地下渗滤系统处理农村生活污水的研究

在天津武清区一村落构建了2个并行的地下渗滤系统,考察了其对农村生活污水的处理效果。该系统水力负荷为10 cm/d,处理能力为50 t/d。填充介质选用土壤、陶粒、炉渣和两种自然有机质,按5∶2∶2∶1的比例配置的人工土层。结果表明地下渗滤系统对污水中各种主要污染因子均有一定的去除效果,在进水COD和C/N较低的不利条件下,COD、总磷、氨氮、总氮、悬浮物均得到有效去除,出水中各项污染指标平均浓度均达到《城镇污水处理厂污染物排放标准》中的一级A标准;具体到不同的污染指标,添加了不同有机质的2个并行系统的处理效果也有所不同。总体上看,地下渗滤系统作为农村生活污水的处理设施有很好的应用前景。     

北京和上海典型复合包装废物处置环境影响比较

采用生命周期评价法研究比较了北京和上海两地纸塑铝复合包装处置阶段的环境影响。通过现场和资料调研的方式获得此阶段的能量物质的输入输出和环境外排数据。结果表明:北京和上海两地纸塑铝复合包装处置阶段的环境影响潜值分别为-0.428 Pt和9.776 Pt,其主要集中在气候变化、土地占用和无机物对健康的损害三方面;每提高10%的回收率,其环境影响潜值北京和上海可分别降低5.446 Pt和5.799 Pt;上海地区纸塑铝复合包装处置阶段对环境的影响在任何同回收率的情况都要高于北京地区,其主要原因是上海地区填埋产生的温室气体释放量过大和再生企业距离打包点较远。     

聚合物驱采出水中聚丙烯酰胺的微生物联合降解作用研究

通过对2株细菌的培养降解实验研究聚丙烯酰胺(hydrolyzed polyacrylamide,HPAM)降解菌对水环境下聚丙烯酰胺的降解作用,讨论协同降解机理。2株降解聚丙烯酰胺的菌株假单胞菌CJ419、枯草芽孢杆菌FA16在初始30℃废水样品上培养,定期测量细菌生物量和HPAM降解率。培养30 d后CJ419和FA16对聚合物的降解率最大值分别达到30.4%和25%,而以1∶1比例的混合菌降解率最大值达到80.3%。对2株菌胞外各组分研究表明:混合菌降解HPAM的机理主要由胞外降解酶系水解聚合物侧链基团导致HPAM降解为小分子物质,同时生长过程中降解菌还会释放非蛋白还原性物质引发氧化反应共同参与HPAM降解。     

天然矿物复合陶瓷材料制备及对印染废水脱色的研究

印染废水是水污染的重要来源之一,是目前较难处理与急需处理的工业废水。天然矿物材料通过吸附、光催化降解等作用可有效去除印染废水中的染料分子。为了开发新型环境矿物材料,采用白云石、菱镁矿等天然矿物作为原材料经粉碎、配料、造粒、烧结、水洗合成天然矿物复合陶瓷材料,用于印染废水的脱色。对酸性黑10B和直接混纺蓝D-3GL2种不同性质的染料废水进行了定量脱色研究。研究表明,当材料投加量为8 g/L,处理时间12 h,pH2~8,对2种废水均有95%以上的去除率;经800℃煅烧15 min的工艺进行再生活化,实现了陶瓷材料的循环使用。此方法制得的天然矿物复合陶瓷材料微孔结构明显,机械强度高,散失率低,解决了粉末材料在废水脱色过程中存在的固液难以分离的问题。     

麻质活性炭的制备及其对Cu~(2+)的吸附研究

以废麻为原料,KOH为活化剂制备粉状活性炭,通过静态吸附实验研究了活性炭对Cu2+的吸附性能,探讨了溶液起始pH值、活性炭投加量、吸附时间、起始Cu2+质量浓度等对Cu2+吸附效果的影响。结果表明,溶液pH和活性炭投加量对吸附效果有较大影响,活性炭对Cu2+的吸附率在60 min内超过50%,初始浓度在10~50 mg/L时,活性炭对Cu2+的吸附量与起始浓度近似成正比。采用Langmuir、Freundlich吸附等温式对吸附平衡数据进行了拟合,结果表明吸附等温线符合Frenudlich模型。采用傅立叶红外光谱法(FT-IR)分析了活性炭的表面官能团,分析表明活性炭表面酸性官能团可能是吸附Cu2+的活性中心。     

序批式活性污泥法工艺处理含盐废水动力学模型研究

为了实现含盐废水序批式活性污泥法(SBR)工艺的启动,采用逐步提高废水中NaCl浓度负荷的方法对活性污泥进行驯化,并建立有机物(COD)与NH4+-N的降解动力学模型。结果表明,经过280d的驯化和稳定运行,SBR系统可以有效降解含盐废水,COD去除率高于74%,NH4+-N平均去除率高于90%,实现了SBR工艺处理含盐废水的启动和稳定运行。含盐废水有机物(COD)降解动力学参数r0(无盐条件下的COD去除速率)为129.87mg/(L.h),KY(盐抑制常数)为7700.01mg/L;含盐废水硝化反应动力学参数Ks(饱和常数)为186.52mg/L,vmax(NH4+-N的最大比降解速率)为0.0034h-1。     

Ferrate(VI) enhanced photocatalytic oxidation of pollutants in aqueous TiO<Subscript>2</Subscript> suspensions

Background, aim and scope  

Photocatalytic oxidation using UV irradiation of TiO₂ has been studied extensively and has many potential industrial applications, including the degradation of recalcitrant contaminants in water and wastewater treatment. A limiting factor in the oxidation process is the recombination of conduction band electrons (e ⁻ _cb) with electron holes (h_vb⁺) on the irradiated TiO₂ surface; thus, in aqueous conditions, the presence of an effective electron scavenger will be beneficial to the efficiency of the oxidation process. Ferrate (FeO₄²⁻) has received much recent attention as a water treatment chemical since it behaves simultaneously as an oxidant and coagulant. The combination of ferrate [Fe(VI)] with UV/TiO₂ photocatalysis offers an oxidation synergism arising from the Fe(VI) scavenging of e ⁻ _cb and the corresponding beneficial formation of Fe(V) from the Fe(VI) reduction. This paper reviews recent studies concerning the photocatalytic oxidation of problematic pollutants with and without ferrate.     

Sorption kinetic characteristics of polybrominated diphenyl ethers on natural soils

Sorption kinetic characteristics of BDE-28 and BDE-47 on five natural soils with different organic carbon fractions were investigated, and could be satisfactorily described by a two (fast and slow)-compartment first-order model with the ratio of rate constants ranged from 9 to 94 times. The fast compartment made a dominant contribution (71% ∼ 94%) to the total sorption amount in the whole process, and accounted for over 90% of the increase in the total sorption amount at initial 5 h. The influence of the slow compartment on the increase in the total sorption amount became principal (above 90%) in the subsequent stage approximately from 9 h or 25 h to the apparent equilibrium at 265 h. The results proposed the different sorption behaviors of the mathematically classified compartments for BDE-28 and BDE-47, which may correspond to the different soil components, such as soil organic fractions with amorphous and condensed structures, respectively.     

Biodegradation and biotransformation of wastewater organics as precursors of disinfection byproducts in water

Laboratory experiments were carried out to investigate wastewater organics as the precursors of disinfection byproducts (DBPs) in drinking water supply. The focus was on the change in wastewater DBP precursors during biological degradation under simulated natural conditions. The wastewater and its treated secondary effluent were characterized for DBP formation potential (DBPFP) and DBP speciation profile, including trihalomethanes, haloacetic acids, chloral hydrate, and nitrogen-containing DBPs. Several model organic compounds, including humic acid, tannic acid, glucose, starch, glycine, and bovine serum albumin (BSA), were used to represent the different types of organic pollutants in wastewater discharge. The results show that the DBPFP of wastewater decreased after biodegradation, but the remaining organic matter had a greater DBPFP yield with chlorine. Different model organics displayed different changes in DBPFP during biodegradation. The DBPFP remained largely unchanged for the glycine solution, decreased greatly for the tannic acid and BSA solutions, and increased nearly 3-fold for the glucose and starch solutions after 10d of biodegradation. Meanwhile, the DBPFP yield increased from 3 for glycine to 51μg DBP mg(-1) C for its degradation residue, and from 1 for glucose and starch to 87 and 38μg DBP mg(-1) C for their organic residues, respectively. Although biodegradation may effectively remove some DBP precursors, biotransformation during the process produces new DBP precursors in the form of soluble microbial products (SMPs). The experimental results reveal that SMPs may be an important source of wastewater-derived DBP precursors in natural waters.     

小型燃油锅炉NOx的排放特征与管理控制

以68台燃油锅炉（≤10～MW）NOx排放实测数据为基础,通过统计分析方法,研究了NOx的排放特征;通过对比分析,探讨了我国燃油锅炉NOx排放控制与管理现状,讨论了进一步加强我国燃油锅炉NOx排放管理控制的可能性与可行性,并提出了相应的管理控制建议。结果表明,NOx平均排放浓度为318．2mg／m^3,基于燃料消耗量的平均排放因子为4．4kg／t,基于燃料发热量的平均排放因子为102．8ng／J,基于燃料氮含量的平均排放因子为2．1mg／mg;建议采取分阶段控制的方式,逐步提高NOx排放限制,从而实现控源减排目标。