基于ANSYS的界面化核电站取水构筑物配筋程序开发

在实际工程应用中,对于结构复杂安全等级高的核电水工结构,相关的通用设计软件尚未形成。利用ANSYS二次开发工具APDL、UIDL以及Tcl/Tk可视化工具命令语言,针对核电站取水构筑物开发了一整套程序,包括了建模、计算以及后处理,后处理部分为内力计算和配筋可视化程序,简化了操作流程。算例表明,内力提取程序运算结果精度良好,可以用于配筋设计,利用配筋可视化程序对工程实例进行的配筋及裂缝验算,结果符合工程要求,针对配筋结果提出了墙体优化设计的建议。通过在ANSYS中实现内力计算和可视化配筋程序,可用于解决核电水工结构设计问题,有良好的工程适用性。     

拟除虫菊酯类农药中间体在鱼体肌肉中的积累和释放行为的研究

本文研究了8种与拟除虫菊酯合成有关的化合物在金鱼和鲤鱼肌肉中的积累和释放行为.实验结果表明,不同鱼种积累同一化合物的程度不同,其差别随着分配系数的增加而显著增加.平衡时的生物富集因子的对数log(BCF)值与分配系数的对数log P值之间有较好的线性关系,其相关方程式为log(BCF)=1.062 logP-1.558(n=8,r=0.975).化合物从鱼体释放到水中的速度符合一级反应动力学公式.释放半衰期的对数log t_(1/2)值亦与log P值相关.其相关方程式为log t_(1/2)=0.784 log P-1.571(n=8,r=0.945).本文结果有助于预测该类有机污染物对环境的影响.     

Advanced treatment of wet-spun acrylic fiber manufacturing wastewater using three-dimensional electrochemical oxidation

A three-dimensional electrochemical oxidation(3D-EC) reactor with introduction of activated carbon(AC) as particle micro-electrodes was applied for the advanced treatment of secondary wastewater effluent of a wet-spun acrylic fiber manufacturing plant. Under the optimized conditions(current density of 500 A/m~2, circulation rate of 5 mL/min, AC dosage of 50 g, and chloride concentration of 1.0 g/L), the average removal efficiencies of chemical oxygen demand(COD_(cr)), NH3–N, total organic carbon(TOC), and ultraviolet absorption at 254 nm(UV_(254)) of the 3D-EC reactor were 64.5%, 60.8%, 46.4%, and 64.8%, respectively; while the corresponding effluent concentrations of COD_(cr), NH_3–N, TOC, and UV_(254) were 76.6, 20.1, and42.5 mg/L, and 0.08 Abs/cm, respectively. The effluent concentration of COD_(cr) was less than 100 mg/L, which showed that the treated wastewater satisfied the demand of the integrated wastewater discharge standard(GB 8978-1996). The 3D-EC process remarkably improved the treatment efficiencies with synergistic effects for COD_(cr), NH_3–N, TOC, and UV_(254) during the stable stage of 44.5%, 38.8%, 27.2%, and 10.9%, respectively, as compared with the sum of the efficiencies of a two-dimensional electrochemical oxidation(2D-EC) reactor and an AC adsorption process, which was ascribed to the numerous micro-electrodes of AC in the 3D-EC reactor. Gas chromatography mass spectrometry(GC–MS) analysis revealed that electrochemical treatment did not generate more toxic organics, and it was proved that the increase in acute biotoxicity was caused primarily by the production of free chlorine.     

聚(丙烯酸-co-丙烯酰胺)/膨润土/腐植酸钠三维网络凝胶吸附剂对Cd2+吸附性能研究

制备了一种聚(丙烯酸-co-丙烯酰胺)/膨润土/腐植酸钠三维网络凝胶吸附剂,重点考察了吸附剂对Cd2+吸附的pH依赖性、吸附动力学和吸附等温线.结果表明,Cd2+溶液pH值对吸附容量有较大影响.在pH=8、吸附时间30 min、Cd2+溶液初始浓度0.02 mol/L和吸附剂用量0.10 g的条件下,吸附剂对Cd2+的饱和吸附量可达294.7 mg/g.与膨润土相比,三维网络凝胶吸附剂具有更高的吸附容量和更快的吸附速率.     

一种分离纯化降解性质粒DNA的简便方法

控制微生物对某些环境污染物降解的质粒——降解性质粒,分子量较大,难于和染色体DNA分离。超螺旋质粒DNA在热变性后冷却即快速复性方面与染色体DNA不同。根据此性质,作者改进了McMaster的和Kado的方法,获得了良好效果。实验证明。经此法纯化的质粒具有转化活性,是研究化学污染物的降解性质粒的简便方法。     

SBR处理模拟氯苯废水

在SBR中利用光合细菌球形红细菌污泥颗粒进行模拟氯苯废水处理的初步研究,结果表明,采用球形红细菌污泥颗粒处理模拟氯苯废水的SBR系统是可行的,其降解氯苯过程符合Monod一级反应动力学方程。当进水氯苯浓度在125～187.5 mg/L变化时,处理效率都能稳定在90.5%～95.6%之间;其最佳工艺条件为反应时间6 h、DO 4.75～5.0 mg/L、沉淀时间1.5 h、污泥颗粒浓度4 000～6 000 mg/L。在污泥颗粒浓度4 000 mg/L、DO 5.0 mg/L、反应时间6 h的最佳条件下,当进水COD为748.1 mg/L、氯苯浓度100 mg/L时,COD的去除率达90.9%,处理后出水COD满足国家一级排放标准要求。     

水处理用活性炭改性研究

利用锆和氯化十六烷基三甲铵共同改性活性炭,制备一种新型去除污水中硝酸盐和磷酸盐的水处理吸附剂,并考察吸附剂加量、反应温度、pH值、共存阴离子等影响因素对吸附效果的影响。结果表明:锆-氯化十六烷基三甲铵改性活性炭(Zr-CTAC-AC)吸附剂适用于硝酸盐和磷酸盐浓度在100mg/L以下的污水,随着Zr-CTAC-AC加量的增加,硝酸盐、磷酸盐去除率逐渐增加,单位吸附量逐渐下降,Zr-CTAC-AC加量为8g/L时,硝酸盐去除率为79%,Zr-CTAC-AC加量为4.0g/L时,磷酸盐去除率可达91%,但应在较低的pH值范围内使用;反应温度对Zr-CTAC-AC的吸附效果影响不大;共存Cl-、HCO3^-和SO4^2-可使硝酸盐的吸附率降低,但对磷酸盐吸附率影响较小;1mol/L NaCl溶液可使吸附到Zr-CTAC-AC表面的硝酸盐90.9%左右被解吸出来,1mol/L NaOH溶液可使吸附到Zr-CTAC-AC表面的磷酸盐78.4%左右被解吸出来。Zr-CTAC-AC能够有效去除污水中硝酸盐和磷酸盐,制备方法简单,且可循环利用,处理成本低。     

电子废弃物中持久性有机污染物分析检测方法的研究进展

针对目前电子废弃物中持久性有机污染物(POPs)尚未形成有效快速分析检测方法的问题,介绍了溶剂萃取、固相萃取、微波萃取和超临界流体萃取等POPs前处理技术的研究进展,总结了POPs的分析方法,如:气相色谱、液相色谱、气相色谱-质谱法、高分辨率气相色谱-高分辨质谱法等化学分析方法,以及生物传感器测定法、表面胞质团共振检测法、酶联免疫检测法等生物分析方法。分析了各方法的优劣,并提出了展望。     

鲤鱼对2,6-二硝基甲苯的生物浓缩、消除与代谢研究

 以鲤鱼为实验生物，应用流动式摄取及释放装置，进行了2，6－二硝基甲苯（2，6－DNT）的生物浓缩与释放研究。取得了2，6－DNT在鲤鱼（全鱼）、肝及肠部的生物浓缩曲线。全鱼的浓缩曲线可以稳态（平台式）曲线描述，但是肝、肠部浓缩曲线均呈峰形。肝部峰快速下降后渐趋稳态，肠部峰下降未得稳态。峰形，肝在先，肠在后。对比2，6－DNT在全鱼及肝、肠的生物浓缩曲线，并参照报道_（1，2）指出，全鱼摄取曲线上各点所表现的浓度值为各时刻鱼体内各组织摄取化学品总重对全鱼重量的比值。肝、肠部峰形曲线预示了在肝、肠内生物浓缩过程发生了生物转化作用。对全鱼的生物浓缩过程应用单区一级动力学模型，求得BCF值与消除速率常数K₁与K₂，由K₁/K₂计算得到的BCF值与实测值相符。释放较慢，释放曲线呈双曲线形，半减期为4.8h。     

Molecular characterization of effluent organic matter in secondary effluent and reclaimed water: Comparison to natural organic matter in source water

Municipal wastewater reclamation is becoming of increasing importance in the world to solve the problem of water scarcity. A better understanding of the molecular composition of effluent organic matter(Ef OM) in the treated effluents of municipal wastewater treatment plants(WWTPs) is crucial for ensuring the safety of water reuse. In this study, the molecular composition of Ef OM in the secondary effluent of a WWTP in Beijing and the reclaimed water further treated with a coagulation–sedimentation–ozonation process were characterized using a non-target Fourier transform ion cyclotron resonance mass spectrometry(FT-ICR MS) method and compared to that of natural organic matter(NOM) in the local source water from a reservoir. It was found that the molecular composition of Ef OM in the secondary effluent and reclaimed water was dominated by CHOS formulas, while NOM in the source water was dominated by CHO formulas. The CHO formulas of the three samples had similar origins. Anthropogenic surfactants were responsible for the CHOS formulas in Ef OM of the secondary effluent and were not well removed by the coagulation-sedimentation-ozonation treatment process adopted.