火焰原子吸收法测定地表水中钾钠钙镁的方法改进

用空气—乙炔火焰原子吸收测定地表水中钾钠钙镁时,将测钾钠用的消电离剂和测钙镁用的释放剂配成混合溶液,加入待测试样中,便可连续测定其中的钾钠钙镁。与现在常用的火焰原子吸收方法测得的结果一致,精密度和准确度符合规范要求,且方法简单快速。     

亚甲蓝分光光度法测定水体阴离子表面活性剂方法的探讨

LAS是地表水和地下水水质的必测项目,国标（GB7494—87）方法操作复杂,要重复萃取四次后再洗涤,有机溶剂消耗量大,而且相当的耗时,本文通过同步实验对比与分析,得出：一次性加入20mL氯仿萃取加洗涤的方法其测定结果较好,而且极大地减轻了氯仿对分析人员身体的损害程度。测定结果有较好的精密度和准确度。本方法具有可观的经济性、安全性和可操作性。     

气相色谱法测定水中的三氯乙醛

建立了一种用气相色谱法测定水体中三氯乙醛的方法。水样先以石油醚萃取,除去高沸点化合物,加入氯化钠破乳,然后再用石油醚—乙醚混合溶剂(V/V=2:1)萃取3次,萃取液经色谱柱分离,用电子捕获检测器检测。最低检出浓度可达0.008 mg/L,线性关系良好(相关系数γ=0.992~0.998),一般共存物质不干扰测定。     

两种新型涂铁改性砂的过滤性能及反冲洗条件研究

以两种新型涂铁改性石英砂(纳米氧化铁改性砂,Nano-OCS;氧化铁改性砂,IOCS)及普通石英砂(RQS)为研究对象,考察了两种新型改性砂对沉后水腐殖酸及浊度的直接过滤效果,对其反冲洗条件进行优化研究,并对3种滤料的过滤效果进行了比较.结果表明,1滤层厚度为45 cm时,最佳滤速为6 m·h-1;3种滤料对腐殖酸和浊度的直接过滤效果依次为:Nano-OCSIOCSRQS,其中两种涂铁砂对腐殖酸的去除率分别为71.70%和61.61%;2Nano-OCS和IOCS滤柱的反冲洗流程分4步,对应的流程及最佳操作条件为:首先,用0.5 mol·L-1NaOH的溶液浸泡,气冲强度13 L·s-1·m-2,气冲时间6 min;然后,用0.075 mol·L-1的NaOH溶液与空气同时反冲洗,NaOH溶液冲洗强度为8 L·s-1·m-2,气冲强度13 L·s-1·m-2,冲洗时间3 min;接着用0.015 mol·L-1的FeCl3溶液与空气同时反冲洗,FeCl3溶液冲洗强度为8 L·s-1·m-2,气冲强度13L·s-1·m-2,冲洗时间2 min;最后,用清水冲洗,冲洗强度8 L·s-1·m-2,冲洗时间4 min.两种涂铁砂反冲洗前后表面形态结构更加复杂、粗糙度增加,对腐殖酸去除率进一步提高.3当滤层厚度由45 cm增加到80 cm时,Nano-OCS对腐殖酸直接过滤的最高去除率由74.6%提高至80.3%,平均去除率由57.9%提高至68.5%.     

K_2Cr_2O_7法和紫外分光光度法测定污水COD的对比研究

分别利用重铬酸钾法、重铬酸钾紫外分光光度法和紫外分光光度法测定污水的COD极差分别为2.43mg/L、1.19 mg/L和4.72 mg/L,RE%分别为0.84%、0.53%和1.36%,重铬酸钾紫外分光光度法和紫外分光光度法的线性范围分别在0~280 mg/L和0~400 mg/L.结果表明:重铬酸钾紫外分光光度法测定的准确度和精密度最高,简化了用标准溶液进行标定的步骤,缩短了实验时间;紫外分光光度法测定的结果准确度和精密度相对差一些,但是快速、操作简单、节省试剂,为广大环境工作者提供借鉴参考的实例。     

亚甲基蓝分光光度法测定废水硫化物的不确定度评定研究

分析了应用亚甲基蓝分光光度(GB/T16489-1996)测定废水硫化物测试过程中不确定度影响因素,主要来源为硫化物标准溶液、标准曲线拟合、随机效应、分光光度计和取样体积这五部分。本测量合成相对标准不确定度0.025 9;其中由测定样品质量引入的不确定度为0.024 7;由样品体积引入的不确定度为0.007 7。本次废水中硫化物测量结果为:0.110±0.006 mg/L,k=2(包含概率约为95%)。     

植物的非传统稳定同位素前处理及测定技术研究进展

一直以来植物都是多领域的研究重点,随着非传统稳定同位素的不断发展,植物非传统稳定同位素研究日益增加。但因植物样品中有机物含量高,同位素分馏复杂,样品前处理及测定中存在诸多难题。本文对植物样品非传统稳定同位素工作中常用的前处理方法和测定技术进行了总结。综述了直接萃取法、湿法消解和高温灰化法的原理、操作和优缺点;以K、Ca、Mg、Fe、B等典型非传统稳定同位素为例介绍了非传统稳定同位素常用测定技术,旨在为植物样品的非传统稳定同位素测定进行梳理,最后对其应用方向和测试方法的发展方向进行了展望。     

A study on the factor market distortion and the carbon emission scale effect of two-way FDI

Based on the data of 30 Chinese provinces for the period from 2004 to 2015, this paper expounds the carbon emissions effect of two-way foreign direct investment (FDI) from the perspective of scale effect and factor market distortions. This study uses Kaya identity to decompose carbon emission and construct simultaneous equations model to empirically examine the factor market distortion and the carbon emission scale effect of two-way FDI. The results show that the inward foreign direct investment (IFDI) increase regional carbon emission through scale effect and also exacerbates factor market distortion in China, whereas the outward FDI trends reduce carbon emission and reduces factor market distortions in China. The study also shows that human capital, research and development (R&D), trade openness, and capital accumulation are important determinants of two-way FDI. Therefore, the study proposes that IFDI policies should focus on acquiring green technologies. In addition, the domestic enterprises should be encouraged to participate in global business.     

阳离子型聚合物对低温低浊水的絮凝效果与形态学特性

采用微絮凝-深床直接过滤工艺,以西安市曲江水厂低温低浊水质为原水(水温低于10 ℃,初始浊度低于10NTU),投加阳离子型聚合物(简称CP)作主混凝剂或助凝剂,借助分形数学理论与图像分析技术,对滤料粒径、原水浊度、原水温度、药剂种类、聚合物分子量及投加量、混合强度等因素对处理效果的影响进行了研究,分析探讨了不同药剂处理低温低浊水的作用机理、絮凝形态学特征以及絮体结构的分形特性.结果表明,①当温度低于4 ℃、初始浊度小于4NTU时,不宜单独采用Al2(SO4)3或PAC作为絮凝剂;当温度为4～10 ℃、初始浊度小于10NTU时,如果只投加Al2(SO4)3或PAC作为絮凝剂,宜用细砂滤料过滤;低温低浊条件下,无机混凝剂形成的絮体粒径小、结构松散脆弱、有效质量密度低、沉速慢,但表征絮体分形特性的分维值较高.②CP作絮凝剂能显著改善低温低浊水的絮凝效果与过滤性能,但混合强度需增大,宜用粗砂滤料过滤;③单独用CP作絮凝剂时,宜投加分子量较低的弱阳性聚合物或投加低剂量较高分子量的强阳性聚合物;CP用作助凝剂时,能显著减少主混凝剂用量,但宜投加强阳性聚合物或增加弱阳性聚合物的剂量.④CP兼备电性中和与吸附架桥絮凝作用,能形成粒径较大、吸附性能与过滤性能良好的网状絮体构型,其有效质量密度高,产生的污泥量少,污泥沉降速度快,脱水效果好,但分维值低.⑤各种水处理药剂的处理效果为:Al2(SO4)3(或PAC) CP＞CP＞PAC＞Al2(SO4)3,这种差别由絮体的形态学特性与构型特征各异引起.     

A real-time simulating non-isothermal mathematical model for the passive feed direct methanol fuel cell

In order to understand the complex transport phenomena in a passive direct methanol fuel cell (DMFC), a theoretical model is essential. The analytical model provides a computationally efficient framework with a clear physical meaning. For this, a non-isothermal, analytical model for the passive DMFC has been developed in this study. The model considers the coupled heat and mass transport along with electrochemical reactions. The model is successfully validated with the experimental data. The model accurately describes the various species transport phenomena including methanol crossover and water crossover, heat transport phenomena, and efficiencies related to the passive DMFC. It suggests that the maximum real efficiency can be achieved by running the cell at low methanol feed concentration and moderate current density. The model also accurately predicts the effect of various operating and geometrical parameters on the cell performance such as methanol feed concentration, surrounding temperature, and polymer electrolyte membrane thickness. The model predictions are in accordance with the findings of the other researchers. The model is rapidly implementable and can be used in real-time simulation and control of the passive DMFC. This comprehensive model can be used for diagnostic purpose as well.