阿拉尔河悬浮物对铀的吸附影响研究          下载免费PDF全文

钟翼  许建新  韩积斌  徐凯 《盐湖研究》2020,28(1):112-122

为了解阿拉尔河悬浮物对铀的吸附特性,通过静态吸附实验,研究了吸附时间、pH值、温度和铀初始浓度等因素对模拟含铀水中U(VI)去除率的影响,并从热力学和动力学方面对吸附过程进行了分析。结果表明,在T=25℃,溶液初始pH=7,接触时间为16 h时,悬浮物对铀的平衡吸附率最佳,为95.48%。随着铀初始浓度的增加,吸附量增加,但吸附率随之下降,升高温度有利于铀的吸附。铀在悬浮物上的吸附过程符合Langmuir等温吸附方程,说明悬浮物对铀为单分子层吸附,且化学吸附占主导地位。吸附动力学过程可用准二级吸附动力学模型描述,表明吸附主要受动力学控制,由两个以上步骤共同控制。FTIR和EDS分析结果表明,吸附过程中铀主要与悬浮物表面活性基团螯合并以表面络合吸附为主。吸附前后的能谱对比分析表明,吸附过程中存在离子交换行为。因此,悬浮物对铀的吸附机理是以表面络合吸附和离子交换为主、物理吸附为辅的混合吸附过程。  相似文献   

红土镍矿样品前处理方法和分析测定技术研究进展     

燕娜  赵小龙  赵生国  郑红文 《岩矿测试》2015,34(1):1-11

随着常规镍来源的硫化镍矿资源的日益枯竭,可直接生产氧化镍、镍锍和镍铁等产品的红土镍矿倍受关注。对于红土镍矿中主量、次量、痕量元素的检测,相同的检测项目存在多种测试方法,且部分相同原理的测试方法存在细节上的差异,使得检测者选择合适的检测方法变得困难。本文综述了近年来红土镍矿中24种元素测定的样品前处理方式及分析技术研究进展。样品前处理方式依据目标元素及后续的分析方法进行选择,其中酸溶法和碱熔法用途最广。酸溶法引入的盐分少,操作简单,但是分解过程中易导致挥发元素As、Sb、Bi、Hg的损失,Cr易随高氯酸冒烟损失。碱熔法分解能力强,适合分析Cr、Si、全铁等项目,但会引入大量的盐类和因坩埚材料损耗而带入其他杂质,给后续分析带来困难。红土镍矿的分析技术依据实验室条件及目标元素的性质和浓度进行选择。电感耦合等离子体发射光谱法(ICP-AES)是主量、次量元素的主要分析方法,适合于分析含量为10-5~30%级别的金属元素;X射线荧光光谱法主要用于分析含量为10-3~1级别的元素,尤其适合于测定Al、Si、Ti、V和P,由于该方法的准确性依赖于一套高质量的标准样品,故更适合炉前检测或检测大批红土镍矿样品。电感耦合等离子体质谱法(ICP-MS)最适合于分析10-4含量以下的重元素,特别是稀土和贵金属元素。原子吸收光谱法(AAS)适合于分析10-4~10-2级别的Ca、Mg、Ni、Co、Zn、Cr、Mn等低沸点、易原子化元素。分光光度法主要用于分析Ni和P。原子荧光光谱法(AFS)主要用于分析As、Bi、Sb等易形成气态氢化物的元素。容量法主要用于分析Al、Fe、Mg和Si O2等主含量元素。尽管AAS、分光光度法、AFS法和容量法检测周期长,但所用仪器为实验室常规配置,可满足缺乏相应大型仪器实验室的日常检测。本文认为,针对各种检测方法的适用性及存在问题,应从开发微波消解法、固体进样直接测汞法、ICP-MS法以及Cr与其他元素同时分析的快速分析方法等方面开展研究,建立灵敏、准确的检测方法,从而更好地服务于红土镍矿的贸易、检验和综合利用。  相似文献   

Adsorption of Chromium(III), Nickel(II), and Copper(II) from Aqueous Solution by Activated Alumina     

Nilima S. Rajurkar  Ashok N. Gokarn  Kumaree Dimya 《洁净——土壤、空气、水》2011,39(8):767-773

The possible use of activated alumina powder (AAP) as adsorbent for Cr(III), Ni(II), and Cu(II) from synthetic solutions was investigated. The effect of various parameters on batch adsorption process such as pH, contact time, adsorbent dosage, particle size, temperature, and initial metal ions concentration were studied to optimize the conditions for maximum metal ion removal. Both higher (molar) and lower (ppm) initial metal ion concentration sets were subjected to adsorption on AAP. Adsorption process revealed that equilibrium was established in 50 min for Cr(III) at pH 4.70, 80 min for Ni(II) at pH 7.00, and 40 min for Cu(II) at pH 3.02. Percentage removal was found to be highest at 55°C for Cr(III) and Ni(II) with 420 µm and 45°C for Cu(II) with 250‐µm particle size AAP. A dosage of 2 g for Cr(III), 8 g for Ni(II), and 10 g Cu(II) gave promising data in the metal ion removal. The adsorption process followed Langmuir as well as Freundlich models. The thermodynamics of adsorption of these metal ions on activated aluminum indicated that the adsorption was spontaneous and endothermic in nature. Present study indicates that AAP can act as a promising adsorbent for industrial wastewater treatment.  相似文献   

Removal of Ni(II) Using Cation Exchange Resins in Packed Bed Column: Prediction of Breakthrough Curves     

Ponnaiah Gomathi Priya  Chiya Ahmed Basha  Veerappan Ramamurthi 《洁净——土壤、空气、水》2011,39(1):88-94

Sorptive removal of Ni(II) from electroplating rinse wastewaters by cation exchange resin Dueolite C 20 was investigated at the temperature of 30°C under dynamic conditions in a packed bed. The effects of sorbent bed length 0.1–0.2 m, fixed flow rate 6 dm³ min^?1, and the initial rinse water concentration (C₀) 53.1 mg L^?1 on the sorption characteristics of Dueolite C 20 were investigated at an influent pH of 6.5. More than 94.5% of Ni(II) was removed in the column experiments. The column performance was improved with increasing bed height and decreasing the flow rate. The Thomas, Yoon–Nelson, Clark, and Wolborska models were applied to the experimental data to represent the breakthrough curves and determine the characteristic design parameters of the column. The sorption performance of the Ni(II) ions through columns could be well described by the Thomas, Yoon–Nelson, and Wolborska models at effluent‐to‐influent concentration ratios (C/C₀) >0.03 and <0.99. Among the all models, the Clark model showed the least average percentage time deviation. The sorptive capacity of electroplating rinse water using Ni(II) was found to be 45.98 mg g^?1.  相似文献   

Cotton Fiber/ZrO2, A New Material for Adsorption of Cr(VI) Ions in Water     

Alfredo Alberto Muxel  Sonia Maria Nobre Gimenez  Flaveli Aparecida de Souza Almeida  Rení Ventura da Silva Alfaya  Antonio Alberto da Silva Alfaya 《洁净——土壤、空气、水》2011,39(3):289-295

The natural cotton fiber was used to synthesize an anion exchange, containing ZrO₂ film on its surface, NCFZC (natural cotton fiber/ZrO₂ composite). This anion exchanger was produced by the reaction of the zirconium oxychloride and hydroxyl groups on surface of the natural cotton fiber. The material was used for Cr(VI) ions adsorption studies. Adsorption equilibrium time and optimum pH for Cr(VI) adsorption were found to be 6 h and 4.0, respectively. The Langmuir and Temkin isotherms were used to models adsorption equilibrium data. The adsorption capacity of NCFZC was found to be 1.33 mmol/g. Kinetic studies showed that the rate of adsorption of Cr(VI) on NCFZC obeyed a pseudo‐second‐order kinetic model.  相似文献   

Removal of Organochlorine Pesticides from Aqueous Solution by Using Neutralized Red Mud     

Senar Ozcan  Ali Tor  Mehmet Emin Aydin 《洁净——土壤、空气、水》2011,39(11):972-979

This work describes the potential usability of neutralized red mud for the removal of organochlorine pesticides (OCPs) from aqueous solutions. After examination on the adsorption capability of neutralized red mud for all studied OCPs, the experiments were performed by employing aldrin as a model compound. The effect of several parameters, such as contact time, pH of the solution, initial aldrin concentration, and dosage of the adsorbent was evaluated by batch experiments. The determination of OCPs was carried out using traditional liquid–liquid extraction followed by a GC coupled with µ‐electron capture detector (GC‐µECD). The results showed that adsorption equilibrium time depended upon the initial aldrin concentration and adsorption followed the second‐order kinetic model. Kinetic study also indicated that the film diffusion mechanism was a main rate control mechanism. The removal was explained by considering the electrostatic interactions between metal oxides surface of the neutralized red mud and inductively charged centers (negative charge (d?) of chlorine atoms and positive charge (d+) of π‐cloud aromatic ring) of the aldrin molecules. In comparison to the Langmuir isotherm model, the Freundlich model better represented the adsorption data. The neutralized red mud was also succesfully employed for the removal of OCPs from real water samples, including tap water and surface (lake) water, fortified with studied OCPs.  相似文献   

Carbon isotopic fractionation by desorption of shale gases     

《Marine and Petroleum Geology》2015

Geochemical studies of shale gas and conventional reservoirs within the Triassic Yanchang Formation of Xiasiwan and Yongning Field, Ordos Basin show that methane is isotopically depleted in ¹³C as compared to δ¹³C₁ calculated by the Ro based on the relationship between δ¹³C₁ and Ro. Geochemical fractionation during the adsorption/desorption process of shale system may play a significant part in influencing δ¹³C₁ values of shale gas. Two shale core samples from confined coring of the Yanchang Formation were adopted segmented desorption experiments to examine this phenomenon. The results show that the δ¹³C₁ of desorbed gas changes little in the first few phases of the experiments at low desorption levels, but become less negative rapidly when the fraction of desorbed methane exceeds 85%. The desorption process for the last 15% fraction of the methane from the shale samples shows a wide variation in δ¹³C₁ from −49‰ to −33.9‰. Moreover, δ¹³C₁ of all desorbed methane from the shale samples is substantially depleted in ¹³C than that calculated by Ro, according to Stahl and Carey's δ¹³C₁–Ro equation for natural gas generated from sapropelic organic matter. This shows some gases with isotopically enriched in ¹³C cannot be desorbed under the temperature and pressure conditions of the desorption experiments. This observation may be the real reason for the δ¹³C₁ of shale gases and conventional reservoirs becomes more negative in Xiasiwan and Yongning Fields, Ordos Basin. The magnitude of the deviation between the δ¹³C₁ of shale gas and that calculated by Ro may be related to the adsorption capacity of shale or the proportion of absorbed gases. In this way, we may be able to evaluate the relative adsorption capacity of shale in geological conditions by δ¹³C₁ of the shale gas, or by δ¹³C₁ of conventional gas which generated by the shale with certainty. The δ¹³C₁ of conventional gas in Dingbian and Yingwang Fields have no deviation because the TOC value of the hydrocarbon source rock is relatively low.  相似文献   

煤层气赋存的分形特征研究          下载免费PDF全文

王辰  冯增朝  周动  赵东  蔡婷婷 《地球物理学报》2019,62(9):3571-3579

本文利用红外热成像手段，对微小煤样内的甲烷吸附区进行了观察，并评估其吸附特征与在煤中的分布规律.研究表明煤中存在不同尺度与甲烷吸附能力的甲烷富集区，吸附/解吸甲烷时，甲烷富集区比邻近区域具有更明显的升温/降温现象.通过图像处理的方法对不同吸附压力条件下的红外热像图中的甲烷富集区进行提取，采用盒维数进行统计发现甲烷富集区符合分形规律.试验表明随着吸附压力升高，甲烷富集区的分形维数增大，分布初值减小.对两个不同煤田的煤层气富集区进行统计表明：从微米级到千米级尺度范围内，甲烷富集区分布具有分形特征，且分形维数均在1.5~2.00之间.  相似文献   

Hydroxytyrosol Recovery From Olive Mill Wastewater: Process Optimization and Development of a Pilot Plant     

《洁净——土壤、空气、水》2017,45(4)

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氨基酸在粘土高岭石上吸附等温线的研究   总被引：2，自引：0，他引：2  

刘效兰  张正斌 《海洋科学》2002,26(9):1-4

研究了4种氨基酸（甘氨酸，赖氨酸，天冬氨酸，谷氨酸）在粘土高岭石上的吸附等温线以及金属铜离子对其等温线的影响。研究表明，氨基酸在高岭石上的吸附等温线以及金属铜离子存在时的吸附等温线均属Langmuir型等温线；铜离子浓度增加时，其等温线斜率也增加，并认为体系可形成Ⅰ型三元表面络合物，铜离子对氨基酸在高岭石上等温线影响的规律和在相同体系中它对氨基酸在高岭石上交换吸附百分率E（%）-pH曲线的影响规律相一致。  相似文献