脱硫脱硫弧菌(Desulfovibrio desulfuricans)。在气体吸收的双膜理论和液相中微生物转化的米门方程基础上,建立了搅拌式生物吸收反应器中脱硫脱硫弧菌净化二氧化硫气体的动力学模型,并求解出相应的动力学参数基质转化最大速度Vmax和米氏常数Km,实验结果所得到的线性方程相关性较好,线性相关系数可以达到0.998,而且脱硫脱硫弧菌吸收液具有较高转化二氧化硫的能力。     

La2O3/ZnO/TiO2光催化降解活性艳红K-2BP的研究

采用溶胶-凝胶法制备了La2O3/ZnO/TiO2复合光催化剂,以紫外灯为光源,活性艳红K-2BP为模型降解物,研究了La2O3/ZnO/TiO2的光催化性能。结果表明：当锌和镧的掺杂量w(ZnO)=20%, w(La2O3)=0.5%, 煅烧温度为500℃时,La2O3/ZnO/TiO2复合光催化剂的光催化活性最高;当催化剂投加量4 g/L,通气量800 mL/min,初始pH值3.12时,La2O3/ZnO/TiO2对活性艳红K-2BP的降解效果最好。实验证明,La2O3/ZnO/TiO2对活性艳红K-2BP的降解遵从Langmuir-Hinshelwood动力学模型,测得其反应速率常数k＝11.5 mg/(L·min);吸附常数K＝2.88×10-2 L/mg。     

沸腾炉大气污染物初始排放因子的研究

以20台沸腾炉(≤60MW)的燃料特性分析数据和大气污染物的排放实测数据为基础,研究了颗粒物(PM)、SO2和NOX初始排放因子EFP0M、EF0SO2、EF0NOX的变化规律,并利用SPSS13.0统计分析软件,分析了EFP0M、EFS0O2、EF0NOX与影响因子间的相关性。结果表明,在沸腾炉运行负荷≥80%的条件下,EF0PM基本不受锅炉出力(W)、燃煤灰分质量分数(Aar)及过量空气系数(α)的影响,EFP0M与W、Aar、α不具有相关性;EF0SO2主要受燃煤硫质量分数(Sar)的影响,两者具有显著正相关关系;W、α、燃煤干燥基挥发分质量分数(Vdaf)对EF0NOX具有显著影响,EF0NOX与α具有显著正相关关系,而EF0NOX与W、Vdaf具有显著负相关关系;EFS0O2和EF0NOX影响因子由强到弱的顺序为:①EFS0O2:SarαW;②EF0NOX:VdafαW燃煤氮质量分数(Nar)。     

燃油锅炉燃烧过程SO2的生成与排放特征

燃料燃烧过程是大气污染物的重要来源之一,对人体健康、空气质量和气候变化产生非常重要的影响。以62台燃油锅炉（≤10.5 MW）的燃料特性分析数据和SO₂排放实测数据为基础,通过统计分析方法,研究了燃油燃烧过程中燃油硫含量S和过量空气系数α对硫的转化率、SO₂排放因子和排放浓度的影响,获得了基于燃料消耗量、燃料发热量的SO₂排放因子EF_C、EF_H以及SO₂标态折算浓度C′_SO2与硫含量S间的关联式。结果表明,在过量空气系数α＞1的燃油燃烧过程中,EF_C、EF_H、C′_SO2与燃油硫含量S呈现出显著的线性正相关性,而与过量空气系数α无关,其关系式分别为：EF_C=18.86602×S,EF_H=443.78751×S ,C′_SO2＝1 509.28337×S;硫转化率η和基于燃料硫含量的SO₂排放因子EF_S则与燃油硫含量S和过量空气系数α无关,其平均值分别为96.3％和1.93 kg/kg。     

新型材料处理化学镀镍废水

采用一种同时具备吸附和离子交换功能的新型材料CARBONITE对低浓度化学镀镍废水进行实验研究,分别探讨了CARBONITE用量、pH值、温度和反应时间对CARBONITE去除废水中Ni2+的影响,并考察了CARBONITE的再生性能。实验结果表明,当CARBONITE投加量为1.5 g/L,pH值为6.8,温度为40℃,反应时间为6 h时,CARBONITE对Ni2+去除率可达最大值91.39%。用pH值为4的硫酸溶液对吸附后的CARBONITE进行再生实验,效果良好,再生3次之后的CARBONITE对Ni2+的去除率仍能达到82%左右。     

Fenton氧化-前置反硝化缺氧好氧池(A/O)处理荧光增白剂废水中试研究

采用Fenton氧化-前置反硝化缺氧好氧池(A/O)对荧光增白剂废水IC出水进行中试实验研究。实验表明,在Fe2+投加量为0.003 mol/L,进水pH值为3,[H2O2]/[Fe2+]为4∶1,反应时间为2 h的条件下,Fenton氧化法对COD的去除率可以达到46%以上,出水BOD5/COD的值由0.26提高到0.58。氧化后废水进入前置反硝化生物脱氮系统进行生化处理,该系统采用间歇式进水,水力停留时间为2 d,实验结果表明,A/O系统对COD、氨氮和总氮的去除率分别达41%、90%以上和86%。该组合工艺对COD的总去除率可达到67%,出水氨氮在20 mg/L以下,总氮在37 mg/L以下。