改性活性炭对亚甲基蓝与Cd~(2+)复合污染物的吸附性能研究

探究改性活性炭对模拟的阳离子染料印染废水亚甲基蓝/Cd⁽²⁺⁾混合溶液的吸附效果及其吸附机理。结果表明,改性活性炭对亚甲基蓝/Cd(2+)混合溶液的吸附效果及其吸附机理。结果表明,改性活性炭对亚甲基蓝/Cd⁽²⁺⁾混合溶液的吸附过程中,亚甲基蓝和Cd(2+)混合溶液的吸附过程中,亚甲基蓝和Cd⁽²⁺⁾存在竞争吸附与静电排斥作用,造成改性活性炭对Cd(2+)存在竞争吸附与静电排斥作用,造成改性活性炭对Cd⁽²⁺⁾的吸附性能降低。改性活性炭对模拟的阳离子染料溶液中两种污染物的吸附符合Langmuir模型,吸附动力学属于准二级动力学模型。对亚甲基蓝和Cd(2+)的吸附性能降低。改性活性炭对模拟的阳离子染料溶液中两种污染物的吸附符合Langmuir模型,吸附动力学属于准二级动力学模型。对亚甲基蓝和Cd⁽²⁺⁾的吸附分别为物理吸附和物理与化学吸附共同作用的单分子层吸附。     

MIL-101的改性及其吸附亚甲基蓝性能研究

金属有机骨架材料作为新兴的材料在很多领域得到了广泛的应用.通过溶剂热法合成了金属有机骨架材料MIL-101,采用3-氨基丙基三乙氧基硅烷对MIL-101进行表面改性,并将改性后的MIL-101用于处理亚甲基蓝染料溶液.考察了3-氨基丙基三乙氧基硅烷用量、水量、反应时间及反应温度对表面改性的影响.改性后的MIL-101对...     

电解二氧化锰对亚甲基蓝和甲基橙染料吸附性能的研究

以电解二氧化锰(EMD)为吸附剂,分析了吸附剂投加量、pH和吸附时间等因素对EMD吸附亚甲基蓝(MB)和甲基橙(MO)的影响;亚甲基蓝是一种典型的阳离子型染料,性质很稳定;甲基橙是一种酸碱指示剂,分子中带有磺酸基-SO3-。结果表明,最佳吸附条件为吸附MB和MO时EMD的最佳用量分别为33.33 g/g和55.56g/g,pH为2、吸附时间为300 min时吸附效果最好。EMD对MB和MO的吸附过程较符合Langmuir等温式和拟二级动力学方程,吸附速率常数分别为0.002 3和0.006 4 g/(mg.min)。EMD对染料的去除机理为吸附和氧化综合作用的结果。     

瓜子壳和花生壳吸附去除亚甲基蓝染料的影响研究

试验以农业固体废弃物花生壳、瓜子壳为生物吸附材料,以亚甲基蓝染料为吸附对象,考察不同条件(如吸附剂用量、溶液pH值和吸附时间等)对亚甲基兰染料吸附效果的影响,结果表明,吸附剂量为2.0 g时,瓜子壳和花生壳对染料的吸附效果较好,均能达到吸附平衡;染料溶液在弱酸或碱性条件下,有利于花生壳和瓜子壳对亚甲基蓝的吸附;花生壳和瓜子壳对亚甲基蓝的吸附均在30 min内达到饱和。而瓜子壳对溶液中亚甲基兰染料的吸附能力要高于花生壳的吸附能力,可作为含亚甲基兰染料印染废水的处理材料。     

用于有机染料废水处理的铜基金属配合物制备及其吸附性能研究

由2-(4-吡啶)-1氢-苯并咪唑(L)和三苯基膦(PPh₃)作为有机配体合成的两例双核铜基金属配合物,Cu₂L₂(PPh₃)₂I₂(1)和Cu₂L₂(PPh₃)₂Br₂(2)及由苯并咪唑基配体-替米沙坦构筑的八核铜金属配合物(3)进行有机染料吸附研究。三例铜配合物在250℃时仍具有较好的热稳定性,对阴离子型染料亚甲基蓝(MB)、阳离子型染料甲基橙(MO)和罗丹明B(RhB)具有不同的吸附能力。其中,配合物3对RhB的吸附能力优于配合物1和2;当RhB和MB在溶液中共存时,配合物3亦表现出优于配合物1和2选择性吸附RhB的性能,具有水处理实际应用的潜力。     

NaOH改性花生壳对亚甲基蓝染料吸附性能的研究

花生壳用5%的NaOH溶液改性作吸附剂处理亚甲基蓝染料废水,考察pH值、吸附剂投加量、染料浓度和温度及吸附时间对染料吸附性能的影响。结果表明,吸附最佳的工艺条件为:温度25℃,吸附剂投加量0.3 g,亚甲基蓝的初始浓度3.5 g/mL,反应时间135 min,pH值7。此时改性花生壳对亚甲基蓝的吸附率达99.57%。     

活性炭对典型染料的吸附性能研究

研究了活性炭对亚甲基蓝、甲基橙、中性红的吸附特性。结果表明,活性炭吸附3种典型染料的qt～t、qe～pH、qe～T曲线趋势基本上是一致的,活性炭对亚甲基蓝染料的吸附能力最强。另外,活性炭对3种染料的吸附行为均符合Langmuir等温吸附和准二级动力学方程,其中,内扩散过程是活性炭吸附亚甲基蓝的速率控制步骤,但不是吸附甲基橙和中性红的速率控制步骤。     

H6P2W18O62/MIL-101(Fe)材料的制备及其吸附性能

采用溶剂热合成法在制备MIL-101(Fe)的过程中引入杂多酸H_6P_2W_(18)O_(62),制备出吸附剂H_6P_2W_(18)O_(62)/MIL-101(Fe),并测试了其对亚甲基蓝(MB)的吸附性能。考察了H_6P_2W_(18)O_(62)的负载量、MB质量浓度、溶液pH、温度等对材料的吸附性能。通过XRD、SEM、FTIR、N2吸附-脱附等手段对材料进行表征。结果表明:吸附平衡前,吸附量随MB质量浓度的增加而增加,在溶液pH=4、H_6P_2W_(18)O_(62)负载量相对于复合物质量分数为35%的条件下,吸附剂H_6P_2W_(18)O_(62)/MIL-101(Fe)对亚甲基蓝溶液吸附效果最佳,在303K下H_6P_2W_(18)O_(62)/MIL-101(Fe)对MB的最大吸附量可达148.1 mg/g。通过动力学和热力学分析,该吸附过程符合拟二级动力学与Langmuir等温吸附模型,同时是一个吸热、自发的过程。     

地质聚合物微球的制备及其对染料的吸附

以偏高岭土和改性水玻璃为原料,采用分散悬浮固化法制备偏高岭土基地质聚合物微球(GM)。使用扫描电子显微镜、比表面积及孔径分布测试仪、傅里叶变换红外光谱仪和X射线粉末衍射仪对其进行了表征,并研究了GM对亚甲基蓝的吸附性能。结果表明,GM对亚甲基蓝的吸附基本符合准二级动力学模型和Langmuir吸附等温线模型,333 K时理论最大吸附量为100.1 mg/g。GM对亚甲基蓝的吸附是自发吸热过程。GM在5次循环利用后,对MB的去除率仍可达81.56%,并易于回收和再生。分析了GM对不同阴阳离子型染料的吸附效果,结果表明,GM对阳离子型染料具有选择性吸附。GM是一种低价、有效、绿色、可循环利用的吸附剂,可用于去除水中阳离子型染料污染物。     

双组分阴离子染料在改性花生壳上的竞争吸附

以接枝法制备得到改性花生壳为吸附剂,研究在酸性橙(AO)和活性艳蓝(KN-R)双组分阴离子染料体系中,改性花生壳对两种染料的吸附去除情况,并通过吸附等温线模型和动力学模型,解析在双组分染料共存条件下,改性花生壳对两种染料的竞争吸附机制。结果表明,在双组分体系中,改性花生壳对AO和KN-R的吸附和单组分体系相似,符合Langmuir等温模型和准二级动力学模型。在反应120 min后,改性花生壳对AO和KN-R的吸附量均小于单组分体系下的吸附量,在溶液pH值为2、初始染料浓度为200 mg/L和温度为298 K的条件下,吸附量分别从243.4、360.9 mg/g降低到140.4、231.3 mg/g,改性花生壳对AO的吸附量下降极为显著,说明两种染料存在竞争吸附,染料分子大且磺胺基含量多的KN-R阻碍改性花生壳对AO的吸附。     

Application of succinylated sugarcane bagasse as adsorbent to remove methylene blue and gentian violet from aqueous solutions - Kinetic and equilibrium studies

In a previous work, succinylated sugarcane bagasse (SCB 2) was prepared from sugarcane bagasse (B) using succinic anhydride as modifying agent. In this work the adsorption of cationic dyes onto SCB 2 from aqueous solutions was investigated. Methylene blue, MB, and gentian violet, GV, were selected as adsorbates. The capacity of SCB 2 to adsorb MB and GV from aqueous single dye solutions was evaluated at different contact times, pH, and initial adsorbent concentration. According to the obtained results, the adsorption processes could be described by the pseudo-second-order kinetic model. Adsorption isotherms were well fitted by Langmuir model. Maximum adsorption capacities for MB and GV onto SCB 2 were found to be 478.5 and 1273.2 mg/g, respectively.     

Adsorption of Anionic and Cationic Dyes from Aqueous Solution on Non-Calcined Mg-Al Layered Double Hydroxide: Experimental and Theoretical Study

Non-calcined Mg-Al layered double hydroxide (LDH) with Mg/Al molar ratio of 3:1 was synthesized using the co-precipitation method. Sorption of anionic (acid blue 25 - AB25, reactive blue 4 - RB4), and cationic (methylene blue - MB) dyes by Mg-Al LDH form aqueous solution was investigated. The effect of solution pH, initial concentration, and contact time were investigated by batch adsorption experiments. The adsorbed amount increases with decrease in pH solution for AB25 and RB4. The cationic dye (MB) solution was insensitive to pH variation and also exhibited a low performance in the kinetic equilibrium studies. While anionic dyes were almost completely extracted from the solution, 90% of the methylene blue remained in solution. The equilibrium data were well described using the Langmuir-Freundlich model for RB4, AB25, and MB dyes with maximum adsorption capacity of 328.90, 246.10, and 43.48 mg/g, respectively. Finally, the mechanism of adsorption involving the dyes and LDH was evaluated using the Monte Carlo approach in the NVT ensemble. The results suggest that molecular simulation can be used to preview quantitatively the dye uptake. Supplemental materials are available for this article. Go to the publisher's online edition of Separation Science & Technology to view the supplemental file.     

Removal of methylene blue from aqueous solution by adsorption onto zeolite synthesized from coal fly ash and its thermal regeneration

BACKGROUND: The removal of cationic dyes from wastewater is of great importance. Three zeolites synthesized from coal fly ashes (ZFAs) were investigated as adsorbents to remove methylene blue (MB), a cationic dye, from aqueous solutions. Experiments were conducted using the batch adsorption technique under different conditions of initial dye concentration, adsorbent dose, solution pH, and salt concentration. RESULTS: The adsorption isotherm data of MB on ZFAs were fitted well to the Langmuir model. The maximum adsorption capacities of MB by the three ZFAs, calculated using the Langmuir equation, ranged from 23.70 to 50.51 mg g^?1. The adsorption of MB by ZFA was essentially due to electrostatic forces. The measurement of zeta potential indicated that ZFA had a lower surface charge at alkaline pH, resulting in enhanced removal of MB with increasing pH. MB was highly competitive compared with Na⁺, leading to only a < 6% reduction in adsorption in the presence of NaCl up to 1.0 mol L^?1. Regeneration of used ZFA was achieved by thermal treatment. In this study, 90–105% adsorption capacity of fresh ZFA was recovered by heating at 450 °C for 2 h. CONCLUSION: The experimental results suggest that ZFA could be employed as an adsorbent in the removal of cationic dyes from wastewater, and the adsorptive ability of used ZFA can be recovered by thermal treatment. Copyright © 2010 Society of Chemical Industry     

Chitosan/polyaniline hybrid for the removal of cationic and anionic dyes from aqueous solutions

Nanostructured chitosan/polyaniline (CH/PANI) hybrid was synthesized via in situ polymerization of aniline in the presence of chitosan. The CH/PANI hybrid was characterized by FTIR spectroscopy, X-ray diffraction, thermogravimetric analysis, and scanning electron microscopy. The CH/PANI hybrid had a nanofibrous structure with an average diameter of 70 nm. This hybrid was employed as an ecofriendly and efficient adsorbent with high adsorption capacity for the removal of Acid Green 25 (AG) and methylene blue (MB) from aqueous solutions. AG and MB were used as anionic and cationic model dyes, respectively. The CH/PANI adsorbent showed high dependence on the pH of the medium with an excellent adsorption performance and regeneration manner. The kinetics and adsorption isotherms were studied. The CH/PANI hybrid follows the pseudo second-order adsorption kinetics and Temkin isotherm model for the adsorption of both AG and MB dyes. This assumes that the enthalpy of dyes molecules decreases with the adsorption on heterogeneous surface with various kinds of adsorption sites and as well as the ability to form multilayers of the dye. Also, intraparticle diffusion was found to play an important role in the adsorption mechanism. The maximum adsorption capacity was found to be 240.4 mg g⁻¹ of AG at pH 4 and 81.3 mg g⁻¹ of MB at pH 11. © 2018 Wiley Periodicals, Inc. J. Appl. Polym. Sci. 2019 , 136, 47056.     

High-Efficiency Sorbent for Dyes Based on Cellulose Resin Crosslinked with Perylene Tetracarboxylic Diimides

The novel cellulose resin crosslinked with perylene tetracarboxylic diimides 3 was synthesized and its structure was characterized by elemental analysis, Fourier transform infrared (FTIR) spectroscopy, and scanning electronmicroscopy (SEM), etc. Dyes adsorption experiments of polymer 3 suggested that it exhibited excellent adsorption capacities for tested four cationic and anionic dyes [Orange G sodium salt (OG), Brilliant ponceau 5R (BP), Methylene blue (MB), and Crystal violet (CV)]. The adsorption capacities for OG, BP, MB, CV were as high as 1.04, 1.21, 1.14, and 0.96 mmol/g, respectively. The adsorption processes obeyed the pseudo second-order model and followed the Langmuir isotherm equation. The adsorption processes were exothermic and spontaneous. The pH = 2 ? 12 made slight influences on adsorption capacities of polymer 3 for dyes. It was supposed that the adsorption mechanism was not only the electrostatic forces and hydrogen bond but also the π-π stacking interaction playing an important role in the adsorption processes.     

The adsorptive properties of UiO-66 towards organic dyes: A record adsorption capacity for the anionic dye Alizarin Red S.

In order to decisively determine the adsorption selectivity of zirconium MOF(UiO-66) towards anionic versus cationic species, the adsorptive removal of the anionic dyes(Alizarin Red S.(ARS), Eosin(E), Fuchsin Acid(FA)and Methyl Orange(MO)) and the cationic dyes(Neutral Red(NR), Fuchsin Basic(FB), Methylene Blue(MB),and Safranine T(ST)) has been evaluated. The results clearly reveal a significant selectivity towards anionic dyes. Such an observation agrees with a plethora of reports of UiO-66 superior affinity towards other anionic species(Floride, PO_4~(3-), Diclofenac sodium, Methylchlorophenoxy-propionic acid, Phenols, CrO_4~(2-), SeO_3~(2-), and AsO_4~-). The adsorption process of ARS as an example has been optimized using the central composite design(CCD). The resultant statistical model indicates a crucial effect of both pH and sorbent mass. The optimum conditions were determined to be initial dye concentration 11.82 mg.L~(-1), adsorbent amount 0.0248 g, shaking time of 36 min and pH 2. The adsorption process proceeds via pseudo-second order kinetics(R~2= 0.999). The equilibrium data were fit to Langmuir and Tempkin models(R~2= 0.999 and 0.997 respectively). The results reveal an exceptional removal for the anionic dye(Alizarin Red S.) with a record adsorption capacity of400 mg·g~(-1). The significantly high adsorption capacity of UiO-66 towards ARS adds further evidence to the recently reported exceptional performance of MOFs in pollutants removal from water.     

The Binding of Anionic Dyes by Cross-Linked Cationic Starches

Adsorption of anionic dyes on the cross-linked with epichlorohydrin starches containing quaternary ammonium groups (CCS) was investigated and compared with that of modified starches containing only quaternary ammonium groups (CS). The adsorption of anionic dyes on CS and CCS closely follows the Langmuir model of adsorption. The computed Langmuir saturation capacity Q _o increases with increasing degree of substitution (DS) of CS or CCS and has the value from 0.81 mol/kg to 3.22 mol/kg for CCS and from 0.88 mol/kg to 1.87 mol/kg for CS. The effectiveness of the cationic groups in dye binding was about 1 mol/equiv for CSS with DS from 0.47 to 0.62 and all the cationic groups had attached one anionic groups of the dye. Increasing DS of CS decreases the effectiveness of dye binding due to the increase in solubility of CS, and the soluble part of CS binds the dye as a typical soluble polyelectrolyte. CCS are more suitable than CS for the anionic dye adsorption from a textile dyeing solution. DS of CCS should be about 0.5–0.6. They adsorb the anionic dyes in few minutes and acts in the wide range of pH of the solutions. The Langmuir saturation capacity Q _o and the effectiveness of the cationic groups in dye binding increase with an increase of the adsorption temperature. The positive values of the enthalpy and entropy suggest that the adsorption is endothermic and during the adsorption of the anionic dye on CCS the randomness of the system increases.     

Removal of Selected Basic Dyes using Activated Carbon from Tannery Wastes

Activated carbon prepared from tannery leather waste (TLW-AC) has been studied for its efficiency of removal of basic dyes, namely rhodamine B (RB), methylene blue (MB), and malachite green (MG) from aqueous solutions. Factors influencing dye adsorption such as the concentration of dye, pH, contact time, and temperature were investigated. The adsorption was found to be strongly dependent on the pH and temperature. The maximum sorption capacity of RB was obtained at pH 3 and for MB and MG was obtained at pH 11. Various thermodynamic parameters such as ΔG°, ΔH°, and ΔS° were calculated. The kinetic studies reveal that the adsorption process follows the pseudo second-order kinetic model. The equilibrium data have been well-described by the Langmuir and Freundlich models, and the data fitted well in both model equations. The study revealed that wastes from leather industry is an economically viable option for dye removal.     

Adsorption of selected dyes on Ti3C2Tx MXene and Al-based metal-organic framework

MXene and metal organic framework (MOF) were used as the main adsorbents to remove synthetic dyes from model wastewater. Methylene blue (MB) and acid blue 80 (AB) were used as the model cationic and anionic synthetic dyes, respectively. To investigate the physicochemical properties of the adsorbents used, we carried out several characterizations using microscopy, powder X-ray diffraction, a porosimetry, and a zeta potential analyzer. The surface area of MXene and MOF was 9 and 630 m² g⁻¹, respectively, and their respective isoelectric points were approximately pH 3 and 9. Thus, MXene and MOF exhibited high capacity for MB (~140 mg g⁻¹) and AB (~200 mg g⁻¹) adsorption, respectively due to their electrostatic attractions when the concentrations of the adsorbents and adsorbates were 25 and 10 mg L⁻¹. Furthermore, the MOF was able to capture the MB due mainly to hydrophobic interactions. In terms of the advantages of each adsorbent according to our experimental results, MXene exhibited fast kinetics and high selectivity. Meanwhile, the MOF had a high adsorption capacity for both MB and AB. The adsorption mechanisms of both adsorbents for the removal of MB and AB were clearly explained by the results of our analyses of solution pH, ionic strength, and the presence of divalent cation, anion, or humic acids, as well as other characterizations (i.e., Fourier-transform infrared spectroscopy and X-ray photoelectron spectroscopy). According to our results, MOF and MXene can be used as economical treatments for wastewater containing organic pollutants regardless of charge (e.g., MB and AB), and positively charged one (e.g., MB), respectively.