城市污水厂污泥催化热水解制备聚合氯化铝铁

采用催化热水解分离城市污水厂污泥中的有机物和无机物,并将无机物制备成了聚合氯化铝铁。研究结果表明:在盐酸质量浓度为20%,反应时间为2 h,反应温度为90℃,固液比1∶3条件下,制备的液体聚合氯化铝铁的Al_2O_3含量为9.34%,Fe_2O_3含量为2.11%,盐基度为47.8%;制备的产品在城市污水处理中取得了较好处理效果。同时采用红外光谱(IR)技术对制备的聚合氯化铝铁的聚合形态进行表征。     

水中氯离子的测定方法及其研究进展

离子是水体中常见的阴离子之一,其含量的测定是水质监测的一项重要指标.其浓度过高会使水质变差、危害身体健康、妨碍植物生长、腐蚀管道和设备.随着环境及环保法规要求的日益严格,水中氯离子的测定也越来越受到重视.综述了近年来水中氯离子的测定方法,主要包括滴定法、离子色谱法、分光光度法、电位滴定法、浊度法.介绍了上述方法的测定原理、特点、应用,并对各种方法进行了对比分析.     

桂南地下热水系统中氟的分布及迁移富集规律

选取广西桂南地区地下热水系统为研究对象,利用氢氧同位素及锶同位素研究手段,对研究区内地下热水中氟的空间分布规律及其控制因素进行研究。结果表明:研究区内地下热水中氟含量变化范围为0.01~17.93mg/L,其中43%地下水样品中氟含量超过饮用水氟骨症临界值1.5mg/L,高氟地下热水的主要水化学类型为Na-HCO3型,水体中氟含量与温度呈明显正相关性;地下热水氢氧同位素特征显示,研究区地下热水的主要来源为大气降水,同时受一定程度蒸发浓缩及水-岩作用影响,地下热水锶同位素特征显示,研究区地下热水水化学组成明显受长石、云母等铝硅酸盐风化及碳酸盐岩溶解影响;对地下热水水化学开展的因子分析结果显示,研究区地下热水系统中影响氟迁移释放的主要因素为萤石的溶解与沉淀过程。     

过氧化氢除藻及相关环境条件优化

采用室内培养的方式,通过正交试验研究了H_2O_2质量浓度、光照、pH值和温度4个因素复合作用对铜绿微囊藻去除的影响。结果表明,在所设置的各因素梯度范围内,对去除铜绿微囊藻影响最大的因素是H_2O_2质量浓度;光照和pH值对藻细胞数和叶绿素a的去除,以及H_2O_2残留量的影响各不相同;温度对藻细胞数的影响最小,对H_2O_2残留量的影响较小,对叶绿素a质量浓度的影响较大。除藻的最佳组合为A_1B_2C_3D_2,即光照为1 500 lx,H_2O_2质量浓度为50mg/L,pH值为8.5,温度为25℃。     

The use of ionic liquids based on choline chloride for metal deposition: A green alternative?

Ionic liquids are studied intensively for different applications. They tend to be denoted as “green solvents”, largely because of their low vapour pressure. In recent years toxicity and biotoxicity of ionic liquids have also been investigated, which proved that not all of these are “green”. In this paper the use of ionic liquids based on choline chloride and ethylene glycol in electrochemistry is discussed in the context of their use as green solvents. Due to their low toxicity and ready biodegradability, these deep eutectic solvents are promising for the electrodeposition of metals. The influence of the use of these liquids as metal deposition baths on the waste water is investigated. Drag-out was found to be the most influencing parameter on the environmental impact of the process, as it is three times higher compared to classical solutions due to the higher viscosity of the ionic liquid. There are no major changes needed in the rinsing configuration of classic electroplating plants, and ion exchange to remove the metal out of the waste water was not hindered by the presence of the ionic liquid. The formation of by-products during the deposition of metals has to be further investigated and evaluated in consideration of the environmental impact.     

Endogenous formation of hydrogen cyanide during distillation for the determination of total cyanide

This paper describes how organic compounds and nitrogen compounds induce the formation of hydrogen cyanide during the distillation process. Hydrogen cyanide formation was confirmed by X‐ray diffraction. The formation scheme for hydrogen cyanide from organic compounds is proposed.     

化工生产中硫化氢泄漏事故的预防和处置对策

通过发生在昆明市安宁齐天化肥有限公司的硫化氢中毒事故,提出硫化氢泄漏事故的预防措施及相应的处置方法,同时总结经验教训,提出整改措施,以避免类似事故的再次发生.     

Biogeochemistry of two types of permeable reactive barriers, organic carbon and iron-bearing organic carbon for mine drainage treatment: Column experiments

Permeable reactive barriers (PRBs) are an alternative technology to treat mine drainage containing sulfate and heavy metals. Two column experiments were conducted to assess the suitability of an organic carbon (OC) based reactive mixture and an Fe⁰-bearing organic carbon (FeOC) based reactive mixture, under controlled groundwater flow conditions. The organic carbon mixture contains about 30% (volume) organic carbon (composted leaf mulch) and 70% (volume) sand and gravel. The Fe⁰-bearing organic carbon mixture contains 10% (volume) zero-valent iron, 20% (volume) organic carbon, 10% (volume) limestone, and 60% (volume) sand and gravel. Simulated groundwater containing 380 ppm sulfate, 5 ppm As, and 0.5 ppm Sb was passed through the columns at flow rates of 64 (the OC column) and 62 (the FeOC column) ml d^− 1, which are equivalent to 0.79 (the OC column) and 0.78 (the FeOC column) pore volumes (PVs) per week or 0.046 m d^− 1 for both columns. The OC column showed an initial sulfate reduction rate of 0.4 µmol g (OC)^− 1 d^− 1 and exhausted its capacity to promote sulfate reduction after 30 PVs, or 9 months of flow. The FeOC column sustained a relatively constant sulfate reduction rate of 0.9 µmol g (OC)^− 1 d^− 1 for at least 65 PVs (17 months). In the FeOC column, the δ³⁴S values increase with the decreasing sulfate concentration. The δ³⁴S fractionation follows a Rayleigh fractionation model with an enrichment factor of 21.6‰. The performance decline of the OC column was caused by the depletion of substrate or electron donor. The cathodic production of H₂ by anaerobic corrosion of Fe probably sustained a higher level of SRB activity in the FeOC column. These results suggest that zero-valent iron can be used to provide an electron donor in sulfate reducing PRBs. A sharp increase in the δ¹³C value of the dissolved inorganic carbon and a decrease in the concentration of HCO₃⁻ indicate that hydrogenotrophic methanogenesis is occurring in the first 15 cm of the FeOC column.     

Are calcareous soils in uplands less prone to damage from road salting than acidic soils?

Previous studies of upland roadside soils in Cumbria, that would normally be naturally acidic, have highlighted that (a) runoff from roads subjected to long-term road salting can dramatically raise soil pH down slope in upland areas; (b) the soil pH increase dramatically changes N cycling in soils down slope, increasing mineralisation of organic matter, ammonification, ammonium leaching down slope and nitrification and nitrate leaching; (c) the increase in nitrification substantially increases nitrate leaching to down-slope rivers, and this is readily detectable in field studies; and (d) loss of soil organic matter over decades of salting is so great that organic matter is no longer substantially solubilised by high salt concentrations found in soil solution below road drains. This paper tests and supports the hypothesis that such effects are minimal for more calcareous soil ecosystems. It examines the soil and soil solution chemistry on another Cumbrian upland highway, the A686 near Leadgate, Alston. Sodium % of soil CEC values for soil transects affected by spray containing road salt are similar at both the A6 and A686 sites. However, spatial trends in calcium, magnesium, ammonium, and nitrate concentrations as well as pH differ, as a direct result of the higher weathering rate of parent material and possibly also the presence of limestone walls above both spray-affected and control transects at the A686 site.     

High efficiency chlorine removal from polyvinyl chloride (PVC) pyrolysis with a gas–liquid fluidized bed reactor

In this research a gas–liquid fluidized bed reactor was developed for removing chlorine (Cl) from polyvinyl chloride (PVC) to favor its pyrolysis treatment. In order to efficiently remove Cl within a limited time before extensive generation of hydrocarbon products, the gas–liquid fluidized bed reactor was running at 280–320 °C, where hot N₂ was used as fluidizing gas to fluidize the molten polymer, letting the molten polymer contact well with N₂ to release Cl in form of HCl. Experimental results showed that dechlorination efficiency is mainly temperature dependent and 300 °C is a proper reaction temperature for efficient dechlorination within a limited time duration and for prevention of extensive pyrolysis; under this temperature 99.5% of Cl removal efficiency can be obtained within reaction time around 1 min after melting is completed as the flow rate of N₂ gas was set around 0.47–0.85 Nm³ kg^?1 for the molten PVC. Larger N₂ flow rate and additives in PVC would enhance HCl release but did not change the final dechlorination efficiency; and excessive N₂ flow rate should be avoided for prevention of polymer entrainment. HCl is emitted from PVC granules or scraps at the mean time they started to melt and the melting stage should be taken into consideration when design the gas–liquid fluidized bed reactor for dechlorination.