响应面法优化巴旦木壳对废水中Pb、Cu和Cd的吸附及同时测定

研究废弃巴旦木壳对模拟废水中Pb、Cu和Cd的去除率。在单因素实验的基础上,采用响应面法对吸附剂投加量、吸附时间和pH值3因素进行优化。实验结果表明,Pb、Cu和Cd分别在最佳吸附吸附剂投加量0.4 g,吸附时间49.38 min,pH值为9.96;吸附剂投加量0.4 g,吸附时间49.91 min,pH值为10.13;吸附剂投加量0.4 g、吸附时间49.83 min、pH值为10.42的条件下,去除率分别为87.42%、73.49%和85.11%。采用偏最小二乘法(PLS)对Pb、Cu和Cd模拟混合试样吸附后的溶液测定的曲线进行拟合回归,计算得出吸附剂对Pb、Cu和Cd的去除率分别为83.2%、66.0%和83.3%。用PLS对吸附后的模拟废水样品进行计算分析,并间接得出巴旦木壳对Pb、Cd和Cu的去除率和建立Pb、Cd、Cu三组分同时测定的多元校正分析方法。     

二硫代乙二酰胺改性硅胶固相萃取-火焰原子吸收光谱法测定水中的痕量铜和铅

制备了二硫代乙二酰胺改性硅胶作为固相萃取吸附剂,在pH 5.2,吸附时间为40min时,得到Cu2+、Pb2+的最大静态吸附容量,分别为19.50,29.39mg·g-1。水样中痕量的Cu2+、Pb2+经固相萃取后采用火焰原子吸收光谱法测定。在最佳条件下,Cu2+、Pb2+的线性范围分别为1.0~100,10~300μg·L-1,检出限(3S/N)分别为0.7,5.0μg·L-1。加标回收率在97.6%~104%之间。方法用于分析标准模拟水样,测定值与认定值相符。     

累托石-壳聚糖吸附剂对Cd~(2+)的吸附作用研究

利用累托石负载壳聚糖制备一种复合吸附剂,并对其结构进行了表征.研究了复合吸附剂对Cd2+的吸附,应用正交试验确定了最佳吸附条件:当pH值为7,吸附时间为30min,投加量为0.3g和温度为20℃时,Cd2+的吸附率达99%以上,处理后的水符合国家污水综合排放标准(GB8978-1996)中的一级标准.通过对实验数据运用相关数学模型拟合,复合吸附剂对Cd2+的吸附符合Langmuir和Freundlich吸附等温式.     

改性核桃壳生物炭对模拟水样中Pb(Ⅱ)的吸附性能研究

该文利用改性核桃壳生物炭对水中Pb(Ⅱ)进行吸附研究,探究了吸附剂投加量、pH值、接触时间、金属离子初始浓度和温度对吸附性能的影响,并对改性前后核桃壳的吸附性能进行了比较。Pb(Ⅱ)初始浓度为100mg/L时,在298K下,当pH值为5.0、投加量为7g/L、以180r/min振荡吸附2h,改性吸附剂CMBC的平衡吸附量为14.23mg/g,吸附率可达99.58%。吸附过程可用Langmuir等温吸附方程描述,且符合准二级动力学模型,是吸热且混乱度增加的自发过程,结果表明,改性核桃壳生物炭的吸附率较未改性时提高了27.21%,用解吸剂对CMBC进行5次吸附-解吸循环后,其对Pb(Ⅱ)的吸附率仍在90%以上,说明CMBC具有良好的吸附性能和再生能力。     

石墨烯/二氧化钛复合材料富集-石墨炉原子吸收光谱法测定铅和镉

以石墨烯/二氧化钛复合材料为吸附剂,结合石墨炉原子吸收光谱法,建立了Pb?和Cd?的检测方法。优化的实验条件为:溶液pH=5.0,吸附时间为60 min,吸附剂用量为0.02 g。结果表明:吸附过程符合拟二级动力学反应模型;吸附反应是吸热过程。建立的石墨烯/二氧化钛复合材料富集-石墨炉原子吸收光谱法对Pb2+和Cd2+的检出限分别为0.086和0.006μg/L,相对标准偏差为3.2%和2.5%。将本方法应用于矿石标准样品的测定,测定结果与标准值相符;用于茶叶实际样品的测定,回收率为96.8%~105.0%。     

核桃壳对废水中Zn~(2+)的吸附研究

采用核桃壳吸附模拟废水中Zn2+,实验结果表明,25℃时,采用粒径为2.5~3.0mm的吸附剂0.6g,pH值为6.0,处理50mL浓度为5mg/L的含Zn2+模拟废水,吸附时间120min,Zn2+的去除率达62%。核桃壳对Zn2+的吸附行为符合拟二级动力学方程和Freundlich等温吸附方程,Zn2+浓度分别为2mg/L、5mg/L、10mg/L时,吸附速率分别为0.0624g/mg·min、0.0060g/mg·min、0.0055g/mg·min,最大吸附量为0.465mg/g。吸附剂再生使用5次后去除率下降,吸附剂内部孔隙率下降。     

聚(丙烯酸-co-丙烯酰胺)/蒙脱土/腐殖酸钠复合物对Pb2+的吸附性能

用制备的聚(丙烯酸-co-丙烯酰胺)/蒙脱土/腐殖酸钠复合吸附剂,研究了溶液pH值、吸附时间和Pb2+溶液初始浓度等因素对重金属Pb2+的吸附性能,探讨了复合吸附剂对Pb2+的吸附机理。结果表明,在pH值为6.0、吸附时间2 h、Pb2+溶液初始浓度0.01 mol/L和吸附剂用量0.10 g的条件下,复合吸附剂对Pb2+的吸附量达到364.05 mg/g,平衡所需的时间为15 min。与蒙脱土相比,复合吸附剂具有更高的吸附容量和更快的吸附速率。     

改性沸石处理含铅废水的试验研究

采用沸石为吸附材料,研究其对废水中Pb2+的吸附作用和机理。研究了吸附剂用量、搅拌时间、pH值以及废水浓度等因素对吸附效果影响的探讨。试验结果表明,利用KCl改性后的沸石0.4g,在pH值为8~9的条件下,处理100mL Pb2+质量浓度为10.11mg/L的废水25min,废水中的Pb2+去除率最高可达99.60%,剩余浓度为0.05mg/L,远低于国家污水综合排放标准(GB8978-1996)的一级标准。     

三乙烯四胺改性榴莲壳吸附水溶液中的Cd~(2+)、Pb~(2+)

采用三乙烯四胺改性榴莲壳,制备新型的改性榴莲壳吸附剂,研究其对Cd2+、Pb2+的吸附性能。结果表明,吸附Cd2+、Pb2+的适宜条件为:pH 6.0,吸附时间120 min。改性后榴莲壳吸附剂对Cd2+、Pb2+的吸附容量有了很大程度的提高,Cd2+、Pb2+最大吸附量分别达到39.30、53.76 mg/g。吸附过程可以很好地用准二级动力学方程描述,吸附等温线用Langmuir方程的拟合效果优于Freundlich方程。     

木薯羧甲基淀粉对铜离子的吸附性能

采用搅拌球磨机对木薯淀粉进行机械活化,以活化60 min的木薯淀粉为原料,干法合成羧甲基淀粉吸附剂。考察羧甲基淀粉的取代度、溶液的pH值、Cu2+的初始浓度、吸附时间、羧甲基淀粉的投加量等因素对羧甲基淀粉吸附Cu2+性能的影响。结果表明,该羧甲基淀粉对Cu2+有很好的吸附作用;用取代度为0.841的羧甲基淀粉处理含Cu2+的废水,在pH=7.0、羧甲基淀粉的投加量50.00 mg/L、吸附时间15 min时,羧甲基淀粉对废水中Cu2+的吸附率高达98.80%,处理后的水质达到国家污水综合排放标准(GB8978-1996)中一级标准要求。     

Nanocomposite Silica Aerogel Activated Carbon: Preparation,Characterization and Application to Remove Lead(II) from Aqueous Solutions

Anovel nanocomposite adsorbent, Silica aerogel activated carbon (SA‐AC) has been prepared for the purpose of removing lead ions from aqueous solution in batch process. The nanocomposite was characterized by Fourier transform infrared spectra (FTIR) and scanning electron microscope (SEM). In the present investigation, Pb(II) adsorption experiments on nanocomposite were conducted on aqueous solution at different initial Pb(II) concentration, pH of the solution, adsorption temperature, adsorbent dosage and contact time. Optimum pH for the adsorption was found to be 6 with corresponding adsorbent dosage level of 0.5 g and 60 °C temperature. The equilibriumwas achieved within 30 min of contact time. It is remarkable that using the developed nanocomposite absorbent, more than 90% of Pb(II) can be removed under desirable experimental conditions. The efficiency of the ions adsorption was determined using atomic absorption spectroscopy. Langmuir and Freundlich isotherm models were applied to analyze the experimental data. The best interpretation for the experimental data was given by the Freundlich isotherm equation. Desorption experiments by elution of the adsorbent with nitric acid show that the nanocomposite could be reused without significant losses of its initial properties.     

The starch modified montmorillonite for the removal of Pb(II), Cd(II) and Ni(II) ions from aqueous solutions

In the present study, we attempted to synthesize a novel sorbent from the starch modified montmorillonite for the removal of Pb(II), Cd(II), and Ni(II) ions from aqueous solutions. Structure and properties of the adsorbent were characterized by Fourier-transformed infrared(FT-IR) spectroscopy, X-ray diffraction (XRD), and Field emission scanning electron microscopic (FE-SEM) techniques. Batch experiments were confirmed through the effect of different conditions including pH, contact time, initial metal concentration and adsorbent dose. Specifically, the optimum value of adsorbent dose was achieved as 20 g/l for the removal of almost metal ions. The adsorption data was fitted with the optimum pH value as 5 for all experiments. The contact time at which the uptake of maximum metal adsorption was observed within 45 min for Pb(II), 90 min for Cd(II), and 60 min for Ni(II). In addition, it was revealed in our study that the equilibrium data obeyed the Langmuir model, and the adsorption kinetic followed a pseudo second-order rate model. Obtained results were noticeable for a modified phyllosilicate adsorbent, and with such a simple and low-cost modification for montmorillonite, the potential of this material as an economical and effective adsorbent for the removal of metal ions from aqueous solution was considerably elevated.     

Removal of cadmium(II) and lead(II) ions from model aqueous solutions using sol–gel-derived inorganic oxide adsorbent

A study was conducted concerning the preparation and application of a novel synthetic oxide adsorbent of MgO-SiO₂ type. The material was prepared via a sol–gel route, utilizing magnesium ethoxide and tetraethoxysilane as precursors of magnesium oxide and silica respectively, and ammonia as a catalyst. The powder was comprehensively analyzed with regard to chemical composition (EDS method), crystalline structure, morphology, characteristic functional groups, electrokinetic stability and porous structure parameters (BET and BJH models). The synthesized oxide adsorbent is amorphous, with irregularly shaped particles, a relatively large surface area of 612 m²/g, and negative surface charge over almost the whole pH range. Comprehensive adsorption studies were performed to investigate the adsorption of Cd(II) and Pb(II) ions on the MgO–SiO₂ oxide adsorbent, including evaluation of adsorption kinetics and isotherms, the effect of pH, contact time and mass of adsorbent. It was shown that irrespective of the conditions of the adsorption process, the synthesized MgO–SiO₂ adsorbent exhibits slightly better affinity to lead(II) than to cadmium(II) ions (sorption capacity of 102.02 mg(Pb²⁺)/g and 94.05 mg(Cd²⁺)/g). The optimal time for removal of the analyzed metal ions was 60 min, although adsorption reached equilibrium within 10 min for Pb(II) and within 15 min for Cd(II) ions, which was found to fit well with a type 1 pseudo-second-order kinetic model. Additionally, adsorption efficiency was affected by the pH of the reaction system—better results were obtained for pH ≥7 irrespective of the type of metal ion.     

On-line Preconcentration and Determination of Trace Metals in Water Samples by Flow Injection Combined with Flame Atomic Absorption Spectrometry via Calix[4]arene Carboxylic Acid Packed Micro-column

An adsorbent calix[4]arene carboxylic acid was employed as the adsorption material for on-line flow injection( FI) micro-column preconcentration coupled with flame atomic absorption spectrometry(FAAS) determination of trace heavy metals(Cu, Pb, Co, Ni and Cd). Parameters such as the pH, loading time and flow rate of sample, and the concentration, volume and flow rate of eluent were optimized. The enrichment factors are 50.0, 56.5, 11.6, 12.1 and 19.1 for Cu, Pb, Co, Ni, and Cd, respectively, and a sample throughput of 20 h^-1 was obtained. The limits of detection for Cu, Pb, Co, Ni, and Cd were in a range of 1.56―3.91 μg/L, and the relative standard deviations(RSDs) were less than 2.76%(n=7). Furthermore, the proposed method was successfully applied to the determination of Cu, Pb, Co, Ni, and Cd in certified reference materials and various water samples.     

Highly efficient adsorbents of poly(o-phenylenediamine) solid and hollow sub-microspheres towards lead ions: a comparative study

Two kinds of different-shaped poly(o-phenylenediamine) (PoPD) polymers: solid and hollow sub-microspheres with both size of about 700 nm synthesized by a solution route without any additional directing agents, were employed as efficient adsorbents for removal of Pb(??) ions from water. Firstly, chemical structures of PoPD sub-microspheres were performed by Fourier-transform infrared (FT-IR), UV-vis, (1)H NMR spectra, X-ray diffraction (XRD) and GPC analysis. When used as adsorbents, both PoPD hollow and solid sub-microspheres showed high adsorptivity and adsorption capacity towards Pb(??) ions in water, and mechanisms of adsorption behaviors were revealed by XRD and X-ray photoelectron spectra (XPS). It was found that the pH and concentration of Pb(??) ion solution, as well as contact time and adsorbent dosage affect the degree of adsorption. Adsorption isotherms and kinetics of Pb(??) ions onto PoPD sub-microspheres were also investigated according to experimental data. Comparative investigations of adsorption behaviors revealed that hollow sub-microspheres showed enhanced adsorptivity adsorption capacity towards Pb(??) ions as compared with solid sub-microspheres typical at low adsorbent dosage. PoPD hollow sub-microspheres also showed good adsorptivity for other heavy-metal ions, such as Hg(??), Cd(??) and Cu(??), which implied their potential applications as effective adsorbents for heavy-metal ions in water.     

Preparation and characterization of nanocomposite,silica aerogel,activated carbon and its adsorption properties for Cd (II) ions from aqueous solution

A novel composite adsorbent, silica aerogel activated carbon was synthesized by sol-gel process at ambient pressure drying method. The composite was characterized by Fourier transform infrared spectroscopy (FT-IR), scanning electron microscopy (SEM), differential scanning calorimetry (DSC) and Nitrogen adsorption/desorption isotherms (BET).In the present study, the mentioned adsorbent was used moderately for the removal of cadmium ions from aqueous solutions and was compared with two other adsorbents of cadmium, activated carbon and silica aerogel. The experiments of Cd adsorption by adsorbents were performed at different initial ion concentrations, pH of the solution, adsorption temperature, adsorbent dosage and contact time. Moreover, the optimum pH for the adsorption was found to be 6.0 with the corresponding adsorbent dosage level of 0.1 g at 60 °C temperature. Subsequently, the equilibrium was achieved for Cd with 120 min of contact time.Consequently, the results show that using this composite adsorbent could remove more than 60% of Cd under optimum experimental conditions. Langmuir and Freundlich isotherm model was applied to analyze the data, in which the adsorption equilibrium data were correlated well with the Freundlich isotherm model and the equilibrium adsorption capacity (q_e) was found to be 0.384 mg/g in the 3 mg/L solution of cadmium.     

Adsorption of metal ions onto Moroccan stevensite: kinetic and isotherm studies

The aim of this paper is to study the adsorption of the heavy metals (Cd(II), Cu(II), Mn(II), Pb(II), and Zn(II)) from aqueous solutions by a natural Moroccan stevensite called locally rhassoul. We carried out, first, a mineralogical and physicochemical characterization of stevensite. The surface area is 134 m2/g and the cation exchange capacity (CEC) is 76.5 meq/100 g. The chemical formula of stevensite is Si3.78Al0.22Mg2.92Fe0.09Na0.08K0.08O10(OH)2.4H2O. Adsorption tests of Cd(II), Cu(II), Mn(II), Pb(II), and Zn(II) in batch reactors were carried out at ambient temperature and at constant pH. Two simplified models including pseudo-first-order and pseudo-second- order were used to test the adsorption kinetics. The equilibrium time and adsorption rate of adsorption were determined. The increasing order of the adsorption rates follows the sequence Mn(II) > Pb(II) > Zn(II) > Cu(II) > Cd(II). The Dubinin-Radushkevich (D-R), Langmuir, and Redlich-Peterson (R-P) models were adopted to describe the adsorption isotherms. The maximal adsorption capacities at pH 4.0 determined from the D-R and Langmuir models vary in the following order: Cu(II) > Mn(II) > Cd(II) > Zn(II) > Pb(II). The equilibrium data fitted well with the three-parameter Redlich-Peterson model. The values of mean energy of adsorption show mainly an ion-exchange mechanism. Also, the influence of solution pH on the adsorption onto stevensite was studied in the pH range 1.5-7.0.     

Removal of Cd(II) and Pb(II) from aqueous solution by modified attapulgite clay

Three low-cost adsorbents (purified raw attapulgite (A-ATP), high-temperature-calcined attapulgite (T-ATP), and hydrothermal loading of MgO (MgO-ATP)) were prepared as adsorbents for the removal of Cd(II) and Pb(II). By evaluating the effect of the initial solution pH, contact time, initial solution concentration, temperature and coexistence of metal ions on Cd(II) and Pb(II) adsorption, the experimental results showed that MgO-ATP was successfully prepared by hydrothermal reaction and calcination as well as appearing to be a promising excellent adsorbent. At an initial pH of 5.0, A-ATP, T-ATP and MgO-ATP reached maximum adsorption amounts of 43.5, 53.9 and 127.6 mg/g for Pb(II) and 10.9, 11.2, and 25.3 mg/g for Cd(II) at 298 K, respectively. The Cd(II) adsorption on A-ATP was fitted by the Freundlich model, while the adsorption of Pb(II) and Cd(II) on T-ATP and MgO-ATP as well as Pb(II) adsorption on A-ATP agreed with the Langmuir model. All kinetic experimental data favored pseudo second-order model. The calculated thermodynamic parameters suggested that Pb(II) adsorption onto MgO-ATP was spontaneous and exothermic. When considering foreign metal ions, the three adsorbents all presented preferential adsorption for Pb (II). Chemical adsorption had a high contribution to the removal of Cd(II) and Pb(II) by modified attapulgite. In summary, the adsorption was greatly enhanced by the hydrothermal loading of MgO. It aimed to provide insights into the MgO-ATP, which could be able to efficiently remove Cd(II) and Pb(II) and serve as an economic and promising adsorbent for heavy metal-contaminated environmental remediation.