环氧丙烷生产工艺现状及清洁生产研究进展

对环氧丙烷生产工艺的现状及新动向进行了综述,指出与蒽醌法制Ｈ２Ｏ２内烯直接环氧化工艺是环氧丙烷清洁生产的发展方向。     

基于3G网络的无线DVR软硬件系统设计与实现

针对目前DVR(Digital Video Recorder)受软硬件捆绑和网络环境制约的不足,研究了基于软压缩的无线传输DvR系统.本文重点分析了基于H.264技术的嵌入式硬盘录像机的系统结构,并详细讨论了基于3G网络的无线嵌入式DVR软件部分各个模块的设计与实现,以及其中的关键技术,最后通过实例分析了系统的性能.     

辽河稠油热采现场硫化氢的防范与治理建议

硫化氢是一种剧毒和较强腐蚀性的气体,近年来在辽河油田一些地区相继出现,特别是稠油热采区块出现了较高浓度的硫化氢。硫化氢的存在已经威胁到油田的安全生产,并成为油气勘探开发过程中必须解决的问题。本文对辽河油气稠油热现场硫化氢的预防与治理提出了一些建议。     

SO2和H2O对Mn-Ce/TiO2催化剂低温SCR活性的影响

采用溶胶凝胶法制备Mn-Ce/TiO_2低温SCR催化剂并考察其活性,研究了SO_2和H_2O对Mn-Ce/TiO_2低温脱硝催化剂的影响,并运用XRD、BET、SEM和FT-IR对中毒前后的催化剂进行表征。结果表明,催化剂在无SO_2和H_2O条件下具有良好的脱硝性能,在140℃时NO_x去除率达到84%。但若向模拟烟气中加入SO_2和H_2O,则随其体积分数增大对催化剂活性产生明显抑制作用。当H_2O的体积分数为5%、SO_2为700×10-6时,反应4 h后,NO_x去除率降为53%。H_2O对催化剂的抑制作用随H_2O的除去而消除,H_2O主要通过与NO_x的竞争吸附来抑制催化剂的活性。低浓度的SO_2对催化剂活性影响较小,SO_2体积分数为100×10~(-6)时,稳定后NO_x去除率仍能维持在80%以上,但较高体积分数的SO_2引起的催化剂失活不可自行恢复。SO_2毒化作用主要是引起了硫酸铵盐覆盖催化剂的表面活性位,以及造成活性组分MnO_x的晶化,并破坏了MnO_x与TiO_2间的强相互作用。H_2O和SO_2共同存在时,H_2O可以弱化SO_2对催化剂的毒化作用,主要因为H_2O与SO_2的竞争吸附作用而使SO_2对催化剂活性的影响减弱。     

The humanitarian common logistic operating picture: a solution to the inter‐agency coordination challenge

Although significant progress has been made in developing the practice of humanitarian logistics, further improvements in efficiency and effectiveness have the potential to save lives and reduce suffering. This paper explores how the military/emergency services’ concept of a common operating picture (COP) can be adapted to the humanitarian logistics context, and analyses a practical and proven approach to addressing the key challenge of inter‐agency coordination and decision‐making. Successful adaptation could provide the mechanism through which predicted and actual demands, together with the location and status of material in transit, are captured, evaluated, and presented in real time as the basis for enhanced decision‐making between actors in the humanitarian supply network. Through the introduction of a humanitarian logistics COP and its linkages to national disaster management systems, local communities and countries affected by disasters and emergencies will be better placed to oversee and manage their response activities.     

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.     

Co-pyrolysis of oil sludge with hydrogen-rich plastics in a vertical stirring reactor: Kinetic analysis,emissions, and products

● Collaborative treatment of plastics and OS was established to improve oil quality. ● PE addition successfully improved OS pyrolysis process by deploying H/C_eff ratio. ● Higher H/C_eff ratio promoted cracking to obtain more gas and light oil fractions. ● The degradation of PE and OS was promoted each other under their temperature range. Pyrolysis is an effective method to treat oily sludge (OS) due to its balance between oil recovery and nonhazardous disposal. However, tank bottom OS contains a high content of heavy fractions, which creates obstacles for pyrolysis due to the high activation energy. The incomplete cracking of macromolecules and secondary polymerization decreases the oil quality and causes coking during the operation process. This study introduced polyethylene (PE) into OS to deploy the H/C_eff ratio of feedstocks for pyrolysis. A strong interaction between OS and PE during copyrolysis could be observed from the TG/DTG curves. PE tightly participated in OS degradation, while OS also promoted PE degradation at high temperature. Apparent pits were generated in solid residues from copyrolysis, which was attributed to the uniform and violent gas release. In addition to HCN, other nitrogenous and sulphurous pollutants were inhibited. Accordingly, more gas products were attained after PE addition with more value-added compositions of alkanes and alkenes. Although the oil yield decreased after PE addition, the oil products from copyrolysis possessed higher heating values and higher contents of light fractions with short chains as well as paraffins. Consequently, copyrolysis of OS and PE significantly improved the pyrolysis process and resulted in high oil quality.     

低铬油套管钢材在不同工况下的腐蚀规律研究

目的 研究低铬油套管钢材在不同腐蚀环境中的腐蚀特征。方法 采用高温高压动态反应釜对1Cr、3Cr这2种常用低铬油套管钢材进行纯CO2、CO2和低浓度H2S共存条件下的腐蚀试验。结果 温度在40~80 ℃条件下,各种钢材的腐蚀速率随着温度的升高而变大。加入低浓度H2S后,可以抑制CO2腐蚀,且随着温度升高,抑制性逐渐减弱。分析认为,在单独CO2环境以及CO2和低浓度H2S共存的环境中,1Cr、3Cr钢表面出现铬富集现象,形成的Cr(OH)3膜保护基底。同时,在CO2和低浓度H2S共存的环境中,1Cr、3Cr钢表面形成致密的FeS产物膜有助于保护基底,抵抗Cl^－侵蚀。结论 低Cr钢表面因铬的富集形成钝化膜,能有效抑制油套管的腐蚀速率,以上研究成果对CO2和低浓度H2S环境中的腐蚀理论以及油田油套管材料合理选择均有一定指导意义。     

添加H2O2加速低合金钢海水腐蚀的主要影响因素研究

采用极化曲线、旋转圆盘电极试验和失重（质量损失）法研究了低合金钢在添加了H。o：的海水中腐蚀加速的主要影响因素。结果发现低合金钢在添加H2O2的海水中腐蚀加速主要受到了H2O2浓度、温度、搅拌速度和H2O2添加周期的影响。研究表明,搅拌速度不变、H2O2添加周期相同的条件下,在H2O2浓度为0．8mol／L的70℃海水中,低合金铜的腐蚀加速最显著;在试验的转速范围内,加速作用随搅拌速度增大变得更为显著;H2O2加入后350min内加速作用较明显。     

石墨相氮化碳协同UV-H_2O_2光催化降解亚甲基蓝

以三聚氰胺为前驱体,经热解—回流法制备了石墨相氮化碳(g-C3N4),采用XRD、FTIR、SEM、EDS、PL等技术对g-C_3N_4进行了表征。研究了g-C_3N_4在UV-H_2O_2体系中对废水中亚甲基蓝(MB)的光降解效果。实验结果表明,UV+g-C_3N_4催化剂+H_2O_2体系能协同降解MB,在初始MB质量浓度为20 mg/L、初始废水p H为5、废水体积为250 mL、g-C_3N_4加入量为0.10 g、H_2O_2浓度为0.4 mmol/L、反应温度为25℃的优化工艺条件下,紫外光照射70 min时MB脱色率达98.32%。g-C_3N_4催化剂具有较好的重复使用性能,使用5次后MB脱色率仍保持在95.10%。