气田开发过程中地下水环境保护方案初探

区域地下水环境的保护是气田开发过程中环境保护工作的重点之一。通过现场调查和统计分析得知,外部污染源是影响当地地下水环境的主要因素,农田径流污染源是外部的主要污染源,以COD_Cr计其排放量分别约占外部污染源排放总量的67%,而钻井液漏失、天然气窜层、钻井废水排放等钻井作业是内部的主要污染源,其COD_Cr排放量约占内部污染源COD_Cr排放总量的62%,因而钻井作业的污染防治应是项目内部地下水污染防治工作的重点。根据地下水环境质量现状分析及变化趋势分析可知由于气田的开发建设,气田区地下水水质已受到一定程度的影响,特征污染物表现为COD_Cr、氨氮、氯化物、硝酸盐氮。为保护气田区地下水环境,分施工期和运营期两阶段设计了地下水环境保护方案,采取源头控制的清洁生产,至末端控制的污染治理并提出了突发污染事故应急预案,为气田的可持续开发提供指导。     

顶空-气相色谱法测定水质中的丙酮和丁酮

本文建立顶空-气相色谱法测定水和废水中的丙酮和丁酮的方法,水样测定结果的相对偏差小于5.0%,加标回收率在91%～103%之间,最低检出浓度0.006 mg.L-1。该方法简便,灵敏度更高,重现性好,线性范围宽,精密度和准确度满意,尤其是避免了消耗大量有机试剂,避免二次污染。旨在为实验分析人员提供技术参考依据。     

实用环境监测气体采集器设计与应用

手持式电动气体采集器解决了传统双联球气体采集时繁琐、计量不准等诸多问题,为快速、准确地获得监测数据提供保障。     

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.