微电解—芬顿氧化工艺预处理高浓度松香改性酚醛树脂生产废水

为了降低松香改性酚醛树脂生产废水的COD并改善其可生化性,采用微电解—芬顿氧化工艺对该废水进行预处理。研究了pH、微电解反应时间、曝气、双氧水投加量等对微电解和芬顿氧化处理效果的影响,考察了COD去除率和BOD₅/COD值的变化趋势。实验结果表明：曝气条件下,调节废水pH为4、进行2次微电解、微电解反应时间各2.0 h时,废水的COD去除率为38%,BOD₅/COD值提高为0.18;再投加7.5%（w）的双氧水,废水的COD去除率为65.3%,BOD₅/COD值为0.37。采用微电解—芬顿氧化的预处理工艺,不仅有效去除了废水的COD,而且显著改善了废水的可生化性。     

络合滴定法测定工业废水中的硫酸根离子

通过对乙二胺四乙酸（EDTA）滴定检测硫酸根离子法的改进，实现了可以同时消除钙、镁及其他重金属离子、碳酸根离子、磷酸根离子干扰的目的。该方法简单、快捷、准确度高，加标回收率为96．38％－99．69％，变异系数为1．2％－1．49％，尤其适用于污染较为严重水体的分析。     

高效液相色谱法测定全氟辛酸铵

全氟辛酸铵是聚四氟乙烯生产废水中的重要污染物,本文采用高效液相色谱对全氟辛酸铵进行定量分析,通过流动相的离子抑制法,达到了满意的检测效果。     

镧对酸雨胁迫下水稻种子可溶性蛋白和脯氨酸含量的影响

分别采用pH值为2.0,2.5,3.0,3.5,4.0,4.5和5.0的模拟酸雨和La(浓度为1mg·l-1)处理水稻种子,测定不同酸雨胁迫下La对水稻种子可溶性蛋白和脯氨酸含量的影响,结果表明,当酸雨胁迫7d时,随胁迫强度的增加(pH5.0-2.0),可溶性蛋白含量逐渐降低,而脯氨酸含量逐渐升高.La可缓解pH5.0-3.0胁迫的伤害;但对pH2.5-2.0无明显防御作用.pH4.0时,解除酸雨胁迫(t=5d,3d)后可溶性蛋白含量即时提升(第6天和第4天),La处理亦可提高可溶性蛋白含量,对脯氨酸含量均无明显影响,pH2.5处理过长时(t≥5d),对水稻种子造成不可逆伤害,可溶性蛋白含量小于对照,而脯氨酸含量大于对照,La处理无明显效应;当酸雨处理3d时,可溶性蛋白与脯氨酸含量均显著大于对照,经La处理后均有所提高,表明La丑对酸雨胁迫下水稻种子萌发有一定防御作用.     

单级SBR生物膜中全程自养脱氮的研究

研究了具有全程自养脱氮作用的生物膜中无机碳源浓度、pH值、溶解氧(DO)对全程自养脱氮的影响.结果表明,当NaHCO3浓度从1.75g/L上升到2.50g/L时,反应体系中的pH值从7.6～8.0上升到8.8左右,氨氮转化率和总无机氮去除率分别急剧下降到53%和48.8%.在进水氨氮负荷为60g/(m³·d)时,最佳DO应控制在0.5～0.7mg/L,此时氨氮转化率达到90%以上.     

The performance of nitrate-reducing Fe(II) oxidation processes under variable initial Fe/N ratios: The fate of nitrogen and iron species

•Bacterially-mediated coupled N and Fe processes examined in incubation experiments. •NO₃⁻ reduction was considerably inhibited as initial Fe/N ratio increased. •The maximum production of N₂ occurred at an initial Fe/N molar ratio of 6. •Fe minerals produced at Fe/N ratios of 1–2 were mainly easily reducible oxides. The Fe/N ratio is an important control on nitrate-reducing Fe(II) oxidation processes that occur both in the aquatic environment and in wastewater treatment systems. The response of nitrate reduction, Fe oxidation, and mineral production to different initial Fe/N molar ratios in the presence of Paracoccus denitrificans was investigated in 132 h incubation experiments. A decrease in the nitrate reduction rate at 12 h occurred as the Fe/N ratio increased. Accumulated nitrite concentration at Fe/N ratios of 2–10 peaked at 12–84 h, and then decreased continuously to less than 0.1 mmol/L at the end of incubation. N₂O emission was promoted by high Fe/N ratios. Maximum production of N₂ occurred at a Fe/N ratio of 6, in parallel with the highest mole proportion of N₂ resulting from the reduction of nitrate (81.2%). XRD analysis and sequential extraction demonstrated that the main Fe minerals obtained from Fe(II) oxidation were easily reducible oxides such as ferrihydrite (at Fe/N ratios of 1–2), and easily reducible oxides and reducible oxides (at Fe/N ratios of 3–10). The results suggest that Fe/N ratio potentially plays a critical role in regulating N₂, N₂O emissions and Fe mineral formation in nitrate-reducing Fe(II) oxidation processes.     

Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment

• Gas diffusion electrode (GDE) is a suitable setup for practical water treatment. • Electrochemical H₂O₂ production is an economically competitive technology. • High current efficiency of H₂O₂ production was obtained with GDE at 5–400 mA/cm². • GDE maintained high stability for H₂O₂ production for ~1000 h. • Electro-generation of H₂O₂ enhances ibuprofen removal in an E-peroxone process. This study evaluated the feasibility of electrochemical hydrogen peroxide (H₂O₂) production with gas diffusion electrode (GDE) for decentralized water treatment. Carbon black-polytetrafluoroethylene GDEs were prepared and tested in a continuous flow electrochemical cell for H₂O₂ production from oxygen reduction. Results showed that because of the effective oxygen transfer in GDEs, the electrode maintained high apparent current efficiencies (ACEs,>80%) for H₂O₂ production over a wide current density range of 5–400 mA/cm², and H₂O₂ production rates as high as ~202 mg/h/cm² could be obtained. Long-term stability test showed that the GDE maintained high ACEs (>85%) and low energy consumption (<10 kWh/kg H₂O₂) for H₂O₂ production for 42 d (~1000 h). However, the ACEs then decreased to ~70% in the following 4 days because water flooding of GDE pores considerably impeded oxygen transport at the late stage of the trial. Based on an electrode lifetime of 46 days, the overall cost for H₂O₂ production was estimated to be ~0.88 $/kg H₂O₂, including an electricity cost of 0.61 $/kg and an electrode capital cost of 0.27 $/kg. With a 9 cm² GDE and 40 mA/cm² current density, ~2–4 mg/L of H₂O₂ could be produced on site for the electro-peroxone treatment of a 1.2 m³/d groundwater flow, which considerably enhanced ibuprofen abatement compared with ozonation alone (~43%–59% vs. 7%). These findings suggest that electrochemical H₂O₂ production with GDEs holds great promise for the development of compact treatment technologies for decentralized water treatment at a household and community level.     

Exogenously applied oxalic acid assists in the phytoremediation of Mn by Polygonum pubescens Blume cultivated in three Mn-contaminated soils

• The OA supply significantly increased the water-extractable Mn in all soils. • All OA supply levels promoted plant growth in unexplored soil. • Low OA supply level promoted plant growth in explored and tailing soils. • OA amendment increased the Mn concentrations and total Mn in P. pubescens. • P. pubescens experienced less Mn stress in unexplored soil than in the other two soils. The current study evaluated the effects of oxalic acid (OA) application on the growth and Mn phytoremediation efficiency of Polygonum pubescens Blume cultivated in three different manganese (Mn)-contaminated soils sampled from an unexplored area (US), an explored area (ES) and a tailing area (TS) of the Ertang Mn mine, South China. The supplied levels of OA were 0 (control), 1 (low level), 3 (medium level), and 9 (high level) mmol/kg, referred to as CK, OA1, OA3 and OA9, respectively. The results revealed that the average water-extractable Mn concentrations US, ES and TS amended with OA increased by 214.13, 363.77 and 266.85%, respectively. All OA supply levels increased plant growth and Mn concentrations in US. The low OA supply level increased plant growth in ES and TS; however, contrasting results were found for the medium and high OA supply levels. Plant Mn concentrations and total Mn increased in ES and TS in response to all OA supply levels. Total Mn in the aerial parts increased by 81.18, 44.17 and 83.17% in US, ES and TS, respectively; the corresponding percentages for the whole plants were 81.53, 108.98 and 77.91%, respectively. The rate of ·O₂⁻ production and malondialdehyde (MDA) concentrations increased in response to OA amendment, especially the medium and high OA supply levels in ES and TS. In general, antioxidant enzymes might play a vital role in alleviating Mn stress in plants cultivated in US, while non-enzymatic antioxidants might be the main factor for plants cultivated in ES and TS.     

柠檬酸与磷共存对土壤吸附镉的影响

以武汉市棕红壤为研究材料,采用室内培养和等温平衡吸附实验,研究了磷和柠檬酸共存下对土壤吸附镉的影响;并模拟干湿交替实验,通过BCR连续提取,研究了不同剂量磷和柠檬酸处理后,经多次干湿交替后镉的形态变化.结果表明,经10 mg·L^-1 CdCl₂溶液处理后的土壤胶体,添加较低质量浓度（40 mg·L^-1）的磷对其吸附镉的影响不明显,而添加磷质量浓度较高（80 mg·L^-1）时可显著提高其对镉的吸附,吸附量较CK处理增加78 g·kg^-1,吸附率提高7.89%;向经40 mg·L^-1磷溶液处理过的土壤胶体中加入柠檬酸,可减弱其对镉吸附,且随柠檬酸浓度增高,抑制效果增加,而且对低剂量磷（40 mg·L^-1）处理的土壤胶体抑制作用更明显,加入1 mmol·L^-1与5 mmol·L^-1柠檬酸后,土壤胶体对镉的吸附率分别降低了30.89%与40.97%;而当磷处理质量浓度较高时,柠檬酸的影响则不显著.周期性的干湿交替显著促进土壤中镉由弱酸提取态及可还原态向可氧化态及残渣态的转变,即磷钝化的镉在柠檬酸的影响下,随干湿交替次数的增加,镉的有效性降低.     

一株发酵纤维素产丁酸菌及其代谢动力学特性

为开发降解纤维素产丁酸菌的种子资源,从牛粪、猪粪堆肥、玉米地土壤和腐木混合物的富集样品中分离得到一株厌氧降解纤维素产丁酸菌.该菌株细胞呈杆状,长7.1~9.1μm,直径1.2μm左右,经鉴定为丁酸梭菌(Clostridium butyricum),命名为C. Butyricum DCB.在35℃条件下,菌株DCB在纤维二糖液体培养基中的最大比生长速率为0.6536h^-1,世代时间为1.06h,纤维二糖降解速率为0.1g/(L·h),丁酸生成速率为0.06g/(L·h).该菌株利用纤维素发酵产丁酸的转化率高达0.23g/g,具有良好的开发前景.