Use of chemically activated cotton nut shell carbon for the removal of fluoride contaminated drinking water:Kinetics evaluation☆

Chemically activated cotton nut shell carbons (CTNSCs) were prepared by different chemicals and they were used for the removal of fluoride from aqueous solution. Effects of adsorption time, adsorbent dose, pH of the solution, initial concentration of fluoride, and temperature of the solution were studied with equilibrium, ther-modynamics and kinetics of the adsorption process by various CTNSC adsorbents. It showed that the chemical y activated CTNSCs can effectively remove fluoride from the solution. The adsorption equilibrium data correlate well with the Freundlich isotherm model. The adsorption of fluoride by the chemical y activated CTNSC is spon-taneous and endothermic in nature. The pseudo first order, pseudo second order and intra particle diffusion kinetic models were applied to test the experimental data. The pseudo second order kinetic model provided a better correlation of the experimental data in comparison with the pseudo-first-order and intra particle diffusion models. A mechanism of fluoride adsorption associating chemisorption and physisorption processes is presented allowing the discussion of the variations in adsorption behavior between these materials in terms of specific surface area and porosity. These data suggest that chemically activated CTNSCs are promising materials for fluoride sorption.     

Characteristics of Amine Surfactant Modified Peanut Shell and Its Sorption Property for Cr（VI）

Modified peanut shell （MPS） was prepared by amination reaction with peanut shell （PS） as the starting material The sorption of Cr（VI） oxyanions on MPS in static and column tests were investigated. In addition, the sorption isotherm and kinetic models were applied to confirm the sorption capacity and the sorption mechanisms. BET surface area anysis showed the physicochemical characterist!cs of the samples. The results of zeta potential,Fourier transform infrared （FT-IR） and Raman spectra analysis illustrated that chemical adsorption and ion exi change are the potential sorption mechanism. The static sorption test showed that the maximum sorption capacity （qm） of MPS for Cr（VI） increased with temperature, which indicated that the Cr（VI） sorption rocess was endothermic. The saturated sorption capacity of Cr（VI） in the colunm sorption test was 138.34 mg.g-1, which accounted for 93.9% of the qmax at 25 ℃. The regeneration capacity of MPS was evaluated using HC1 solution as an eluent. The high regeneration efficiency （82.6%） validated the dominance of the ion exchange mechanism in the Cr（VI） sorption process with C1ions displacing Cr（VI） oxyanion on MPS. The Langmuir isotherm model showed a higher correlation coefficient than the other adsorption isotherm models. And in the kinetic study, a pseudo-second-order model fit the data best.     

Ghezeljeh nanoclay as a new natural adsorbent for the removal of copper and mercury ions:Equilibrium,kinetics and thermodynamics studies

Heavy metal determination was carried out by applying the solid phase extraction (SPE) method in batch mode followed by atomic absorption spectroscopy (AAS) and inductively coupled plasma atomic emission spectrosco-py (ICP-AES) from aqueous solutions using Ghezeljeh montmoril onite nanoclay as a new natural adsorbent. The Ghezeljeh clay is characterized by using Fourier Transform Infrared (FT-IR) Spectroscopy, Scanning Electron Mi-croscopy–Energy Dispersive Spectrometry (SEM–EDS) and X-ray Diffractometry (XRD) and X-ray Fluorescence (XRF). The results of XRD and FT-IR of nanoclay confirm that montmoril onite is the dominant mineral phase. Based on SEM images of Ghezeljeh clay, it can be seen that the distance between the plates is Nano. The effects of varying parameters such as initial concentration of metal ions, pH and type of buffer solutions, amount of ad-sorbent, contact time, and temperature on the adsorption process were examined. The effect of various interfer-ing ions was studied. The adsorption data correlated with Freundlich, Langmuir, Dubinin–Radushkevich (D–R), and Temkin isotherms. The Langmuir and Freundlich isotherms showed the best fit to the equilibrium data for Hg(I ), but the equilibrium nature of Cu(II) adsorption has been described by the Langmuir isotherm. The kinetic data were described with pseudo-first-order, pseudo-second-order and double-exponential models. The adsorp-tion process follows a pseudo-second-order reaction scheme. Calculation ofΔG0,ΔH0 andΔS0 showed that the nature of Hg(II) ion sorption onto the Ghezeljeh nanoclay was endothermic and was favored at higher temper-ature, and the nature of Cu(II) ion sorption was exothermic and was favored at lower temperature.     

交联氧化铝-壳聚糖新杂化吸附剂的制备及去除废水中Cu(Ⅱ)(英文)

A novel biosorbent was developed by coating chitosan,a naturally and abundantly available biopolymer,on to activated alumina based on oil shale ash via crosslinking.The adsorbent was characterized by various techniques,such as Fourier transform infrared spectroscopy,scanning electron microscopy,thermogravimetric-differential thermal analysis,and X-ray photoelectron spectroscope.Batch isothermal equilibrium adsorption experiments were condcted to evaluate the adsorbent for the removal of Cu(Ⅱ) from wastewater.The effect of pH and agitation time on the adsorption capacity was also investigated,indicating that the optimum pH was 6.0.The equilibrium adsorp-tion data were correlated with Langmuir and Freundlich models.The maximum monolayer adsorption capacity of chitosan coated alumina sorbent as obtained from Langmuir adsorption isotherm was found to be 315.46 mg·g-1 for Cu(Ⅱ).The adsorbent loaded with Cu(Ⅱ) was readily regenerated using 0.1 mol?L?1 sodium hydroxide solution.All these indicated that chitosan coated alumina adsorbent not only have high adsorption activity,but also had good stability in the wastewater treatment process.     

超重力旋转填料床中柠檬酸钠缓冲液吸收二氧化硫(英文)

Absorption of SO2 from a SO2/air mixture with sodium citrate buffer solution was investigated using a rotating packed bed(RPB) in laboratory scale.The effects of operating parameters,such as the rotation speed of RPB,liquid-gas ratio,inlet gas flow rate,inlet concentration of SO2 in flue gas,sodium citrate buffer concentration and initial pH of absorption solution,on the SO2 concentration in the absorption solution or removal efficiency of SO2 were examined.Incremental rate of sulfate radical ions in the absorption solution was also examined.Experimental results indicate that the efficiency of this regenerative process will be improved by using RPB under appropriate operating conditions,and the generation of SO2-4 will be restrained in the process in RPB.     

Sorption and Diffusion Behavior of Carbon Dioxide into Poly（l-lactic acid） Films at Elevated Pressures

Equilibrium sorption amount, desorption diffusion coefficients and sorption diffusion coefficients of CO2 in poly（l-lactic acid） （PLLA） films at elevated pressures were determined by the gravimetric method, in which the Fick＇s diffusion model was applied to analyze both the desorption and sorption processes. The equilibrium sorption amount of CO2 in PLLA increased with lowering temperature and elevating pressure at the temperature range from 40 to 60 ℃ and pressure from 10^4 to 2x10^4 kPa. Desorption diffusion coefficients were greatly influenced by the equilibrium sorption amount, and they were in the same order of magnitude as the sorption diffusion coefficients. The scan electron microscope （SEM） photos demonstrated that there was no foaming phenomenon of the PLLA film during desorption and sorption processes. The XRD spectra implied that the crystalline degree of PLLA film decreased after CO2 processing. It was concluded that PLLA polymer could be well swollen and plasticized by supercritical CO2.     

锰氧化物负载沸石固定床离子交换柱去除铀(VI)的研究

The adsorption of uranium (VI) on the manganese oxide coated zeolite (MOCZ) from aqueous solution was investigated in a fixed-bed column. The experiments were conducted to investigate the effects of bed height, flow rate, particle size, initial concentration of uranium (VI), initial pH, presence of salt and competitive ions. The U-uptake by MOCZ increased with initial uranium (VI) concentration and bed height, but decreased as the flow rate and particle size increased. In the presence of salt and competitive ions, the breakthrough time was shorter. The ad-sorption capacity reached a maximum at pH of 6.3. The Thomas model was applied to the experimental data to de-termine the characteristic parameters of the column for process design using linear regression. The breakthrough curves calculated from the model were in good agreement with the experimental data. The BDST model was used to study the influence of bed height on the adsorption of uranium (VI). Desorption of uranium (VI) in the MOCZ column was investigated. The column could be used for at least four adsorption-desorption cycles using 0.1 mol•L－1 NaHCO3 solution as the elution. After desorption and regeneration with deionized water, MOCZ could be reused to adsorb uranium (VI) at a comparable capacity. Compared to raw zeolite, MOCZ showed better capacity for uranium (VI) removal.     

Simultaneous removal of copper and zinc ions by low cost natural snail shell/hydroxyapatite/chitosan composite

In this work, the snail shell/hydroxyapatite/chitosan composite was prepared as adsorbent. The adsorption potential of the composite was studied for simultaneous sorption behavior of Zn(Ⅱ) and Cu(Ⅱ) ions in a batch system. Chitosan and hydroxyapatite(HAP) were extracted from shrimp shell and bone ash,respectively, so this is a low cost natural composite. To prepare the composite, chitosan was dissolved in acetic acid, then HAP and snail shell powders were added to the chitosan solution. The morphology and characterization of the composite was studied by SEM and EDX analysis. Atomic adsorption was used to measure the amount of the ions. Experimental parameters were optimized with Design Expert Software and five parameters such as the concentration of ions, p H, adsorbent amount and contact time were studied at room temperature. Optimized value for the parameters of Zn(Ⅱ) and Cu(Ⅱ) concentrations, p H, adsorbent dose, and contact time were 3.01 mg·L~(-1), 5.5, 0.02 g and 95 min, respectively. The adsorption isotherms for Zn(Ⅱ) and Cu(Ⅱ) showed Langmuir and Tempkin, respectively. Kinetic and equilibrium studies showed the experimental data of Zn(Ⅱ) and Cu(Ⅱ) ions were best described by the pseudo-second-order model. Studies on thermodynamic show the adsorption process were physical and spontaneous.     

累托石吸附分离水中金霉素(英文)

The removal of antibiotics from water by clay minerals has become the focus of research due to their strong adsorptive ability. In this study, adsorption of chlortetracycline (CTC) onto rectories was conducted and the effects of time, concentration, temperature and pH were investigated. Experimental results showed that adsorption equilibrium was reached in 8 h. Based on the Langmuir model, the maximum adsorption capacity of CTC on rectories was 177.7 mg·g 1 at room temperature. By the study on adsorption dynamics, it is found that the kinetic date fit the pseudo-second-order model well. The adsorption of CTC by rectories is endothermic and the free energy is in the range of 10 to 30 kJ·mol 1 . The pH value of solution has significant effects on adsorption and the optimal pH is at acidity (pH 2-6). At concentration of 2500 mg·L 1 , the intercalated CTC produces an interlayer space with a height of 1.38 nm, which is 1.12 nm in raw rectories, suggesting that the adsorption occurs between layers of rectories.     

Dowex50W-X树脂吸附硫酸溶液中的锶

In this study,strontium adsorption from sulfuric acid solution by different Dowex 50W-X ion exchange resins was investigated.Among these resins,Dowex 50W-X8 resin showed the maximum sorption of strontium from the aqueous solutions.The effect of pH,contact time,mass of resin,temperature,and concentration of interfering ions on strontium adsorption were evaluated to determine the optimum conditions of strontium sorption process.The kinetic models of sorption were analyzed using pseudo-first and pseudo-second order models.The results indicated that the pseudo-second order kinetic model was more appropriate than the other one.Moreover,the data obtained in this study were fitted into several sorption isotherm models and it was found that the Langmuir sorption isotherm shows the best fitting to the experimental data.     

Green synthesis of nickel nanoparticles using Ocimum sanctum and their application in dye and pollutant adsorption

Nickel nanoparticles as an eco-friendly adsorbent was biosynthesized using Ocimum sanctum leaf extract. The phys-iochemical properties of green synthesized nickel nanoparticles (NiGs) were characterized by UV–Vis spectroscopy (UV–Vis), Fourier Transform Infrared Spectroscopy (FTIR), X-ray diffraction (XRD), Scanning Electron Microscope (SEM) and Transmission Electron Microscope (TEM). NiGs were used as adsorbent for the removal of dyes such as crystal violet (CV), eosin Y (EY), orange I (OR) and anionic pol utant nitrate (NO3?), sulfate (SO42?) from aqueous solution. Adsorption capacity of NiGs was examined in batch modes at different pH, contact time, NiG dosage, initial dye and pol utant concentration. The adsorption process was pH dependent and the adsorption capacity increased with increase in contact time and with that of NiG dosage, whereas the adsorption capacity decreased at higher con-centrations of dyes and pol utants. Maximum percentage removal of dyes and pol utants were observed at 40, 20, 30, 10 and 10 mg·L?1 initial concentration of CV, EY, OR, NO3?and SO42?respectively. The maximum adsorption capacities in Langmuir isotherm were found to be 0.454, 0.615, 0.273, 0.795 and 0.645 mg·g?1 at pH 8, 3, 3, 7 and 7 for CV, EY, OR, NO3?and SO42?respectively. The higher coefficients of correlation in Langmuir isotherm sug-gested monolayer adsorption. The mean energies (E), 2.23, 3.53, 2.50, 5.00 and 3.16 kJ·mol?1 for CV, EY, OR, NO3?and SO42?respectively, calculated from the Dubinin–Radushkevich isotherm showed physical adsorption of adsor-bate onto NiGs. Adsorption kinetics data was better fitted to pseudo-second-order kinetics with R2 N 0.870 for al dyes and pol utants. NiGs were found to be an effective adsorbent for the removal of dyes and pol utants from aque-ous solution and can be applied to treat textile and tannery effluents.     

A222型阴离子交换树脂脱除HPPH+体系中的SO42-、NO3-

优化选取凝胶型强碱性苯乙烯系A222型阴离子交换树脂,对HPPH⁺溶液中SO₄^2-、NO₃^-的交换性能进行了研究。通过静态法分别考察了A222型阴离子交换树脂在水溶液及0.05mol/L HPPH⁺溶液中对SO₄^2-和NO^3-脱除过程。结果表明,A222型阴离子交换树脂对HPPH⁺无化学吸附作用,在水体系中对SO₄^2-和NO₃^-的平衡交换量分别为0.8382mmol/g和1.2980mmol/g,符合Langmuir和Freundlich吸附经验方程。树脂用量和温度是离子交换过程的主要影响因素,温度升高有利于离子交换的进行,树脂的优化用量为4g/L。A222型阴离子交换树脂可高效联合脱除HPPH⁺体系中的SO₄^2-和NO₃^-。FTIR谱图表征显示,SO₄^2-和NO₃^-可与树脂交换基团进行交换。     

反离子对部分电荷中和的聚乙烯亚胺接枝介质的蛋白质色谱行为的影响

前期研究表明部分电荷中和的聚乙烯亚胺接枝琼脂糖介质FF-PEI-R440具有较高静态吸附容量和快速传质速率。本文选取硫氰酸根离子、氯离子、磷酸氢根离子以及硫酸根离子这4种反离子,在离子强度为0.03、0.06 mol·L^-1下,研究其对FF-PEI-R440吸附与洗脱行为的影响。结果表明：在两种离子强度下,饱和吸附容量的增加顺序均为SCN^- < SO₄^2- < HPO₄^2- < Cl^-;在低离子强度下,除SCN^-外,反离子种类对传质速率和动态结合容量没有显著影响;在高离子强度下,传质速率的增加顺序为SCN^- < SO₄^2- ≈ Cl^- < HPO₄^2-,而动态结合容量的增加顺序与饱和吸附容量序列一致;两种离子强度下Cl^-均保持最高的动态结合容量;反离子种类对蛋白质洗脱行为没有显著影响。上述结果说明反离子主要影响FF-PEI-R440的吸附性能,而不影响洗脱,且流动相中选择Cl^-为反离子最利于FF-PEI-R440的实际柱色谱操作。     

Separation of mixed salts(Cl~-/SO_4~(2-)) by ED based on monovalent anion selective membranes

The industrial products or wastewater rich in the mixed salts(Cl~-/SO_4~(2-)) not only causes the environmental damage, but also induces waste of resource. In this study, an ED stack with monovalent selective AEMs and conventional CEMs was employed to separate the Cl~-and SO_4~(2-)from simulated wastewater. The effect of current density and mass fraction percentage was investigated in order to optimize the experimental conditions during ED process. It was found that at a concentration ratio between NaCl and Na_2SO_4 of 95/5(wt%/wt%) and a current density of40 m A·cm~(-2), a current efficiency of 72%, an energy consumption of 1.6 k W·h·kg~(-1) Na Cl and a Cl~-/SO_4~(2-)concentration(67.5/3.5 g·L~(-1)) were obtained. Hence, it is appropriate and effective to separate Cl~-and SO_4~(2-)by ED using the monovalent selective AEMs.     

电絮凝-半短程硝化-厌氧氨氧化组合工艺处理裂化催化剂废水

裂化催化剂生产过程中产生的高盐度、高浊度、高氨氮、低C/N比废水难以处理。构建了电絮凝-半短程硝化-厌氧氨氧化组合工艺,考察了该组合工艺对实际裂化催化剂废水的处理效果以及处理稳定性。结果表明组合工艺处理裂化催化剂废水具有较好的稳定性,出水水质稳定在以下水平:浊度< 30 NTU,NH₄⁺-N< 10 mg·L^-1,NO₂^--N< 3 mg·L^-1, NO₃^-< 40 mg·L^-1,COD< 100 mg·L^-1;通过进水氨氮浓度确定曝气时间的方式可以保证长期稳定的半短程硝化过程,出水NO₂^-/NH₄⁺-N比值维持在0.9～1.4之间,满足厌氧氨氧化反应器的进水要求;同时在裂化催化剂废水的高盐度胁迫下厌氧氨氧化工艺能够表现出显著的厌氧氨氧化效果。     

硫酸根对聚合氮化碳光催化活性的影响

在pH=1条件下分别加入硫酸根、硝酸根、磷酸根对三聚氰胺进行处理,采用高温煅烧法制备了一系列聚合氮化碳材料,并通过X射线衍射（XRD）、扫描电子显微镜（SEM）、紫外-可见漫反射光谱（UV-Vis DRS）等分析手段对样品进行了表征。以罗丹明B（RhB）为污染物,探究了在可见光下聚合氮化碳对RhB的光催化降解性能、稳定性以及降解机理。加入0.12 mol硫酸根处理的聚合氮化碳（CN-0.04SO₄^2-）在45 min内对RhB的降解率为99.1%,其伪一级动力学常数是未加硫酸根的23.0倍,硫酸根能有效地增强聚合氮化碳的光催化活性。CN-0.04SO₄^2-经过3次循环实验对RhB的降解率略有下降,说明其具有良好的稳定性。活性物种捕获实验表明,影响光催化降解RhB的主要活性物种是·O₂^-和·OH。     

一步法制备Mg改性玉米芯生物炭吸附磷酸盐研究

研究通过MgCl2溶液浸泡玉米芯后在450℃下慢速热解1 h 一步法制备获得Mg改性生物炭(Mg-BC),探究其对磷酸盐的吸附和影响因素.结果表明,Mg-BC吸附磷符合准1级、准2级动力学模型,说明吸附过程主要受物理、化学作用控制.Mg-BC对磷的等温吸附符合Langmuir方程,吸附类型为单分子层吸附,最大吸附量为5...     

粉煤灰源C-S-H吸附U(Ⅵ)性能及机理

以粉煤灰铝回收过程的脱硅液为原料,通过控制钙硅摩尔比的常规沉淀法制备得到大比表面积介孔C-S-H（401 m²·g^-1）,系统研究了初始浓度、投加量、pH和离子强度对C-S-H吸附U（Ⅵ）过程的影响,以及吸附的热动力学特征,并评价了C-S-H去除实际含铀废水中毒性金属的性能。结果表明,通过控制合成条件实现了低品质硅钙渣向高附加值吸附材料的转变。0.75 g·L^-1 C-S-H在pH 2仍具有较高的平衡吸附容量（q_e=67.9 mg·g^-1）,在富含CO₃^2-的碱性溶液中UO₂（H₂O）₅²⁺转变为UO₂（CO₃）₃^4-不利于带负电的C-S-H表面吸附U（Ⅵ）。当C-S-H投加量升高至2～5 g·L^-1,材料对U（Ⅵ）的吸附去除效率即能维持在相对较高水平（C[U（Ⅵ）]_initial=500 mg·L^-1,去除率88.3%～93.5%）,吸附可在数小时内达到平衡,符合拟二级动力学模型和两阶段Weber-Morris方程模型,吸附等温线符合Langmuir模型,吸附机理主要为离子交换（84.6%）和表面络合。材料对含铀废水中的U、Zn、Hg、Mn和Cd均表现出良好的吸附去除性能,因而C-S-H可成为在废水毒性金属去除方面极具应用前景的材料。     

CoCo-PBA@ CuFe-LDH活化过一硫酸盐降解阿特拉津

为了有效降解废水中的阿特拉津(ATZ),采用共沉淀法将钴基-普鲁士蓝类似物(CoCo-PBA)负载于层状双金属氢氧化物CuFe-LDH上,制得复合材料CoCo-PBA@ CuFe-LDH,用于活化过一硫酸盐(PMS)降解ATZ.通过考察降解过程的主要影响因素,发现提高催化剂CoCo-PBA@ CuFe-LDH 用量和反...     

短程硝化过程中NO_2~-对NH_4~+及NH_2OH氧化产生N_2O的影响

N2O是一种强效的温室气体,而污水生物脱氮过程是N2O产生的一个主要人为来源。在本研究中,向生物处理出水中投加NH+4、NH2OH及NO-2,研究了NO-2对NH+4及NH2OH氧化过程中N2O产生的影响。试验结果表明,NH+4及NH2OH氧化过程的最初30 min内(总反应时间180 min)产生的N2O占总N2O产生量的25%以上。在NH4+或NH2OH氧化完成前的30 min内,N2O的净产生量仅有0.2 mg·L-1。NH2OH的氧化是短程硝化开始阶段产生N2O的途径,此后NH+4或NH2OH氧化为AOB提供还原NO-2电子,引起的反硝化作用是产生N2O的主要途径。在实际生活污水短程硝化试验过程中,由于部分COD的存在,在低氧条件下,可能会出现异养菌的反硝化作用。同时,由于氧气及NO-2对氧化亚氮还原酶(NOS)的抑制,使得在生活污水进行短程硝化时,N2O的净产量比上述出水试验时增加了17%以上,总产量最高达到了11.07 mg·L-1。这一途径对N2O产生的贡献也是不容忽视的。