不同温度桉树叶生物炭对Cd2+的吸附特性及机制

通过元素分析、BET-N₂、Zeta电位、Boehm滴定,SEM-EDS、FTIR等分析方法对不同热解温度（300、500和700℃）下制备的桉树叶生物炭进行表征,研究了3种生物炭（BC300、BC500和BC700）对Cd²⁺的吸附特性与机制.结果表明,随温度升高,生物炭产率下降,灰分、pH值和Zeta负电荷量上升,比表面积增大.当Cd²⁺浓度为20mg/L时,平衡时间依次为80min（BC700）<360min（BC500）<540min（BC300）,均符合准二级动力学模型（R²>0.98）,以化学吸附为主.BC300和BC500吸附过程均符合Langmuir和Freundlich模型,BC700更符合Freundlich模型,最大吸附量依次为BC700（94.32mg/g） > BC500（67.07mg/g） > BC300（60.38mg/g）.在Boehm滴定结果分析的基础上,结合FTIR和SEM-EDS,表明生物炭吸附机制主要为静电吸附和官能团络合作用.BC700吸附性能最佳,原因可能是具有较大的比表面积、较多的负电荷量和较为丰富的官能团.     

新型铈钨钛复合氧化物催化还原脱硝机理

利用水热共沉淀法制备了铈钨钛复合氧化物催化剂,考察了H₂O₂络合修饰对其催化脱硝转化频率（TOF）的影响;并借助傅里叶原位红外光谱仪研究了H₂O₂络合修饰后铈钨钛复合氧化物的催化脱硝机理.结果表明：H₂O₂络合修饰可增强铈钨钛复合氧化物表面Brønsted酸位强度,提高其表面NH₃低温吸附和中低温NH₃-SCR脱硝性能,400℃时其NO_x催化脱除频率TOF高达0.658s^-1;NH₃和NO_x在H₂O₂络合修饰后铈钨钛复合氧化物表面存在竞争吸附,其表面催化脱硝反应主要为吸附态NH₃、NH₂和NH₄⁺与气态NO+O₂的反应,其低温NH₃-SCR反应机理遵循Eley-Rideal（E-R）机理.     

基于SWAT模型的泗河流域除草剂迁移模拟

泗河流域农药污染对南四湖湖泊乃至南水北调工程具有重要的影响,为了解流域农药迁移过程并对其采取治理措施,本研究在泗河流域通过实地采样与调查、室内实验分析、数据统计等手段,借助SWAT模型对流域除草剂阿特拉津及其代谢产物进行迁移模拟.结果表明,除草剂输出与流域径流量有很高的相关性,输出时间以7~8月份为主,输出量占全年的69%以上.且受河道长度、耕地分布等因素的影响,阿特拉津的输出量以东部上游地区和中部地区为主,流域出水口处的阿特拉津输出量居中等水平;阿特拉津代谢产物DEA和DIA的输出量的空间分布相似,以下游流域出口处和中部地区为主.本研究可为流域除草剂迁移治理提供理论支持.     

河北省涞水县大气颗粒物单颗粒分析表征及来源识别

为了解河北省涞水县颗粒物污染特征,采用单颗粒分析技术扫描电镜-X射线能谱法和气团后向轨迹分析技术对该县2015年3个典型污染时段〔即正常管控、严格管控（2015年阅兵期间）及发生严重颗粒物染污〕采集的7个大气颗粒物样品进行了分析表征和来源解析.共测量了1 506个粒径≥0.5 μm的单颗粒,其中粒径小于2.5 μm的颗粒占98%以上,测量结果揭示了细颗粒污染特征.结果表明:①碳质颗粒为主要颗粒物种类,其检出数目占比在90%以上.②非供暖期严格管控时段,当地居民日常生活产生的球形碳质颗粒检出数目占比最高.③非供暖期正常管控时段,机动车排放的碳质集合体颗粒检出数目占比最高,交通污染贡献最大.④供暖期球形碳质颗粒检出数目占比最高,含硫颗粒检出数目占比相对增加,燃煤的贡献最大.3个采样时段48 h气团后向轨迹分析结果表明,在空气质量良好、颗粒物污染水平较低的情况下,影响研究区域空气质量的主要是本地源;雾霾天气（处于严重颗粒物污染时段）时,西南方向外来源和本地源共同构成研究区域的颗粒物污染状态.      

水解酸化-地下渗滤技术处理生活污水的工艺研究

为优化水解酸化-地下渗滤系统(Hydrolytic Acidifi-cation-Subsurface Wastewater Infiltration System,HA-SWIS)工艺参数,提高分散式污水处理效果,通过控制HA水力停留时间(Hydraulic Retention Time,HRT)、搅拌速度、SWIS水力负荷(Hydraulic Load Rate,HLR)及干湿比,考察系统COD、NH4+-N、TN和TP的去除效果。由于温度控制在18～22℃,忽略温度对COD、NH4+-N、TN和TP去除效果的影响。结果表明,随优化参数改变,HA-SWIS联合工艺去除污染物效果存在显著性差异(p <0. 05)。当HA搅拌速度为15 r/min、HRT为2 h时,SWIS的HLR为0. 08～0. 12 m3/(m2·d),干湿比为1∶1～2∶1时,联合工艺对COD、NH4+-N、TN和TP的去除效率最高,分别为92. 0%、78. 6%、65%和92. 7%。该装置占地小,基建费用低,无需药剂投入,每吨水处理费用0. 46元/t,处理水质可回用,满足景观水要求(GB/T 18921—2002),适用于管网不完善地区。     

活性炭吸附二硫化碳解析气相色谱法测定废气中乙酸乙酯和乙酸丁酯研究

采用活性炭管吸附废气中的乙酸乙酯和乙酸丁酯,经二硫化碳萃取解析,使用DM-1色谱柱分离后FID检测.实验结果表明:(1)采用活性炭管吸附废气中的目标组份,富集效率良好,二硫化碳解析率可达92％以上;(2)当乙酸乙酯和乙酸丁酯的含量为6.8～102 ng时,测定结果的相对标准偏差分别在1.8％ ～4.2％和3.2％ ～6.1％之间(n=6);(3)当样品采集量为30 L时,方法检出限分别为0.02 mg·m-3和0.02 mg·m-3.因此,方法能满足实验对空气废气中的乙酸乙酯和乙酸丁酯的检测要求.     

Algal uptake of dissolved organic nitrogen in wastewater treatment plants

The algal uptake of dissolved organic nitrogen(DON) in the anaerobic–anoxic–oxic(A_2O)process was investigated in this study. Anaerobic, aerobic and effluent DON samples from two wastewater treatment plants(WWTPs) were separated into hydrophilic and hydrophobic fractions using a DAX-8 resin coupled with an anion exchange resin and a nanofiltration(NF)pretreatment. Hydrophilic DON accounted for 66.66%–88.74% of the entire DON for the two plants evaluated. After a 15-day incubation, 16.95%–91.75% DON was bioavailable for algal growth, and untreated samples exhibited higher DON bioavailability, with 52.83% DON average uptake rates, compared with the hydrophilic and hydrophobic fractions(45.53% and 44.40%, respectively) because the pretreatment caused the inorganic salt to be resistant to algae. Anaerobic untreated samples, hydrophilic fractions and hydrophobic fractions showed higher DON reduction rates and higher biomass accumulation compared with the other DON fractions due to the decomposition of resistant organics by anaerobic and anoxic bacteria.DON in aerobic and effluent samples of plant A was more bioavailable than that of plant B with usages of 27.49%–55.26% DON. DON bioavailability in the anaerobic–anoxic–oxic process decreased in the following order: anaerobic effluent aerobic. The DON contents were reduced after anaerobic treatment in the two plants. The EEM-PARAFAC model identified three DON components, including two humic acid-like substances and one protein-like substance in plant A and two protein-like substances and one humic acid-like substance in plant B.     

大宝山尾矿库区水体重金属污染特征及生态风险评价

为阐明大宝山槽对坑尾矿坝水体中重金属的污染特征,分析了过滤水、悬浮物和沉积物中重金属的含量,并采用地累积指数法和潜在生态风险指数法对沉积物中重金属污染程度进行评价.结果表明,水体中ρ(Cu)、ρ(Zn)、ρ(Cd)和ρ(Pb)分别高达7.228、41.190、0.178和0.377 mg/L,其中pH和E_h(氧化还原电位)是影响重金属含量的重要因素.悬浮物和沉积物中重金属沿河流断面呈相似的空间分布规律,Cu和Cd污染较为严重.从尾矿库N1采样点至河流下游N4采样点处,重金属沿水流方向呈现溶解态向悬浮态和沉积态迁移特征,而Cu的迁移行为有所不同.据地累积指数法的评价结果,各重金属I_geo(地累积指数)顺序为Cu>Cd>Zn>Pb,Cu和Cd的I_geo平均值分别为4.552和1.605,属重度污染和偏中污染.潜在生态风险指数法评价表明,各重金属危害程度为Cu>Cd>Pb>Zn,Cu和Cd的E_ri(潜在生态危险系数)平均值分别为193.3和143.0,均属强生态危害级别.两种方法均表明Cu和Cd为主要风险元素.该研究区域的RI(生态危害指数)为163.1～576.6,平均值为356.6,属强生态危害级别,相关部门应采取相应措施,加强对该区域污染防治和风险管理.      

燃气发动机瞬态工况下NOx排放特征

NO_x排放控制是发展燃气汽车的核心问题.为获得增压中冷燃气发动机瞬态工况NO_x的排放特征,实验选取了6MK375N-50增压中冷燃气发动机,研究了不同转速、转矩、进气流量、进气温度及湿度对NO_x排放的影响.试验结果表明NO_x的排放随着转速的增加先升高后减缓,转速为1400 r·min-1时NO_x排放最高,转矩的增加也会使NO_x排放增加,随着进气流量的增加,NO_x排放量先增加后稳定,进气流量为180 kg·h~(-1)时NO_x排放最高,进气温度对NO_x排放也有直接影响,进气温度为31℃时NO_x排放最高,随着进气湿度的增加,NO_x排放水平降低,对试验结果的双因素方差分析得到,各影响因素对NO_x的排放影响均非常显著.对1400 r·min-1下各个工况对应NO_x进行拟合,变化规律符合公式y=a-b×ln(x+c).     

Effect of pretreatment techniques on food waste solubilization and biogas production during thermophilic batch anaerobic digestion

The purpose of this study was to optimize the alkaline, ultrasonication, and thermal pretreatment in order to enhance the solubilization of food waste (FW) for the production of volatile fatty acids, hydrogen, and methane in thermophilic batch anaerobic digestion. Initially, the effect of pretreatment techniques in the acidogenic phase was studied, and the optimal combinations of different conditions were determined. It was found that each pretreatment technique affected food waste solubilization differently. Alkaline pretreatment increased hydrogen yield in the acidogenic sludge by four times over control. COD solubilization was increased by 47 % when FW pre-heated at 130 °C for 60 min. Ultrasonication at 20 kHz and 45 min reduced processing time to 38 h from the 60–80 h needed in normal operation. Response surface methodology (RSM) was used to optimize a combination of alkaline, ultrasonication, and thermal pretreatment. Optimized conditions were applied to methanogenic single-stage thermophilic AD process, and their impact on biogas production was monitored. Results showed that FW heated at 130 °C for 50 min geminates biogas production compared to control experiment. In conclusion, a short thermal pretreatment regime could significant affect biogas production in single-stage thermophilic AD.