Destruction of 4-phenolsulfonic acid in water by anodic contact glow discharge electrolysis

Destruction of 4-phenolsulfonic acid (4-PSA) in water was carried out using anodic contact glow discharge electrolysis. Accompanying the decay of 4-PSA, the amount of total organic carbon (TOC) in water correspondingly decreased, while the sulfonate group of 4- PSA was released as sulfate ion. Oxalate and formate were obtained as minor by-products. Additionally, phenol, 1,4-hydroquinone, hydroxyquinol and 1,4-benzoquinone were detected as primary intermediates in the initial stages of decomposition of 4-PSA. A reaction pathway involving successive attacks of hydroxyl and hydrogen radicals was assumed on the basis of the observed products and kinetics. It was revealed that the decay of both 4-PSA and TOC obeyed a first-order rate law. The effects of different Fe ions and initial concentrations of 4-PSA on the degradation rate were investigated. It was found that the presence of Fe ions could increase the degradation rate of 4-PSA, while initial concentrations lower than 80 mmol/L had no significant effect on kinetic behaviour. The disappearance rate of 4-PSA was significantly affected by pH.     

Photocatalytic degradation of C. I. Reactive Red 24 solution with K6SiW11O39SnII

Environmental friendly materials, K₆SiW₁₁O₃₉Sn (SiWSn), was synthesized. SiWSn photocatalytic decomposition of C. I. Reactive Red 24 (RR24) with the UV-lamp (253.7 nm, 20 W), Xenon lamp filtered less than 390 nm light (500 W) and sun light was investigated. The results showed that RR24 solution could be effectively decolorized with the SiWSn photocatalyst. The photocatalytic degradation efficiency of RR24 with SiWSn was affected by the initial concentration of RR2 solution, the amount of SiWSn and the photolysis time. It is demonstrated that the process of photodegradation of RR24 with SiWSn is a pesudo first-order reaction, which can be described by Langmuir-Hinshelwood equation. Hydroxyl radicals and holes are both the main oxidants in the photocatalytic reaction of RR24 with SiWSn.     

针铁矿/H_2O_2体系对染料橙黄Ⅱ光化学脱色的实验研究

以针铁矿(α-FeOOH)为光催化剂,在金属卤灯(λ≥365 nm)照射下,对α-FeOOH与H2O2组成的非均相Fenton体系内橙黄Ⅱ的脱色进行了研究。考察了初始pH值、α-FeOOH用量、H2O2浓度和反应时间对橙黄Ⅱ脱色过程的影响。结果表明,在α-FeOOH用量为0.3 g/L,H2O2浓度为6 mmol/L,pH 3.0时,橙黄Ⅱ的脱色效果最好,光照90 min后脱色率达到99.4%。橙黄Ⅱ的光降解反应动力学符合Langmuir-Hinshelwood(L-H)动力学方程。对不同时间溶液中的总有机碳(TOC)监测,结果表明体系中橙黄Ⅱ的矿化率较低,通过对溶液中铁(Fe2+和总铁)溶出的测定,说明可能的反应涉及针铁矿表面的铁循环。     

污泥焚烧残渣水热合成NaPl型沸石和水钙沸石的性质研究

本文以污泥焚烧残渣为原料,以传统水热合成方法制得NaPl型沸石和水钙沸石,并对其相关指标进行表征．经x射线衍射、扫描电镜和红外光谱测定表明,制得的产物为无其它杂晶生成的NaPl型沸石和水钙沸石,且具有放射束片状晶体形貌和沸石骨架结构．与原污泥焚烧残渣相比,合成沸石的比表面积和阳离子交换容量提高了47倍、17倍,分别达到...     

基于阻尼器反力墙体系的特大型LNG储罐控制研究

特大型液化天然气(LNG)储罐的固有频率通常介于2～10Hz之间,处于大部分地震运动的频率范围之内.在过去的几十年中,许多事故已经证明,储罐在地震作用下很容易遭破坏.使用隔震支座来减少储罐的地震作用已经被证明是非常有效的,但对于特大型LNG储罐,其连接组件对隔震层层问位移有严格限制,尤其是在软土场地中,桩水平抗力与隔震...     

膜生物反应器脱氮除碳环境的研究

利用膜生物反应器研究垃圾填埋场垃圾渗滤运行环境,在常温环境下,运行结果表明：膜能够截留大量并使世代时间长的硝化菌在最短的时间富集成为优势菌种,对垃圾渗滤液中氨氮具有高效的去除效率;氨氮负荷0.082~0.109gN/gMLSS.d,CODC r负荷0.136~0.192g CODC r/gMLSS.d,DO 2.0~3.5mg/L,脱除氨氮的效果较好,去除率在95%~98%,CODC r去除率60%~70%。     

某恒温间歇反应的热失控研究

为得到某恒温间歇反应冷却系统临界温度Tc并评估该反应体系的热危险性,基于间歇反应体系热参数的敏感性,探讨数值计算方法和选用4种反应热失控临界判据得到的不同Tc值。结果表明,数值计算方法得到了反应体系的Tc为31.7℃,Semenov判据、Sliding判据、Da/St判据得到的Tc值分别为10℃,17℃和27℃;无量纲绝热温升B给出的结论是,在允许的工艺温度范围内,该反应对任意的冷却系统温度都处于难以控制状态。数值计算方法及各判据得到的Tc的较大差异性说明各方法均有一定的局限性。在运用参数敏感性分析的基础上,结合风险矩阵图方法对系统冷却失效的热危险性进行评估,得到不同Tc下风险可接受、有条件接受及不可接受对应的参数范围的物料累积度Xac与最大反应速率到达时间θ间的关系。     

真实条件下长时间作业的驾驶安全性影响研究

为研究长时间单调驾驶对驾驶员疲劳、嗜睡、反应时间和驾驶速度的确切影响,以合作企业3系重卡为操作对象进行了一组真实驾驶条件试验。在自愿的基础上随机地从合作企业物流公司选择12名经验丰富的驾驶员作为试验的驾驶员样本。试验采用主观评分方法记录试验者的嗜睡和疲劳状况,所有数据分析基于统计学软件PASW Statistic 18.0。试验结果表明长时间单调驾驶会导致驾驶员疲劳和嗜睡,而疲劳和嗜睡在一定的程度上会导致驾驶速度的加快,却没有导致驾驶员反应时间的显著变化。在持续驾驶3 h之后驾驶员的疲劳和驾驶绩效发生了明显劣化,故从安全的角度考虑应以2~3 h为界合理安排司机的作业负荷和绩效考评。     

Hybrid microbial electrolytic/UV system for highly efficient organic pollutants removal

This study for the first time proposed an efficient microbial electrolyte/UV system for Methyl Orange decomposition. With an external applied voltage of 0.2 V and cathode aeration of20 mL/min, H_2O_2 could be in-situ generated from two-electron reduction of oxygen in cathode, reaching to 8.1 mg/L in 2 hr and continued to increase. The pollutant removal efficiency of approximate 94.7% was achieved at initial neutral pH, with the activation of ·OH in the presence of UV illumination. Although the nature of its guiding principles remain on the vista of practical exploration, this proof-of-concept study provides an alternative operation pattern of solar–microbial hybrid technology for future wastewater treatment from a basic but multidisciplinary view.     

响应面法优化Fenton预处理精细化工废水

甘肃省某精细化工企业实际生产废水成分复杂、有机物含量高、可生化性差,为满足后续生化工艺需求,急需开展适宜的预处理技术研究.采用Fenton氧化工艺对该企业废水进行预处理,在单因素试验基础上,以初始pH、H₂O₂投加量、n（H₂O₂）:n（Fe2+）、反应时间为考察因素,COD_Cr去除效果为响应值,构建响应曲面模型,分析4个独立因素及各因素之间的交互作用对COD_Cr去除效果的影响;同时,对反应过程进行表观反应动力学分析,采用紫外光谱及傅立叶变换红外光谱分析废水有机物结构变化,探究该反应过程机理.结果表明:①废水预处理的最佳工艺条件为初始pH 4、H₂O₂投加量8 mL/L、n（H₂O₂）:n（Fe2+）12、反应时间88 min,废水COD_Cr去除率达30.15%;模型的实际运行结果与预测值接近,模型可靠.②Fenton氧化降解该精细化工废水中有机物途径复杂,难以通过单一的底物模型进行拟合.③Fenton氧化能有效降解废水中不饱和有机物,但出水中仍含有酰胺类、不饱和醛类和芳香类化合物.研究显示,Fenton预处理能有效降解废水中难降解有机物,但出水仍未达到后续生化处理要求,还需进一步优化或与其他预处理工艺组合.