蔬菜对土壤镉铜锌富集能力的研究

调查了福建部分污染严重地区不同蔬菜对镉、锌、铜的富集能力。结果表明蔬菜对镉的平均富集系数为0.017,锌的平均富集系数为0.116.铜的平均富集系数为0.014。蔬菜对镉的富集系数的品种间差异最大,达315倍,远高于锌和铜的富集系数的品种间差异。茭白、豇豆和莲藕对镉的富集能力较低,可作为镉污染土壤优先选种的蔬菜品种,而青包菜、白包菜、芥菜、空心菜、芋头等对镉的富集系数较高,不宜在镉污染土壤上栽培。     

Qualitative analysis and quantitative simulation on Yin-Huang water salinization mechanism in Bei-Da-Gang reservoir

Yellow River water transfer for Tianjin is important in solving the water shortage in Tianjin, which facilitate economic development and social progress for many years. Fresh water drawn from Yellow River（ i. e., Yin-Huang water） becomes saltier and saltier when being stored in the Bei-Da-Gang reservoir. We qualitatively analyze the water salinization mechanism based on mass transfer theory. The main factors are salinity transfer of saline soil, evaporation concentrating, and the agitation of wind. A simulative experimental pond and an evaporation pond were built beside the Bei-Da-Gang reservoir to quantitatively investigate the water salinization based on water and solute balance in the simulative pond. 80% of increased [Cl^-] is due to the salinity transfer of the saline soil and the other 20% is due to evaporation concentrating, so the former is the most important factor. We found that the salinization of Yin-Huang water can be described with a zero-dimension linear model.     

广东河源电厂循环水高浓缩倍率试验研究及工程应用

循环冷却系统浓缩排污水是电厂最大的排污水,是节水减排和废水零排放的关键问题之一。以河源电厂为例,分析了电厂进水水质条件;选用了5种水稳剂,采取极限碳酸盐硬度计算浓缩倍率的方法,通过静动态阻垢、防腐与杀菌试验,探明了各种药剂的极限浓缩倍率,论证了河源电厂循环冷却系统10倍以上的浓缩倍率运行方式的可行性。按试验所确定的原则,河源电厂循环冷却水系统按10倍的浓缩倍率运行,一年来未出现腐蚀与结垢现象。分析了实际运行期间的运行数据,对我国循环冷却水处理、节约用水、减少排污具有一定的示范意义。     

强化混凝-吸附预处理生活污水

采用混凝/吸附复配的方式对生活污水进行了浓缩预处理。通过对有机物去除率和混合絮体沉降性能的考察,优选出最佳混凝剂聚合氯化铝和最佳吸附剂粉末活性炭,其最优投加量分别为60 mg/L和40 mg/L。在此复配条件下,COD去除率由单独投加混凝剂时的62%提高到73%,浊度去除率由88%提高到93%。同时利用分子量分级实验进一步阐述了混凝/吸附复配过程提升污水浓缩效果的机制。在机械加速澄清池连续实验中,在原水COD 300~500 mg/L、浊度130~360 NTU的水质条件下,出水COD稳定在70~86 mg/L之间,去除率达80%以上,出水浊度稳定在10 NTU以下。     

东川因民矿区地下水-选厂水水化学特征及资源化影响因素

矿区水质分析结果表明,地下水属弱碱性淡水软水-微硬水。泉水水化学类型为HCO3-Ca·Mg。坑道水水化学类型为HCO3-Mg·Ca、HCO3·SO4-Mg·Ca、SO4·HCO3-Mg·Ca和SO4-Mg·Ca。地下水水化学成分的变化与(SO42-)浓度相关。泉水与坑道水具有一定的水力联系。选厂排放水中Pb、As含量高于坑道水。坑道水、选厂排放水具有弱侵蚀性。采矿活动和选矿过程对地下水-选厂水水质有较大影响,地下水水化学演变受控于矿业活动和矿区地球化学背景。     

干式电选工艺在化工矿山中的应用研究

在详细分析原矿性质的基础上,采用悬浮电选机干式作业对磷矿石进行富集。试验结果表明,磷矿石经一粗一精一扫电选作业后可得到品位为30．23％的磷精矿,其回收率为83．26％。干式电选工艺无废水产生,而且工艺简单,分选指标好,是磷矿石富集的重点处理工艺,有很好的工业应用前景。     

Inefficiencies analysis of a point-focus CPV∕T system

In this paper, a point-focus concentrating photovoltaic and thermal (CPV∕T) system, sized for a domestic application, is presented in order to evaluate its inefficiencies and the related costs. The CPV∕T system adopts parabolic concentrator mirrors to reflect the light on triple-junction cells InGaP∕InGaAs∕Ge (indium--gallium phosphide∕indium--gallium arsenide∕germanium) placed on pipes, where the cooling fluid flows; CPV∕T system consists of three modules in parallel linked to a tank that works as hot water storage. The main maintenance problems are due to: moving parts such as the tracking system, cell wear linked to hotspot problems and optics cleaning. In particular, the model presented allows us to evaluate electric and thermal outputs, energy inefficiencies, and maintenance costs of the CPV∕T system. The analysis has been subdivided in several steps and a FMECA (Failure Mode, Effects and Criticality Analysis) approach has been considered to investigate the main failure modes and their relative effects in terms of efficiency losses and intervention costs. So, the inefficiencies analysis has allowed to identify the system malfunction causes, evaluating the impact due to the stops for each type of fault. Hence, an economic analysis has allowed to evaluate the CPV∕T system convenience when inefficiencies and maintenance incidence are also considered.     

Membrane fouling controlled by coagulation/adsorption during direct sewage membrane filtration (DSMF) for organic matter concentration

Unlike the role of the membrane in a membrane bioreactor, which is designed to replace a sediment tank, direct sewage membrane filtration (DSMF), with the goal of concentrating organic matters, is proposed as a pretreatment process in a novel sewage treatment concept. The concept of membrane-based pretreatment is proposed to divide raw sewage into a concentrated part retaining most organics and a filtered part with less pollutant remaining, so that energy recovery and water reuse, respectively, could be realized by post-treatment. A pilot-scale experiment was carried out to verify the feasibility of coagulant/adsorbent addition for membrane fouling control, which has been the main issue during this DSMF process. The results showed that continuous coagulant addition successfully slowed down the increase in filtration resistance, with the resistance maintained below 1.0 × 10¹³ m^− 1 in the first 70 hr before a jump occurred. Furthermore, the adsorbent addition contributed to retarding the occurrence of the filtration resistance jump, achieving simultaneous fouling control and chemical oxygen demand (COD) concentration improvement. The final concentrated COD amounted to 7500 mg/L after 6 days of operation.     

Membrane fouling controlled by coagulation/adsorption during direct sewage membrane filtration (DSMF) for organic matter concentration

Unlike the role of the membrane in a membrane bioreactor, which is designed to replace a sediment tank, direct sewage membrane filtration(DSMF), with the goal of concentrating organic matters, is proposed as a pretreatment process in a novel sewage treatment concept. The concept of membrane-based pretreatment is proposed to divide raw sewage into a concentrated part retaining most organics and a filtered part with less pollutant remaining, so that energy recovery and water reuse, respectively, could be realized by post-treatment. A pilot-scale experiment was carried out to verify the feasibility of coagulant/adsorbent addition for membrane fouling control, which has been the main issue during this DSMF process. The results showed that continuous coagulant addition successfully slowed down the increase in filtration resistance, with the resistance maintained below 1.0 × 1013m~(-1) in the first 70 hr before a jump occurred. Furthermore,the adsorbent addition contributed to retarding the occurrence of the filtration resistance jump, achieving simultaneous fouling control and chemical oxygen demand(COD)concentration improvement. The final concentrated COD amounted to 7500 mg/L after 6 days of operation.     

选矿废水净化处理与回用的研究与生产实践

通过废水净化处理试验和废水回用选矿对比试验 ,对南京栖霞山锌阳矿业有限公司选矿废水的处理与回用进行了研究 ,最终提出了优先直接回用 ,其余适度净化处理再回用的方案 ,实现了废水的零排放。设计了废水全部回用系统 ,并已成功地应用于生产实践。