纳滤膜分离技术在安全饮用水保障中的应用

纳滤膜分离技术在饮用水制备方面具有独特的作用,是保障安全饮用水生产的有效方法。本文详细综述了国内外纳滤膜技术在饮用水生产中应用研究的最新进展,以及纳滤膜对地表水或地下水中存在的各种无机、有机污染物的分离特性。     

地震台站观测系统的防雷技术——以陕西为例

雷电对地震观测台站的危害已成为影响台站长期稳定运行的重要因素之一。针对地震台站观测系统建设,从4个方面对避雷技术进行了分析设计。同时以陕西省的地震观测台站为例,具体说明了防雷措施的应用方法及应用效果。     

基于虚拟仪器技术的振动台模型试验98通道动态信号采集系统研制

土工结构振动台模型试验除了需采集常规的加速度、位移、应变信号外,还需采集模型场地土中振动孔隙水压力、动土压力等信号,由于同步采集的动态信号的多样性和复杂性,一般的振动台信号采集系统难以满足这样的多种动态信号同步采集要求。基于传感器融合技术和虚拟仪器技术,研发了一套适用于多种类型信号输入的动态信号同步采集系统,可实现80通道动态信号、18通道数字信号的同步采集、回放和频谱分析等功能,并具有界面友好、使用维护方便等特点。     

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.     

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.     

易失稳瓦斯抽采钻孔加固技术数值模拟研究

针对松软煤层瓦斯抽采钻孔稳定性差、钻孔形变较大、钻孔及周围煤体漏风严重等造成钻孔密封难的技术难题,提出了预先采用加固技术来提高松软煤层瓦斯抽采钻孔的稳定性,合理的解决钻孔高效密封的现实难题。首先,阐述了易失稳瓦斯抽采钻孔加固技术的基本原理。其次,利用FLAC3D模拟软件对比分析了松软煤层、硬质煤层在不同固孔材料固化后钻孔周围位移场变化。研究表明:采取固孔措施后的钻孔相比措施前等值线分布稀疏,梯度较小,不同位置处的煤体的位移量差别较小。钻孔形成后,顶部位移量均大于底部位移量,左右两帮的位移量基本相同,有效的降低钻孔周边煤体的位移变化量,增强钻孔稳定性,为钻孔的高效密封提供了保障。     

基于Web的油气集输联合站变更管理信息系统设计与实现

为了完善采油厂实现油气集输联合站变更管理的信息化,减少变更活动中人工操作的工作量。提出了基于Web的变更管理系统架构方案,并运用Java技术及SQL数据库技术研发出变更管理信息系统。系统能够实现变更申请审批、变更风险评估、变更现场监督、变更历史记录查询以及变更作业票管理等功能,并在某油田多个油气集输联合站得到应用。应用结果表明,基于Web的变更管理系统具有较好的现场应用性,能够切实提高联合站变更管理的效率,有效地发挥变更管理在规章制度更新、过程工艺改进以及工作场所变化等方面的优势,从而通过进一步完善联合站安全管理体系,最终为企业安全生产提供工具化支持。     

受四环素影响的活性污泥胞内外聚合物特征

利用离心加超声的方法对处理四环素抗生素废水的活性污泥胞外聚合物(EPS)和胞内聚合物(IPS)进行提取,将其分为-溶解型胞外聚合物(slime)、松散附着型胞外聚合物(LB)、紧密附着型胞外聚合物(TB)、胞内聚合物(IPS).用BCA法和蒽酮-硫酸法测定了各层EPS和IPS溶液中的蛋白质和多糖含量,同时用三维荧光光谱扫描(EEM)和同步荧光光谱扫描(SFS)对其中的溶解性有机物(DOM)进行定性和定量分析,结果表明在EPS中的蛋白质和多糖的含量高于IPS,且蛋白质含量均比多糖含量高,而在slime和IPS中的蛋白质和多糖的含量高于LB和TB;低激发波长类色氨酸和高激发波长类色氨酸是EPS和IPS溶液的主要成分,且溶液中的溶解性代谢产物和芳香蛋白类物质相对含量在slime、LB、TB和IPS逐渐增加,而难降解有机物-腐殖酸类物质的相对含量逐渐降低;进水四环素浓度与污泥各层EPS和IPS溶液中DOM也具有较好的相关性;三维荧光法检测溶液中的DOM与化学分析测试出的蛋白质含量具有较好的相关性.     

A photolysis coefficient for characterizing the response of aqueous constituents to photolysis

UV photolysis and UV based advanced oxidation processes (AOPs) are gaining more and more attention for drinking water treatment. Quantum yield (ø) and molar absorption coefficient (ε) are the two critical parameters measuring the effectiveness of photolysis of a compound. The product of the two was proposed as a fundamental measure of a constituent’s amenability to transformation by photolysis. It was shown that this product, named the photolysis coefficient, k _p , can be determined using standard bench tests and captures the properties that govern a constituent’s transformation when exposed to light. The development showed the photolysis coefficient to be equally useful for microbiological, inorganic and organic constituents. Values of k _p calculated by the authors based on quantum yield and molar absorption coefficient data from the literature were summarized. Photolysis coefficients among microorganisms ranged from 8500 to more than 600000 and are far higher than for inorganic and organic compounds, which varied over a range of approximately 10 to 1000 and are much less sensitive to UV photolysis than the microorganisms.