硫化法制备废水处理用光催化剂La3NbS2O5

采用高温硫化法制备了具有可见光活性的La3 NbS2 O5光催化剂,运用X射线衍射谱图、扫描电子显微镜照片、比表面积和紫外-可见漫反射光谱对La3 NbS2 O5的结构、物理性质和光吸收性能进行了表征.以亚甲基蓝为目标降解物,考察了硫化温度、催化剂加入量和制备方法对亚甲基蓝降解率的影响.实验结果表明,当硫化温度为800...     

Effective cleanup of oil contamination on bio-inspired superhydrophobic surface

Environmental Science and Pollution Research - The oil-water separation is a popular issue and the removal of oil from bulk water is also meaningful especially in oil spill incident, which not only...     

Associations between ambient high temperatures and suicide mortality: a multi-city time-series study in China

Environmental Science and Pollution Research - Suicide prevention has become a public health issue of great concern. Previous studies proved that ambient temperature had an impact on suicide death,...     

Air pollution inequality and health inequality in China: An empirical study

Environmental Science and Pollution Research - China’s residents experience unequal exposure to air pollution in different regions, and the corresponding health consequences have increased...     

粉煤灰基层状金属氧化物对水中活性红X-3B的吸附

以粉煤灰(FA)为原料,采用共沉淀法制备了层状双金属氢氧化物(LDH)和层状金属氧化物(LMO,也称LDO),并采用XRD和BET技术进行了表征。比较了FA、LDH、LMO对活性红X-3B染料(X-3B)的吸附效果;考察了LMO吸附X-3B的影响因素,并探讨了吸附机理。XRD表征结果表明,LMO在吸附X-3B后重新恢复LDH层状结构。BET表征结果表明,LMO的比表面积大于LDH。吸附实验结果表明,3种吸附剂对X-3B吸附效果的优劣顺序为:LMOLDHFA;在初始X-3B质量浓度为50 mg/L、LMO投加量为2.0 g/L、吸附温度为25℃、吸附pH为7、吸附时间为30 min的条件下,X-3B去除率可达98.1%;LMO对X-3B的吸附符合Langmuir等温吸附方程,饱和吸附量为129.53 mg/g,且吸附过程可用准二级动力学方程描述。     

生物滴滤塔处理模拟甲硫醚废气

在常温条件下,采用生物滴滤塔处理模拟甲硫醚废气,考察了气体空床停留时间(EBRT)、容积负荷、喷淋密度及营养液pH对生物滴滤塔性能的影响。实验结果表明:当EBRT为90 s、进气甲硫醚质量浓度为150 mg/m~3、喷淋密度为0.65 m~3/(m~2·h),营养液pH为6.8时,甲硫醚去除率为90%;容积负荷高于15 g/(m~3·h)时,对生物滴滤塔的性能产生抑制作用;EBRT为90 s及60 s时,最佳喷淋密度分别为0.56~0.65 m~3/(m~2·h)及0.65~0.75 m~3/(m~2·h);降解甲硫醚的微生物对pH的变化较敏感,最适营养液pH为6~7。     

沸石联合微生物固定化去除微污染水体中氨氮的研究

将沸石联合经过驯化的活性污泥微生物固定化,通过静态实验.考察了不同粒径沸石及不同组分固定化方法对沸石联合微生物固定化去除氨氮的影响;通过动态实验,考察了沸石联合微生物固定化去除微污染水体中低浓度氨氮的机制.结果表明,活性污泥经过16 d的驯化,氨氮去除率为90%以上;沸石吸附氨氮为快速吸附,粒径<0.5 mm的沸石的吸附容量明显大于其他粒径的沸石;不同组分固定化小球对氨氮的去除效率不同,各组分均有贡献,吸附容量依次为:沸石固定化小球>沸石联合微生物固定化小球>微生物固定化小球;沸石联合微生物固定化去除微污染水体中低浓度氨氮可分为4个阶段,即沸石吸附阶段、吸附饱和及微生物适应阶段、硝化作用明显加强和沸石部分再生阶段、微生物作用良好和沸石进一步再生阶段,最终沸石吸附与生物再生处于良好的动态平衡中,氨氮去除率达到60%左右.     

Continuous measurement of peroxyacetyl nitrate (PAN) in suburban and remote areas of western China

Knowledge on atmospheric abundance of peroxyacetyl nitrate (PAN) is important in assessing the severity of photochemical pollution, and for understanding chemical transformation of reactive odd nitrogen and its impact on the budget of tropospheric ozone (O₃). In summer 2006, continuous measurements of PAN were made using an automatic GC–ECD analyzer with an on-line calibrator at a suburban site of Lanzhou (LZ) and a remote site of Mt. Waliguan (WLG) in western China, with concurrent measurements of O₃, total reactive nitrogen (NO_y) and carbon monoxide (CO). At LZ, several photochemical episodes were observed during the study, and the average mixing ratio of PAN (plus or minus standard deviation) was 0.76 (±0.89) ppbv with the maximum value of 9.13 ppbv, compared to an average value of 0.44 (±0.16) ppbv at remote WLG. The PAN mixing ratios in LZ exhibited strong diurnal variations with a maximum at noon, while enhanced concentrations of PAN were observed in the evening and a minimum in the afternoon at WLG. The daily O₃ and PAN concentration maxima showed a strong correlation (r² = 0.91) in LZ, with a regression slope (PAN/O₃) of 0.091 ppbv ppbv^?1. At WLG, six well-identified pollution plumes (lasting 2–8 h) were observed with elevated concentrations of PAN (and other trace gases), and analysis of backward particle release simulation shows that the high-PAN events at WLG were mostly associated with the transport of air masses that had passed over LZ.     

Ag/Cu合金触点废料回收铜粉的工艺研究

Ag/Cu合金触点废料含Ag量在30%(质量分数)以上,含Cu量在60%(质量分数)以上、含Sn量在2%(质量分数)以上.先将Ag/Cu合金触点废料中的Cu分离,然后采用葡萄糖预还原、水合肼再还原制得了粒径在0.3～O.6 pm的类球形超细铜粉(纯度≥99.9%).研究表明,适量聚乙烯吡咯烷酮(PVP)的加入有助于超细铜粉粒径均匀且形貌趋于一致;量佳反应温度为70℃;抗氧化剂苯并三氮唑可以有效防止超细铜粉的表面氧化.     

污染物负荷对曝气生物滤池处理效果的影响研究

考察了进水有机负荷和氨氮负荷对曝气生物滤池出水水质的影响.结果表明,系统COD、氨氮和TN的去除率随进水有机负荷的增加而下降,在氨氮为28.3～33.6 mg/L、TN为39.0～45.8 mg/L条件下,有机负荷小于3.53 kg/(ms3·d)时,出水COD、氨氮和TN分别小于50、5、15 mg/L,去除率分别在85%、85%和65%以上;氨氮和TN的去除率随氨氮负荷的增加而下降,在COD为287.6～313.4 mg/L、氨氮负荷小于0.56 kg/(m3·d)时,出水氨氮小于8 mg/L,去除率在85%以上,出水TN小于15mg/L,去除率在65%以上.