顶空气相色谱法测定地表水中吡啶

采用顶空进样、毛细管柱HP -INNOWAX分离、GC -FID测定地表水中吡啶。水样顶空时通过加碳酸钠盐大幅度降低了检出限 ,最低检出浓度达到 0 0 2mg/L。本法加标回收率为 96 5 %～ 10 1% ,变异系数为 7 8%～ 9 8%。     

电子束照射法脱硫脱氮技术工艺

在阐明电子束照射法脱硫脱氮技术的机理、流程、特点的基础上 ,探讨了该工艺在应用过程中存在的主要经济、技术问题。     

生物脱硫中细菌的载体培养条件优化与动力学研究

选用氧化亚铁硫杆菌作为烟气脱硫的主要菌种在活性炭载体上进行固定化培养,研究了不同培养条件下氧化亚铁硫杆菌的生长过程,考察了细菌在载体中培养时接种量、载体投加量对细菌生长的动力学过程的影响,同时通过计算机拟合,确定了各个条件下的细菌生长动力学参数．从而确定了培养的优化条件。     

固相萃取-气相色谱/质谱法测定水中多环芳烃

建立了固相萃取-气相色谱／质谱联用测定水中多环芳烃(PAHs)的分析方法．优化了固相萃取条件。结果表明,固相萃取效率高、萃取时间短,采用MS的选择离子检测方式对实际水样中PAHs进行定性定量分析,平均回收率在80．4％～115％之间,相对标准偏差为7．03％～18．5％,方法的检出限在0．010～0．020μg／L之间。通过实际样品中PAHs的分析表明,该法快速,溶剂用量少,能满足痕量分析的要求。     

气相色谱法测定苯系物标准样品

提出了以二硫化碳为稀释剂，用氯苯作内标物，采用程序升温，调节载气流量，在一根色谱柱上使苯系物标准样品中的7个组分得到完全分离。对苯系物标准样品进行多次测定，各组分的测定结果均在标准样品的保证值范围内，相关标准差小于3％，方法的准确度和精密度均较好。     

Optimization of the O3/H2O2 process with response surface methodology for pretreatment of mother liquor of gas field wastewater

• Real ML-GFW with high salinity and high organics was degraded by O₃/H₂O₂ process. • Successful optimization of operation conditions was attained using RSM based on CCD. • Single-factor experiments in advance ensured optimal experimental conditions. • The satisfactory removal efficiency of TOC was achieved in spite of high salinity. • The initial pH plays the most significant role in the degradation of ML-GFW. The present study reports the use of the O₃/H₂O₂ process in the pretreatment of the mother liquor of gas field wastewater (ML-GFW), obtained from the multi-effect distillation treatment of the gas field wastewater. The range of optimal operation conditions was obtained by single-factor experiments. Response surface methodology (RSM) based on the central composite design (CCD) was used for the optimization procedure. A regression model with Total organic carbon (TOC) removal efficiency as the response value was established (R² = 0.9865). The three key factors were arranged according to their significance as: pH>H₂O₂ dosage>ozone flow rate. The model predicted that the best operation conditions could be obtained at a pH of 10.9, an ozone flow rate of 0.8 L/min, and H₂O₂ dosage of 6.2 mL. The dosing ratio of ozone was calculated to be 9.84 mg O₃/mg TOC. The maximum removal efficiency predicted was 75.9%, while the measured value was 72.3%. The relative deviation was found to be in an acceptable range. The ozone utilization and free radical quenching experiments showed that the addition of H₂O₂ promoted the decomposition of ozone to produce hydroxyl radicals (·OH). This also improved the ozone utilization efficiency. Gas chromatography-mass spectrometry (GC-MS) analysis showed that most of the organic matters in ML-GFW were degraded, while some residuals needed further treatment. This study provided the data and the necessary technical supports for further research on the treatment of ML-GFW.     

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.     

利用矿化垃圾层预防和控制渗滤液导排系统堵塞

在卫生填埋场中,垃圾渗滤液导排系统堵塞普遍存在,悬浮固体形成的物理堵塞、有机物降解和金属离子沉淀导致的生物-化学堵塞是引起导排系统堵塞的关键因素.本文构建了"矿化垃圾+砾石层导排"的渗滤液下渗装置,通过矿化垃圾预处理渗滤液中悬浮固体和有机物以控制导排系统发生的物理和生物-化学堵塞.结果表明,在矿化垃圾层,渗滤液中化学需氧量(COD)和悬浮固体(SS)去除较多,去除率分别达到了85%和87%,并且Ca²⁺浓度也出现了波动较大的现象;然而,渗滤液在砾石层下渗过程中,其COD、SS和Ca²⁺浓度保持稳定.并且,砾石层可排水孔隙率在长期运行的过程中没有明显变化,表明渗滤液在砾石导排层没有形成明显的沉淀.与此同时,在没有添加矿化垃圾的对照组发现,砾石层可排水孔隙率减少最多的区段是渗滤液的进水点位(可排水孔隙率减少达到了53%),即渗滤液有机负荷最大处的饱和砾石层堵塞最为严重,其无机堵塞物主要是碳酸钙等.因此,在渗滤液流入砾石层前,采用矿化垃圾层部分饱和的方式对渗滤液中有机物和悬浮固体进行预处理,可以预防和控制渗滤液在砾石层形成沉淀堵塞.研究为填埋场的运行管理渗滤液导排系统堵塞提供了新的思路和方法.     

生活污水为主要补给源的城郊排水沟渠氮磷滞留特征

为揭示生活污水补给影响下排水沟渠氮、磷滞留特征,以合肥市城郊结合部的关镇河支渠为对象,以NH₄Cl和KH₂PO₄为添加营养盐,以NaCl为保守型示踪剂,开展5次现场示踪试验. 在此基础上,利用OTIS(one-dimensional transport with inflow and storage)模型估算D(扩散系数)、A(渠道过水断面面积)、A_s(暂态存储区断面面积)、α(暂态存储交换系数)、λ(主流区溶质一阶吸收系数)和λ_s(暂态存储区吸收系数);并利用营养螺旋原理,计算营养盐的S_w(吸收长度)、V_f(吸收速度)和U(吸收速率)等. 结果表明:①A_s/A具有随流量减小而增大的变化特征,平均值为0.35;5次试验得到的α均处在10-3数量级水平,平均值为2.49×10-3 s-1. ②S_w-NH₄和S_w-PO₄(分别表示NH₄-N和PO₄-P的S_w,下同)均较大,最大值分别达934 020、47 518 m,意味着关镇河支渠已基本不具备氮、磷滞留能力;而S_w-NH₄和S_w-PO₄均不同程度地出现负值,表明该支渠还具有“源”的作用. ③V_f-NH₄与河水平均深度、渠道流量均呈显著负相关,V_f-PO₄和U-PO₄与渠道水面宽度均呈显著正相关. ④NH₄-N和PO₄-P的营养螺旋指标与其相应质量浓度背景值无明显相关性.      

大管径真空排水技术在雨水泵站中的应用与数值分析

针对传统雨水泵站存在的问题,介绍了大管径真空排水技术在雨水泵站应用中的独特优势及具体实施方法。为研究其排水过程中的流态分布、流体动力学性能,建立了典型管道的数值模型,采用κ-ξ紊流模型及Vof方法,对其进行了非稳态数值模拟,分析了两相流在大管径管道充水过程中的气液流动特性。结果表明:大管径排水过程中存在分层流、气泡流及波浪流,并在弯管附近出现短暂集气现象;液相在倾斜管路中有短暂流速停滞现象,随着压差的推进,最终在管道中形成液相满管流。