原子吸收分光光度法测定水中铅的不确定度评定

对GB/T 7475-1987《水质铜、铅、锌、镉的测定》〔1〕原子吸收分光光度法测定水中铅的测量不确定度进行了评定。通过测量重复性、滴定管、移液管、标准溶液浓度等影响测量结果的不确定度分量的分析和量化,求得水中铅测定结果的相对合成标准不确定度。     

新型机械澄清池设备的设计及在尾矿水处理中的应用

国内现有的机械加速澄清池因池体及设备结构的原因,存在刮泥耙直径小、驱动扭矩低,高负荷时排泥差等问题,不能满足用户对设备大池径（大于Ф29m）、大处理量、高效澄清、多用途的要求。介绍了新型澄清池设备的工艺、结构设计及特点。新型机械澄清池设备通过对池体结构的改进设计,及对刮泥机、提升搅拌机、排泥防堵搅拌机三者同心套装结构,扭矩可达百万牛顿米的带齿回转支承及多组电机同步驱动的刮泥耙驱动机构,池周边增设斜板及集水装置等方面的设计,实现了池径大于qb29in机械澄清池的设计制造,填补了国内该项目的空白,经矿山尾矿水处理实际应用证明效果理想。     

环境地表γ计量率、工频电磁场和射频电场监测实验结果对比分析研究

本文通过两实验室针对环境地表γ计量率、工频电磁场和射频电场仪器对比实验,并对结果进行了统计检验。分析结果表明,两者监测数据无显著差异。     

建筑陶瓷碳计量与优化模型研究

采用投入产出分析方法和目标规划方法,以某建陶企业为代表,建立了建筑陶瓷产业投入产出模型及低碳优化模型,利用投入产出模型计量和预估了建筑陶瓷产业关键环节碳排放和产品碳足迹;应用低碳优化模型对建筑陶瓷企业的产品计划进行了低碳优化.结果表明,建筑陶瓷企业年二氧化碳排放量达182 543.9 t,单位产品碳排放量多于国外先进水平10%以上;影响建筑陶瓷产业二氧化碳排放的关键环节为烧成和喷雾干燥过程,烧成和喷雾干燥过程排放的二氧化碳占总排放的80%以上;3种建筑陶瓷产品中,坯砖、抛光砖、釉面砖的万平米产量碳足迹依次为150.2、168.0、159.6 t.建筑陶瓷企业经低碳模型优化后可以在保证同样利润的同时降低5.4%的碳排放,也可以在保证碳排放相同的条件下使利润提高5.6%.     

黄河口无机碳输运过程对pH异常增高现象的响应

为研究黄河无机碳的输运过程及有效入海通量,通过对2004年至2006年黄河口汛期和非汛期淡水-海水混合过程中无机碳参数、溶解氧饱和度、叶绿素和NH⁺₄、 PO^3-₄的分析得出,黄河口低盐度区pH出现相对于淡水端异常增高现象,而恰在此区域DIC出现亏损现象,黄河口淡-咸水混合区域pH异常增高现象可以表征无机碳的沉降作用.淡咸水混合初期生物好氧呼吸作用的降低能够导致p_CO2的迅速降低是造成低盐度区pH出现相对于淡水端异常增高现象的主要原因.根据河口溶解物质的保守混合模型,发现混合过程中ΔDIC与ΔTA是1∶1的关系,表明DIC出现亏损是由于HCO^-₃清除造成的,汛期和非汛期黄河口无机碳的沉降作用能够清除输入到河口DIC总量的10%,即黄河口每年可清除1.21×10⁵ t河流输入的溶解无机碳,DIC的有效入海通量约为10.86×10⁵ t,通过评估,黄河流域风化作用吸收的大气CO₂量将有10%左右被河口无机碳沉降作用重新释放到大气中,而流域风化作用固定的CO₂在河口将有2.24×10⁵ t（以CO₂计）重新释放到大气中.     

沈阳市降雪中PFOS和PFOA污染现状调查

通过调查降雪中PFOS和PFOA的浓度,阐明了沈阳市大气中PFOS和PFOA的污染状况和污染规律.2006-02-06采集沈阳市区和郊区共计36个采样点的降雪样品,2006-02-25在其中5个采样点再次采集降雪样品.固相萃取融雪水中的PFOS和PFOA,利用LC-MS-SIM法测定样品中PFOS和PFOA浓度.全部样品中均检出PFOS和PFOA.2006-02-06降雪中PFOS和PFOA的浓度几何平均值分别为2.0 ng·L^-1（范围：0.4～46.2 ng·L^-1）和3.6 ng·L^-1（范围：1.6～22.4 ng·L^-1）,95%置信区间分别为1.5～2.8 ng·L^-1和3.1～4.2 ng·L^-1.PFOS和PFOA的最高浓度同时出现在郊区采样点朱尔屯,市中心区2种物质的浓度呈显著正相关.2006-02-25的5个采样点降雪中PFOS和PFOA的浓度几何平均值均为2.2 ng·L^-1.2次降雪中PFOS浓度差异不显著,2006-02-25降雪中PFOA浓度高于2006-02-06.结果表明,沈阳市区和郊区降雪中广泛存在PFOS和PFOA污染,局部区域可能存在共同的PFOS和PFOA污染来源;沈阳地区有较稳定的PFOS来源持续向大气中输送该类物质;PFOS和PFOA的环境行为可能不同.     

华北地区1951-2009年气温、降水变化特征

基于华北五省(市)64个基本气象站的1961-2009年逐年逐月气温、降水资料, 利用泰森权重计算了华北地区面平均降水及面平均气温,并建立了7个长序列气象站的气温、降水与面平均值的回归方程,展延了研究区1951-1960年面平均降水和气温资料。对展延后的1951-2009年序列数据,应用Mann-Kendall检验、Mann-Whitney检验、9 a滑动平均等方法进行趋势分析,分析结果显示: 该区59 a间年气温上升了1.5 ℃,年气温序列存在显著上升趋势,年气温序列在1993年前后有一个突变点,年气温距平以1989年为低温期与高温期的分界线,年气温平均每10 a增长2.2%;年降水序列无显著趋势,亦无显著跳跃趋势,年降水距平大致以1976年为多雨期与少雨期的分界线,年降水平均每10 a增长-1.3%。研究成果为深入分析华北地区气候变化规律、未来气候变化影响,以及水资源对气候变化的响应提供了基础。     

化学沉淀法处理线路板厂络合铜废水实验研究

为解决某线路板厂络合铜废水达标排放的问题,模拟该厂络合铜废水处理的工艺条件,采用硫酸亚铁和硫化钠相结合的化学沉淀法进行小试,通过正交实验确定最佳药剂投加量.结果表明,影响络合铜废水处理效果的各因素的重要性顺序依次为pH、PAM、FeSO4·7H2O、LIME、Na2S;处理500mL络合铜废水的最佳的操作条件是废水初始...     

Removal of phosphate from wastewater using alkaline residue

Alkaline residue(AR) was found to be an efficient adsorbent for phosphate removal from wastewater. The kinetic and equilibrium of phosphate removal were investigated to evaluate the performance of modified alkaline residue. After treatment by NaOH(AR-NaOH), removal performance was significantly improved, while removal performance was almost completely lost after treatment by HCl(AR-HCl). The kinetics of the removal process by all adsorbents was well characterized by the pseudo second-order model. The Langmuir model exhibited the best correlation for AR-HCl, while AR was effectively described by Freundlich model. Both models were well fitted to AR-NaOH. The maximum adsorption capacities calculated from Langmuir equation were in following manner: AR-NaOH AR AR-HCl. Phosphate removal by alkaline residue was pH dependent process. Mechanisms for phosphate removal mainly involved adsorption and precipitation, varied with equilibrium pH of solution. For AR-HCl, the acid equilibrium pH( 6.0) was unfavorable for the formation of Ca-P precipitate, with adsorption as the key mechanism for phosphate removal. In contrast, for AR and ARNaOH, precipitation was the dominant mechanism for phosphate removal, due to the incrase on pH( 8.0) after phosphate removal. The results of both XRD and SEM analysis confirmed CaHPO4·2H2O formation after phosphate removal by AR and AR-NaOH.     

Warm forming die design,Part II: Parting surface temperature response characterization of a novel thermal finite element modeling code

The majority of the research activities in the area of warm forming are concentrated on demonstrating or simulating the improved formability associated with forming lightweight materials such as aluminum alloys at elevated temperatures. However, the ability to design the proper thermal management system within the forming tool is a critical aspect to delivering this technology as a viable, stable production alternative to traditional stamping. This work begins to address the thermal stability issues of this process by examining the impact of process cycle time on the parting surface temperature response. Cycle times of 10, 15, 30, and 300 s were evaluated using a reciprocating surface and a self-heated experimental block of 1020 steel fitted with resistance cartridge heaters. The presented results indicate that cycle time does not significantly impact the steady-state temperature response at the parting surface for a well-insulated die that has proper thermal management. Parting surface experimental results were compared to values obtained numerically and through the use of the novel thermal finite element analysis software PASSAGE/Forming^®.