环境风险评价中氯气泄漏扩散的计算

根据HJ/T169-2004((建设项目环境风险评价技术导则>(简称<导则>),对某化工厂使用的液氯钢瓶的事故源进行分析.采用<导则>推荐的Cox和Carpenter稠密气体扩散模型,在氯气泄漏的初期,将其作为重气泄漏扩散进行计算,得到重气云团温度、半径、卷入空气质量和质量浓度随扩散时间的变化关系.计算结果与非重气扩散高斯模式的计算结果有较大差异.因此,对涉及氯气的项目进行环境风险评价时,应重视氯气作为重气泄漏扩散的环节.     

可见光催化剂BiVO_4 降解废水中直接耐酸大红4BS

以直接耐酸大红4BS模拟染料废水为目标污染物,研究了BiVO_4对直接耐酸大红4BS(简称4BS)的吸附效果以及废水初始质量浓度、废水pH和BiVO_4的加入量对光催化降解效果的影响.实验结果表明:当废水初始质量浓度为40 mg/L、废水pH为6.38、BiVO_4加入量为1.0 g/L时,4BS的降解率可达98.9%;BiVO_4重复使用5次后4BS的降解率可达80.0%以上;COD的变化趋势说明4BS被催化剂吸附和光催化降解的过程是循序渐进的.     

某电镀厂污泥酸浸除杂提磷试验

探讨了武汉某工业园电镀厂污泥酸浸、除杂提磷的工艺及条件。当H2SO4（浓度为72％）用量为4mL/g污泥,在液固比为5：1,常温搅拌浸出时间为1h,用碱液调节浸出液pH为4后沉淀1h,过滤,磷的浸出率为86％,铁的沉淀率达到94．2％,除铁后的浸出液进一步用NH4HCO3净化,并制取磷铵产品,总养分（N＋P2O5）为52％。产品达到国家合格品的标准。     

A failure analysis of fillet joint cracking in an oil storage tank

This paper has studied failure of an oil storage tank. During operation, several cracks were observed at the fillet weldment between reactor shell and annular plates in the bottom of oil storage tank. Extreme stresses in the structure during its operation were determined taking into account shape and geometry imperfections as well as corrosion influence. Both reactor shell and annular plates are made of carbon steel (SM53C). In this study, in order to identify the causes for the fillet weldment cracking, failure analysis such as fractography, tensile test, hardness test, corrosion test(SSRT), chemical analysis was performed. The failure of oil storage tank is the result of the combined and synergistic interaction of mechanical stress and corrosion reactions. Although cracks were initiated by corrosion, failure was generated by propagation of crack caused by stresses concentration. It was recommended that (1) the local stresses be reduced by improved weld toe geometry, and (2) the reinforcement be used in order to avoid failure by stresses concentration.     

Performance of a full-scale biofilm system retrofitted with an upflow multilayer bioreactor as a preanoxic reactor for advanced wastewater treatment

To enhance nitrogen removal in an existing microbial contact oxidation (MCO) system with a treatment capacity of 900 m3/d, an upflow multilayer bioreactor (UMBR) was chosen as a preanoxic reactor for the removal of organic matter and nitrate. The removal performance of the retrofitted plant was evaluated during the startup phase at a low temperature in winter. The high removal (>80%) of organic matter and suspended solids in the UMBR provided stable nitrification conditions in the MCO system, as a result of the substantial reduction in organic matter and solids loaded onto the MCO system. This treatment system showed a stable nitrogen removal efficiency of 75.3%, even in the low temperature range 7 to 10 degrees C. Phosphorus was completely removed by chemical precipitation. Production rates of excess sludge, as a function of the loads of influent flowrate and biological oxygen demand (BOD), were 0.022 kg dry solid/m3 wastewater and 0.132 kg dry solid/kg BOD.     

投加沸石粉活性污泥搅拌参数优化及其对离子交换速率的影响研究

在0.3 m×0.3 m×0.36 m方形搅拌槽中初步探讨了不同的搅拌器类型、安装高度以及曝气强度对投加了沸石粉的高浓度活性污泥悬浮状态的影响,并根据固液悬浮理论确定了最佳的搅拌参数.同时,进行了不同搅拌速率下沸石对污水中氨氮的离子交换动力学研究.结果表明在无曝气的情况下,选用三叶推进式搅拌器,搅拌器离底高度为1/3搅拌器直径时所需要的临界搅拌速率最低.曝气有助于反应池中污泥的悬浮,对于30 g/L的污泥,当曝气强度由10 m3/(m2·h)增大1倍时,临界搅拌速率降低了50%.搅拌速率为120 r/min时,沸石对污水中氨氮的离子交换速率受膜扩散过程控制,当其增大为180 r/min时,其控制步骤为粒内扩散,沸石粉活性污泥达到完全均匀悬浮的临界搅拌速率不足以满足传质的要求.需增大一定程度.     

再生水做景观用水使用含氯消毒剂消毒的副产物及安全性

再生水消毒后主要作为城市杂用水利用,消毒副产物及其毒性的研究非常重要.在浓度为 5～8 mg/L 的消毒剂(ClO2、HClO)量下,灭菌率能够达到 100%.2 种消毒体系均产生少量ClO2-、ClO3-和CHCl3,对检验用水生生物未产生毒性.适当的选择消毒剂浓度,控制反应条件,能够实现再生水的安全回用.     

基于电阻率的硫酸污染水泥土检测方法的探讨

电阻率法作为一种简单有效的测试方法,已在岩土工程检测中得到了一定程度的应用.通过室内试验模拟了水泥土试块受不同浓度硫酸溶液污染的反应,采用电阻率法研究了孔隙水电阻率、水泥土电阻率、结构因子与溶液浓度和龄期之间的关系.结果表明,孔隙水和水泥土电阻率随溶液浓度增大而减小、随龄期的增大而增大,结构因子随着溶液浓度和龄期的增加而增加,它们之间具有较高的相关性.这充分说明,电阻率法可应用于硫酸污染水泥土的检测和评价.     

沸石生物联合吸附再生工艺参数优化研究

简述了沸石生物联合吸附再生工艺(ZCS工艺)的工艺原理,选取了影响沸石生物联合吸附再生工艺污水处理效果的影响因素,通过正交实验,优化了工艺的运行参数.在优化结果为泥龄(SRT)40 d、沸石投加量16.8 g/L、外回流比(R)1、内回流比(r)1、A池碳源投加比(m)0、吸附池溶解氧(DO吸)1 mh/L和O池溶解氧(DOO)2 mg/L的条件下稳定运行后,出水水质达到《城镇污水处理厂污染物排放标准》(GB18918-2002)中一级B标准的要求.