N2气氛下煅烧的黄铁矿对As(Ⅲ)的吸附作用

微量As(Ⅲ)是水中较难去除的毒性物质,天然黄铁矿对水中As(Ⅲ)的去除能力低于磁黄铁矿.将黄铁矿在氮气下高温煅烧使其转变为由磁黄铁矿构成的多孔结构化材料,具有较高的比表面积和表面化学反应活性,在地下水As(Ⅲ)去除方面具有潜在的应用前景.考察了煅烧温度、煅烧时间、pH值以及溶解氧对去除水中As(Ⅲ)的影响.结果表明黄铁矿煅烧生成的单斜磁黄铁矿对As(Ⅲ)具有最佳去除效果,最佳煅烧条件为600℃煅烧1 h;在水溶液有溶解氧条件下煅烧黄铁矿去除As(Ⅲ)的适宜p H值范围较宽(4~10),而在水溶液缺少溶解氧条件下适宜pH值则变为7~10;煅烧黄铁矿在有氧水溶液中对As(Ⅲ)的吸附比缺氧水溶液中的吸附效果好.     

油页岩对钴离子的吸附性能研究

油页岩中因含有大量的黏土矿物而对金属离子具有一定的吸附能力.采用静态吸附法对油页岩吸附钴离子的影响因素及吸附动力学进行了研究.结果表明,油页岩粒度、溶液浓度、溶液pH值、吸附时间等均对吸附性能有一定影响.油页岩对钴离子的吸附量随样品粒径的减小而增大;随着钴离子初始浓度的增加,油页岩对钴离子的吸附总量增加;溶液pH值在3~8范围内,油页岩对钴离子的吸附量和吸附率随着pH值的增大呈上升趋势.通过吸附动力学研究发现,油页岩对钴离子的吸附过程符合准二级动力学过程和粒子内扩散机理.     

磁赤铁矿对有机染料吸附行为的特征研究

利用标准地质样品磁赤铁矿,运用XRD,BET对其进行晶型及比表面积的表征。采用动态吸附实验,研究了磁赤铁矿对浓度为1.0×10-5 mol/L的酸性桃红(Sulforhodamine,SRB),结晶紫(Crystal violet,CV)的吸附特性。考察了溶液离子浓度、pH、吸附时间以及吸附剂投加量对其吸附特性的影响。结果表明,在相同实验条件下,SRB在100min达到吸附平衡,CV在20min达到吸附平衡。溶液pH和离子强度对其吸附都有很大的影响,磁赤铁矿对CV及SRB的最大吸附量分别为3.27×10-3及0.587×10-3。利用Langmuir和Freundlich等温吸附模型对吸附过程进行描述,结果表明,磁赤铁矿对SRB的吸附符合Freundlich模型,对CV的吸附属于Langmuir模型。用准一级和准二级吸附动力学方程对实验数据进行了线性回归分析,结果表明SRB属于准一级动力学方程,CV属于准二级动力学方程。热力学研究表明,磁赤铁矿吸附CV及SRB的过程都是自发进行的吸热反应。     

黄铁矿净化水中低浓度磷

以产自安徽铜陵新桥矿的黄铁矿为典型样品,研究黄铁矿对磷的吸附作用。静态实验考察黄铁矿粒度、固液比、pH值、离子强度、温度、吸附时间等因素对黄铁矿去除磷效果的影响,XPS和FE-SEM研究吸附磷后黄铁矿颗粒表面形貌和成分特征。结果表明：黄铁矿粒径越小（50～180目）,去除磷效率越高（9.3%～90.7%）;提高固液比（0.2～2 g/L）,磷的去除率增加（6.5%～97.1%）;在pH值3～9.65范围内黄铁矿对磷都有很好的去除效率（95%以上）;NO3-对磷的去除效果表现为微弱的促进作用,Cl-有微弱的抑制作用,溶液中SO42-、HCO3-对黄铁矿吸附磷表现出较强的抑制作用。温度对黄铁矿吸附效率基本没有影响。黄铁矿对磷吸附动态实验表明除磷效率在16 h后接近最大值。除磷作用机理是黄铁矿表面缓慢氧化产生的三价铁对磷的化学吸附。成果表明黄铁矿用于净化污水中低浓度磷具有很大的潜力。     

天然蛇纹石吸附Sb(V)的影响因素及机理分析

以焦锑酸钾(KSb(OH)_6)为Sb(V)锑源,采用XRD,XRF,FTIR对蛇纹石进行表征。探讨了不同吸附时间、Sb(V)初始浓度、初始pH、温度条件下蛇纹石吸附除Sb(V)的效果。结果表明:在动力吸附模型中,Elovich模型和假二级动力学模型对蛇纹石处理Sb(V)的拟合效果均较好,吸附过程为由化学吸附控制的非均相扩散,由假二级动力学模型可知理论最大吸附量为2.82×10~(-3);在等温吸附模型中,Langmuir模型拟合效果稍优于Freundlich模型,理论最大吸附量可达8.90×10~(-3);在广泛pH范围内,吸附量随着初始pH的降低而增加,初始pH值在1.9～3.6范围内时,吸附量迅速从6.66×10~(-3)减少至2.97×10~(-3),初始pH值大于3.6,吸附量随pH值增加而减少的幅度变小;蛇纹石对Sb(V)的吸附去除量随温度的升高而增大,最大为5.25×10~(-3)。蛇纹石Sb(V)的吸附为化学吸附;高零电点使蛇纹石在广泛pH值范围内可被质子化,Sb(OH_6)~-与质子化的镁氧(氢氧)八面体端面形成配合物。     

低聚合羟基铁-蒙脱石复合体吸附铬酸根的实验研究

摘要：在模拟的酸性土壤条件下，利用制备的低聚合羟基铁蒙脱石复合体对铬酸根进行吸附实验。重点研究了吸附条件对复合体铬吸附能力的影响，对比了蒙脱石和含水氧化铁。结果表明，实验条件下复合体有较强的铬吸附能力，其铬吸附量低于铁沉积物而明显高于蒙脱石。铬初始质量浓度是影响复合体铬吸附量的最主要因素，离子强度次之。吸附时间(12h以上)、温度、pH值对复合体铬吸附量的影响很小；说明在酸性土壤条件下，复合体有强且稳定的铬吸附能力。     

氧化锰、氧化铁、氧化铝对砷(Ⅲ)的吸附行为研究

合成了氧化锰、氧化铁、氧化铝三种矿物,以氧化铁、氧化锰为吸附剂研究了pH值、离子强度和时间等因素对吸附As(Ⅲ)的影响,并讨论了氧化锰、氧化铁、氧化铝三种矿物对As(Ⅲ)的饱和吸附容量及等温吸附实验。pH值对氧化锰吸附As(Ⅲ)几乎不影响,对氧化铁吸附As(Ⅲ)在很大的范围内(pH为3.5~8.5)影响不大,离子强度对二者吸附As(Ⅲ)的影响不大,吸附反应在0.5 h左右达到吸附平衡。在优化吸附条件下氧化锰、氧化铁、氧化铝对As(Ⅲ)的饱和吸附容量分别为48.38 mg/g、23.70 mg/g、3.52mg/g,三种合成矿物对As(Ⅲ)的饱和吸附容量:氧化锰氧化铁氧化铝。对实验数据进行Freundlich和Langmuir拟合,相关系数R均在0.98以上,吸附动力学符合Lagergren二级速率方程。     

黄河泥沙对硝基氯苯的吸附机理研究

通过静态吸附实验,研究了黄河底泥对硝基氯苯的吸附机理,并在此基础上研究了影响吸附的不同条件。实验结果表明,最佳平衡吸附时间为2h;吸附量随着平衡浓度的增加而增加,随着含沙量的增加而降低;温度对吸附的影响随含沙量不同而不同,含沙量较高时,温度对吸附影响不大,含沙量较低时,吸附量随温度的升高呈先下降后增加的趋势;在本实验条件下,吸附量随着pH值的增加而下降,随离子强度增加而增加。     

膨润土尾矿复合陶粒制备与Cr(Ⅵ)吸附性能

膨润土提纯后的尾矿主要含石英、斜绿泥石和白云母等矿物,以尾矿为主原料制备了复合陶瓷颗粒,采用XRD,IR和SEM探讨了烧结工艺对结构变化的影响,研究了复合陶瓷颗粒的组分变化、烧结温度、pH、初始浓度、吸附时间和温度对Cr(Ⅵ)离子吸附效果的影响,探讨了动力学和热力学变化。结果表明,烧结温度对吸附影响不大,烧结适宜温度为1000℃,陶瓷颗粒的主晶相为石英和硅灰石,表面为不均匀多孔结构。吸附的最佳吸附条件是pH值1、陶瓷颗粒用量1 g、吸附时间12 h及铬离子初始浓度100 mg/L,吸附率达96.33%。吸附行为符合准二级动力学方程,属于单分子层化学吸附;热力学数据说明,吸附反应为自发吸热反应。     

焙烧水滑石吸附脱除水中硫酸根离子的研究

利用焙烧水滑石对水中硫酸根离子进行吸附性能研究,考查了初始pH值、吸附时间、吸附剂用量等条件对吸附的影响。结果表明,焙烧水滑石对水中硫酸根离子具有良好的吸附能力。X射线衍射分析结果表明,水滑石及其焙烧产物对硫酸根的吸附机理不同。pH值对吸附的影响较大,pH值较低时吸附效果较好。吸附平衡符合Langmuir方程,室温下饱和吸附量为32.895 mg/g。     

地下水系统中镍污染和天然胶体共迁移特征

为了对地下水系统中天然胶体与Ni²⁺的共迁移特征进行研究,通过静态吸附实验和石英砂模拟含水层介质柱实验研究了土壤胶体对Ni²⁺在地下水中运移的影响,以及pH、离子强度（IS）、有机质等对土壤胶体吸附Ni²⁺的影响。结果表明：随着pH值升高,土壤胶体对Ni²⁺的吸附量增加;离子强度的增加会显著地降低土壤胶体吸附Ni²⁺的能力;腐殖酸（HA）的存在会增强胶体对Ni²⁺的吸附能力;在有胶体的情况下,Ni²⁺穿透砂柱的时间会缩短,吸附能力增强,吸附量增加,但当离子强度增加时,虽然Ni²⁺穿透砂柱的时间也被缩短,但是吸附量却降低。     

Evaluation of adsorption potential of bamboo biochar for metal-complex dye: equilibrium,kinetics and artificial neural network modeling

Metal-complex dyes are widely used in textile industry, but harmful to the environment and human health due to aromatic structure and heavy metal ions. The objective of this work was to evaluate the adsorption potential of bamboo biochar for the removal of metal-complex dye acid black 172 from solutions. Freundlich model was more suitable for the adsorption process of bamboo biochar than Langmuir isotherm, indicating multilayer adsorption of acid black 172 on a heterogeneous bamboo biochar surface. Adsorption kinetics analysis of pseudo-second-order and Weber–Morris models revealed that intraparticle transport was not the only rate-limiting step. The bamboo biochar exhibited a good adsorption performance even at high ionic strength. Analysis based on the artificial neural network indicated that the temperature with a relative importance of 29 % appeared to be the most influential parameter in the adsorption process for dye removal, followed by time, ionic strength, pH and dye concentration.     

The adsorption of gold(I) hydrosulphide complexes by iron sulphide surfaces

The adsorption of gold by pyrite, pyrrhotite, and mackinawite from solutions containing up to 40 mg/kg (8 μm) gold as hydrosulphidogold(I) complexes has been measured over the pH range from 2 to 10 at 25°C and at 0.10 m ionic strength (NaCl, NaClO₄). The pH of point of zero charge, pH_pzc, has been determined potentiometrically for all three iron sulphides and shown to be 2.4, 2.7, and 2.9 for pyrite, pyrrhotite, and mackinawite, respectively. In solutions containing hydrogen sulphide, the pH_pzc is reduced to values below 2. The surface charge for each sulphide is therefore negative over the pH range studied in the adsorption experiments. Adsorption was from 100% in acid solutions having pH < 5.5 (pyrite) and pH < 4 (mackinawite and pyrrhotite). At alkaline pH’s (e.g., pH = 9), the pyrite surface adsorbed 30% of the gold from solution, whereas the pyrrhotite and mackinawite surfaces did not adsorb.The main gold complex adsorbed is AuHS°, as may be deduced from the gold speciation in solution in combination with the surface charge. The adsorption of the negatively charged Au(HS)₂⁻ onto the negatively charged sulphide surfaces is not favoured. The X-ray photoelectron spectroscopic data revealed different surface reactions for pyrite and mackinawite surfaces. While no change in redox state of adsorbent and adsorbate was observed on pyrite, a chemisorption reaction has been determined on mackinawite leading to the reduction of the gold(I) solution complex to gold(0) and to the formation of surface polysulphides. The data indicate that the adsorption of gold complexes onto iron sulphide surfaces such as that of pyrite is an important process in the “deposition” of gold from aqueous solutions over a wide range of temperatures and pressures.     

Adsorption of chromate on variable charge soils as influenced by ionic strength

The adsorption behavior of chromate on two variable charge soils (Oxisol and Ultisol) was investigated through batch experiments at different ionic strengths and pH values. The adsorption of chromate on the variable charge soils was found to be strongly dependent on the pH of the soil solutions. A characteristic pH was observed, which corresponds to the intersection of the chromate adsorption—pH curves at different ionic strengths. The characteristic pH values are 5.50 for Oxisol and 5.04 for Ultisol, close to the point of zero salt effect (PZSE) of these soils. The zeta potentials measured for these soils provide the evidences to support the interpretation of the effect of ionic strength on the adsorption of chromate on these variable charge soils. The adsorption behavior of chromate was interpreted by a schematic representation of chromate distribution at increasing ionic strength. The chromate desorption–pH curves were also found to intersect at pH of 5.15 and 4.89 for the Oxisol and Ultisol, respectively. It is considered that chromate adsorption by the variable charge soils was mainly determined by the electrostatic potential on the adsorption plane, which was controlled by the ionic strength of the soil solutions.     

Adsorption of antimony(V) on kaolinite as a function of pH,ionic strength and humic acid

The present work investigated the adsorption and mobility (desorption) of Sb(V) on kaolinite using batch experiments. The adsorption of Sb(V) on kaolinite was studied as a function of contact time, pH, ionic strength, humic acid (HA), initial Sb(V) concentration and temperature. Kinetic studies suggest that the equilibrium is achieved within 24 h. The adsorption of Sb(V) was strongly affected by changes in I at low ionic strength and unaffected at high ionic strength. The adsorption is weakly dependent on the presence of humic acid, but is strongly dependent on pH. Within the range tested, the optimal pH for Sb(V) adsorption is 3.6, and close to 75% removal can be achieved. Desorption is dependent on the original suspension pH. The addition sequence of Sb(V)/HA do not influence the adsorption of Sb(V) on kaolinite. The adsorption data fit both the Freundlich and Langmuir isotherm. The thermodynamic parameters (ΔH ⁰, ΔS ⁰ and ΔG ⁰) were calculated from the temperature dependence, and the results suggest the endothermic and spontaneous nature of the process.     

Adsorption of brilliant green from aqueous solution by unmodified and chemically modified Tarap (<Emphasis Type="Italic">Artocarpus odoratissimus</Emphasis>) peel

Tarap peel (TP) and oxalic-acid-modified Tarap peel (TP-OX) were used to remove brilliant green (BG) dye from aqueous solution. Surface modification of TP suggested that functional groups such as carboxyl, hydroxyl and amino were involved in the adsorption of BG onto TP. Parameters such as effects of pH, contact time, ionic strength, initial dye concentration and temperature were included to study the adsorption of BG onto TP and TP-OX. Adsorption isotherm models were used to investigate the adsorption process, while kinetics models were used to provide insight into the adsorption mechanisms. Optimised contact time of 2 h with no pH adjustment was used. Adsorption of BG onto TP was best fitted to the Freundlich model, while experimental data for TP-OX are best described by the Tempkin model. The maximum adsorption capacities were determined as 174 and 275 mg g^?1 for TP and TP-OX, respectively. Thermodynamics study indicated the endothermic nature of adsorptions of BG onto both adsorbents. According to kinetics study, the adsorption mechanisms on both adsorbents followed pseudo-second-order model, and film diffusion might have major role in the adsorption process.     

Toward the understanding of the treatment of textile industries’ effluents by clay: adsorption of anionic dye on kaolinite

Clays, particularly kaolinite, are promising adsorbents for the treatment of textile effluents, but there is a need of better understanding the mechanisms of adsorption, especially in the case of anionic dyes. Thus, the removal of RR120 anionic dye was investigated using Tunisian raw clay (TBK) composed of kaolinite and illite, and a standard kaolinite (KGa-2), and conducting batch experiments by varying different parameters (contact time, ionic strength, concentration, temperature). We investigated the clays’ surface charges by electrophoretic mobility measures and the dye-clay interactions during adsorption, by the streaming-induced potentials (SIP). The results showed that KGa-2 has higher adsorption capacity for RR120 dye than TBK clay, moreover enhanced by increasing the ionic strength and/or lowering the pH of the aqueous. The SIP results showed an increase of negative charges for both clays, reflecting the adsorption of the anionic dye on the positive charges of the amphoteric surfaces of the clays. The SIP magnitudes indicated a higher adsorption rate for KGa-2 in accordance with the kinetic study. The Sips model that described the best adsorption isotherms indicates lateral interactions of the dye molecules, stronger in the case of KGa-2 than TBK. Also, the dye molecules form a thinner layer on KGa-2 surfaces. In addition, the dye molecule’s structure was not altered, as verified by mass spectrometry. The adsorption process was feasible and spontaneous and favored at ambient temperature. Thus, kaolinite-rich clays are effective in the removal of anionic dyes in aqueous solution and potential good adsorbents in wastewater treatment.     

热活化胶状黄铁矿去除酸性溶液中的Cd(Ⅱ)

利用XRD和SEM测试方法表征了热活化胶状黄铁矿结构和微观形貌,考察了溶液pH、溶解氧和热活化温度对热活 化胶状黄铁矿去除水中Cd（Ⅱ）的影响,并探讨了除Cd（Ⅱ）反应动力学和作用机理。胶状黄铁矿在N2氛围下650℃热活化 5 min可完全分解生成多孔结构化单斜磁黄铁矿（PMPyr）。在pH 2~6的无氧水溶液中PMPyr除Cd（Ⅱ）效率均达到88%以 上,除Cd（Ⅱ）效率受pH影响较小;PMPyr表面氧化会抑制其与Cd（Ⅱ）的反应。PMPyr除Cd（Ⅱ）动力学可用准二级动力学模型拟合（R2> 0.9992）,结合溶液pH变化趋势、Fe（Ⅱ）和SO42-浓度变化推测,PMPyr除Cd（Ⅱ）机理主要是Fe1-xS和CdS溶度积差异推动了PMPyr与Cd（Ⅱ）交换反应,表面络合属于次要作用。