羧甲基壳聚糖微球对曙红Y的吸附研究

以壳聚糖粉末为原料,戊二醛进行交联、羧甲基化,制得羧甲基壳聚糖微球。采用SEM对壳聚糖微球的形貌、大小进行了表征,研究羧甲基壳聚糖微球对曙红Y的吸附性能。探讨吸附剂用量、吸附时间、曙红Y的初始浓度、pH、温度对脱色率的影响,研究吸附等温曲线和动力学方程。实验结果表明,曙红Y初始浓度增加时,吸附量也增加,直到吸附饱和,羧甲基壳聚糖的饱和吸附量为75 mg/g;相同条件下,吸附剂用量增加时,平衡吸附量减小,去除率增加。298 K,吸附剂投加量为1 g,pH=7.0,吸附时间为40 min时,初始浓度为560 mg/L的曙红Y染料的去除率可以达到90%以上。符合Langmuir等温方程和二级吸附动力学方程。     

焙烧层状氢氧化镁铝吸附脱除水中苯酚的研究

用层状氢氧化镁铝的焙烧产物吸附水中苯酚,研究了吸附剂用量、吸附时间、温度、溶液pH值等条件对吸附性能的影响。结果表明,吸附主要发生在90min内,吸附量随着温度的升高而增加。溶液初始pH值对吸附影响较大,pH值在6～11范围内吸附效果较酸性时好。吸附符合Langmiur等温线,饱和吸附量为0.557mg/g。     

粉煤灰滤料对水中Ni^2＋的吸附研究

通过静态吸附试验,研究了粉煤灰滤料对水中Ni^2＋的吸附作用,探讨了吸附剂投加量、吸附时间、溶液pH值以及初始浓度对Ni^2＋吸附效果的影响,拟合了吸附等温线。结果表明,当粉煤灰滤料投加量为30g／L,溶液初始浓度为10mg／L,pH=7时,在30℃、180r／min的转速条件下振荡90min,Ni^2＋的去除率可达到95．2％。经过拟合,粉煤灰滤料对水中Ni^2＋的吸附符合Freundlich和Langmuir吸附等温模型。     

麦饭石负载壳聚糖对As(V)的吸附性能研究

利用麦饭石负载壳聚糖制备一种复合吸附剂。研究了复合壳聚糖对As(V)的吸附。结果表明:在pH值为4～7,吸附时间为40min,复合壳聚糖对As(V)的去除率达99%以上,残余As(V)浓度低于国家综合排放标准(0.5mg/L)。通过对实验数据运用相关数学模型拟合,表明复合壳聚糖对As(V)的吸附符合Langmuir和Freundlich吸附等温式,最大吸附量qmax为39.1850mg/g,n为4.7902,相关系数分别为:0.9967、0.9489。吸附过程动力学适合二级动力学方程。     

污泥基生物炭处理酸性含U(Ⅵ)废水的效能与机理

通过城市污泥（SS）慢速热解制备污泥基生物炭（SSB），并研究初始pH、投加量、共存离子、吸附时间和温度等因素对SSB去除U(Ⅵ)的影响，探讨吸附动力学和吸附等温线特征。通过元素分析、扫描电镜（SEM）、傅里叶红外光谱（FTIR）、X射线衍射（XRD）和X射线光电子能谱（XPS）分析U(Ⅵ)吸附去除的机理。结果表明SSB去除U(Ⅵ)的适宜条件为：pH=3、投加量1 g/L、吸附时间240 min；在此条件下，在温度30℃时最大吸附量为34.51 mg/g。吸附动力学符合拟二级动力学模型；Langmuir吸附等温模型能更好描述生物炭对U(Ⅵ)的吸附行为。U(Ⅵ)吸附去除机理主要包括静电作用，与Si—O—Si的n-π相互作用，与羟基（—OH）、羧基（—COOH）的配位络合。通过5次吸附-解吸试验发现，U(Ⅵ)去除率和SSB再生率均在80%以上。本研究表明污泥基生物炭具备处理与修复酸性含U(Ⅵ)废水污染的潜力。     

胞外聚合物对水中Cu~(2+)的吸附研究

以胞外聚合物作为生物吸附剂,对水中微量Cu2+的生物吸附特性进行研究,分析了原始pH值、胞外聚合物投加量、吸附时间对Cu2+吸附去除率的影响。研究结果表明:当初始Cu2+的质量浓度为10mg/L时,吸附最佳原始pH值范围为2～5,胞外聚合物的投加量为16mg/g,吸附时间为40min。Cu2+的吸附过程可分为3个阶段:①8min的快速吸附阶段;②8～40min达表观一级动力学吸附阶段;③吸附-解吸平衡阶段。Cu2+吸附等温线与Freundilich方程拟合良好。     

疏水性MCM-41分子模板剂对水中U(VI)的吸附性能试验研究

采用水热合成法制备了疏水性介孔二氧化硅材料(MCM-41-dry)并经煅烧制得亲水性介孔二氧化硅材料(MCM-41-cal).试验探讨了pH值、吸附时间、投加量以及U(VI)初始浓度等因素对MCM-41材料煅烧前后吸附U(VI)效果的影响,利用SEM、EDS、BET和FTIR分析其吸附机理.试验结果表明, MCM-41-dry材料因具有有机模板剂,其吸附效果远高于MCM-41-cal的吸附效果;当pH值为5,吸附时间为180 min,温度为30 ℃,MCM-41-dry投加量为0.2 g/L,U(VI)初始浓度为10 mg/L时,其对U(VI)的吸附率可达99.2%;Langmuir吸附等温模型和准二级动力学方程能较好的拟合其吸附过程,当T=303 K时,理论饱和吸附量为241.935 mg/g,吸附为单分子层吸附,以化学吸附为主.通过BET、FTIR表征则说明MCM-41-dry具有六方形介孔结构能吸附U(VI),官能团羟基和氨基发挥了很大的作用.     

不溶性腐殖酸吸附Cr(Ⅵ)的研究

研究了不溶性腐殖酸对六价铬的吸附作用。进行了反应接触时间、pH值、IHA投加量、光照条件、温度等对反应的影响研究,确定了最佳反应条件,同时应用未处理的腐殖酸进行对比研究,说明不溶性腐殖酸的作用效果。试验表明在反应接触时间60 min、pH值为7左右、不溶性腐殖酸投加量为5 g/L和Cr(Ⅵ)的质量浓度为5.36 mg/L的条件下,不溶性腐殖酸对铬离子去除可达95%,比未处理的腐殖酸对铬离子去除提高近1倍。并绘制了不溶性腐殖酸对铬离子的反应动力学曲线和吸附等温线。     

钛柱撑蒙脱石对镍离子和锰离子的吸附机理

以钠基蒙脱石(Na-MMT)、钛酸四丁酯作基质材料,通过溶胶-凝胶法制备了钛柱撑蒙脱石(Ti-MMT)。利用XRD、FTIR及SEM对Ti-MMT进行了结构表征,考察了不同吸附条件对Ti-MMT吸附Ni~(2+)和Mn~(2+)的影响,并重点分析水溶液pH对Ti-MMT Zeta电位及吸附的影响,探究了Ti-MMT吸附Ni~(2+)和Mn~(2+)的机理。结果表明:Ti-MMT具有较大的晶面间距(d001=2.94 nm);pH对吸附Ni~(2+)与Mn~(2+)有较大影响,去除率随初始水溶液pH增加而提高。在pH=7,Ni~(2+)和Mn~(2+)初始质量浓度为50 mg/L,Ti-MMT投加量分别为5和9 g/L时,Ni~(2+)在318 K下吸附120 min,吸附量可达9.46 mg/g,去除率可达94.59%,Mn~(2+)在328 K下吸附180 min,吸附量可达4.82mg/g,去除率可达86.73%。此外,Ti-MMT对两种离子的吸附都更符合Temkin等温吸附模型及拟二级动力学模型,吸附过程受液膜扩散、颗粒内扩散等环节控制,且以离子交换的化学吸附为主。热力学分析表明,Ti-MMT对Ni~(2+)的吸附属于自发吸热熵增过程,而Mn~(2+)属于吸热熵增的非自发过程。     

荔枝皮吸附水中孔雀绿的响应曲面法研究

采用Box-Behnken响应曲面优化设计对荔枝皮吸附去除水中染料孔雀绿（MG）的影响因素（如吸附时间、吸附剂用量、pH值）进行研究,建立了去除率和上述因素之间的二次多项式模型,得到荔枝皮吸附孔雀绿的最佳吸附条件为：温度25℃、吸附时间122.31min、吸附剂用量2.81g/L、pH=6.75、MG浓度为100mg/L,最优条件下荔枝皮对孔雀绿的吸附去除率可以达99.75%。用Langmuir和Freundlich方程对吸附等温线进行拟合,其中Langmuir方程拟合效果最好,其最大吸附量为142.86mg/g,且吸附过程符合假二次动力学模型。此外,热力学结果表明,荔枝皮对孔雀绿的吸附属于自发的吸热过程。结合吸附-解吸循环实验和对吸附的FT-IR表征,表明荔枝皮是一种极具潜力的高效的吸附剂,能有效去除水中的孔雀绿离子。     

Magnetic nanocomposite of multi-walled carbon nanotube as effective adsorbent for methyl violet removal from aqueous solutions: Response surface modeling and kinetic study

Magnetic nanocomposite of multi-walled carbon nanotube (m-MWCNT) was synthesized for adsorptive removal of methyl violet (MV) from aqueous solutions. The experiments were conducted using a central composite design (CCD) with the variables of adsorbent dosage (0.4-1.2 g/L), solution pH (3-9), contact time (10-42 min) and ionic strength (0.02-0.1mol L^?1). Regression analysis showed good fit of the experimental data to a quadratic response surface model whose statistical significance was verified by analysis of variance. By applying the desirability functions, optimum conditions of the process were predicted as adsorbent dosage of 0.99g/L, pH=4.92, contact time of 40.98 minutes and ionic strength of 0.04 mol L^?1 to achieve MV removal percentage of 101.19. Experimental removal efficiency of 99.51% indicated that CCD along with the desirability functions can be effectively applied for optimizing MV removal by m-MWCNT. Based on the study, the adsorption process followed Langmuir isotherm model and pseudo-second-order kinetic model could realistically describe the dye adsorption onto m-MWCNT.     

核桃壳水热炭对六价铬的吸附特性

以核桃壳为前体采用水热炭化法制备水热炭,利用低温液氮物理吸附仪和傅里叶变换红外光谱仪测定水热炭的孔结构和表面官能团;实验研究其对液相中Cr(Ⅵ)的吸附特性,考察吸附剂加入量、Cr(Ⅵ)初始浓度、pH值、吸附时间等因素对吸附效果的影响。结果表明,水热炭的孔径分布范围较宽,表面含氧官能团丰富,能够很好地吸附溶液中的六价铬;溶液pH值对Cr(Ⅵ)的脱除影响很大,pH值呈酸性时吸附效果较好,pH值为2时脱除率达98.85%.当反应温度35℃、Cr(Ⅵ)初始浓度50mg/L、水热炭投加量为16g/L、pH值为6、吸附时间为100min时,Cr(Ⅵ)离子的去除率可达98%以上。核桃壳水热炭对Cr(Ⅵ)具有良好的吸附能力,吸附过程符合准二级吸附动力学模型,可用Freundlich吸附等温模型来描述,吸附等温线的线性相关性显著。     

碱性钙基膨润土对亚甲基蓝和刚果红的吸附去除

该文研究了碱性钙基膨润土(ACB)对水体中的亚甲基蓝(MB)和刚果红(CR)染料的吸附性能,考察了吸附剂用量、吸附时间及温度、pH及盐等因素对吸附效果的影响,同时进行了两种染料在碱性钙基膨润土上的吸附等温模型、吸附动力学模型研究。结果表明,ACB对MB、CR的脱色率随着吸附剂用量的增加而增加,在实验条件下,50 mg/L MB和100 mg/L CR的最佳吸附剂质量浓度分别为1.0 g/L和2.0 g/L;升高温度可以加快吸附速率,但对最终的脱色率影响很小;50 mg/L MB的吸附平衡时间在60 min左右,100 mg/L CR的吸附平衡时间在120 min左右;在pH=3～12时,ACB对MB的脱色率都稳定在99%左右,而适宜ACB吸附CR的pH=3～7,对CR的脱色率保持在90%左右;NaCl的加入对MB的吸附效果影响很小,对CR的吸附则有很强的抑制作用;ACB对MB的吸附同时符合Langmuir和Freundlich模型,而ACB对CR的吸附则更符合Langmuir模型;ACB对两种染料的吸附过程均符合准二级动力学模型,颗粒内扩散模型的拟合结果说明吸附过程存在颗粒内扩散作用。     

Monodisperse‐porous N‐methyl‐D‐glucamine functionalized poly(vinylbenzyl chloride‐co‐divinylbenzene) beads as boron selective sorbent

To generate a new sorbent with high boron adsorption capacity, we synthesized monodisperse‐porous poly(vinylbenzyl chloride‐co‐divinylbenzene), poly(VBC‐co‐DVB), beads 8.5 μm in size by a new “modified seeded polymerization” technique. By using their chloromethyl functionality, the beads were derivatized by a simple, direct reaction with a boron‐selective ligand, N‐methyl‐D ‐glucamine (NMDG). The selection of poly(VBC‐co‐DVB) beads as a starting material allowed to obtain high boron sensitive‐ligand density on the beads depending on their high chloromethyl content. In the batch adsorption runs performed using NMDG‐attached poly(VBC‐co‐DVB) beads as sorbent, boron removal was efficiently performed in a wide pH range between 4 and 11. Quantitative boron removal was observed with the sorbent concentration of 4 g/L. In the same runs, plateau value of equilibrium adsorption isotherm was obtained as 14 mg boron/g beads. Relatively higher boron adsorption was explained by high ligand density and high specific surface area of the sorbent. Boron adsorption isotherms were analyzed using Langmuir and Freundlich models. In the kinetic runs performed for boron removal, the equilibrium was attained within 10 min at a value of 98%. The fast kinetic behavior was explained by the smaller particle size and enhanced porosity of the new sorbent. Infinite solution volume model and unreacted core model were used to evaluate boron adsorption onto the NMDG‐attached poly(VBC‐co‐DVB) beads. The results indicated that the adsorption process is controlled by the particle‐diffusion step. © 2012 Wiley Periodicals, Inc. J Appl Polym Sci, 2012     

Removal of arsenic(III) from aqueous solution by concrete-based adsorbents

The present paper investigates the adsorption of arsenic(III) (As(III)) onto 2 concrete-based low-cost materials, i.e., Aerocrete and Vermiculite impregnated by ferric oxyhydroxide. Adsorption experiments were performed to study the effect of initial pH, initial concentration of As(III), contact time, and ions usually present in water. No significant effect of the initial pH on the adsorption of As(III) by Aerocrete and Vermiculite was observed at the pH range of 4–8. The As(III) removal efficiency decreased at a high initial pH (i.e., 10). The Langmuir isotherm showed that the maximum As(III) adsorption capacity of Aerocrete and Vermiculite is 15.15 and 13.51 mg/g, respectively, which is higher than that observed using titanium dioxide (i.e., 3.52 mg/g), at pH 7 and 24 ±1 °C. A pseudo-second order kinetic model fitted well the experimentally obtained kinetic data. This suggests that chemisorption most probably controls the adsorption of As(III) on Aeroctere and Vermiculite. Significantly, As(III) (1 mg/L) could be removed almost completely by both Aeroctere and Vermiculite (1 g/L) in 30 and 60 min, respectively at pH 7 and 24 ±1 °C. Importantly, Ca²⁺, Mg²⁺, Na⁺, HCO₃⁻, SO₄²⁻, and Cl⁻ ions had no significant effect on the adsorption of As(III) on Aeroctere and Vermiculite. The results showed that the proposed concrete-based adsorbents have the potential to remove As(III) from water.     

Effective Removal of Arsenic with Lanthanum(III)- and Cerium(III)-loaded Orange Waste Gels

Abstract

Orange waste has been chemically modified and loaded with lanthanum(III) and/or cerium(III) to examine its adsorption behavior to both As(V) and As(III). Arsenate removal was found to be favored over a pH range of 6 ～ 9.5 while arsenite removal took place at pH values ranging from 9 to 11. The maximum sorption capacity of the gel for As(III) removal was evaluated as 43 mg/g, while that for As(V) was 42 mg/g. Column-mode tests using the La(III)-loaded gel confirmed a complete removal of As(V). A reasonably high adsorption potential within the design criteria makes the present gel an alternative choice for arsenic removal.     

Optimizing adsorption of arsenic(III) by NH2-MCM-41 using response surface methodology

Response surface methodology (RSM) was used to optimize process parameters for arsenic (As(III)) removal from aqueous solution using amine-functionalized MCM-41 (NH₂-MCM-41). Four independent variables such as pH, initial metal concentration, temperature and adsorbent dosage were investigated. The optimal conditions to remove As(III) by NH₂-MCM-41 was found to be pH 5.62, initial As(III) concentration 5.00 mg/L, temperature 20 °C and NH₂-MCM-41 dosage 5.00 g/L. XRD, FTIR and SEM analyses testified to the obvious change of the surface morphology and the presence of metal on the sorbent after adsorption.     

Biosorption of hexavalent chromium from aqueous solutions using raw coconut fiber as a natural adsorbent

Abstract

This work aims to evaluate the Cr(VI) removal efficiency and adsorption capacity of the raw coconut fiber from synthetic aqueous solutions through the operational parameters as well as to represent the mechanisms of removal by kinetic and isotherm models. The experimental study was conducted in batch system and the optimum conditions for the adsorption of this metal by the biomass were according to: pH 2, contact time of 270?min, and 10?g/L of adsorbent dosage concentration. The removal efficiency obtained for Cr(VI) solutions was 99.2% at concentrations of 25–50?mg/L. For the highest concentrations, the removal decreased from 96.3% to 74.4%, when Cr(VI) solutions ranged from 100?mg/L to 250?mg/L, respectively. The adsorption kinetics was applied and showed a good agreement for pseudo-second-order and Elovich models, which point out a chemisorption. For the adsorption capacity at equilibrium conditions, the best fit was for the Redlich–Peterson isotherm indicating favorable adsorption and monolayer coverage.     

Adsorption of Cu(II) ions from aqueous solutions using ion exchange resins with different functional groups

The extraction of heavy metals from industrial effluents using efficient adsorbents is crucial for wastewater treatment and beneficial for metal recycling. In this study, the removal of Cu(II) from an acidic solution by commercial resins Dowex G-26 and Puromet™ MTS9570 was investigated. The influences of contact time, solution concentration, pH, temperature, and a resin dosage on the adsorption process were studied with batch technique. The optimum adsorption conditions were obtained at a concentration of 1100 mg/L Cu, contact time of 30 min, pH 3.5, and resin dosage of 0.025 g/ml for the removal of 99.9% and 90% of copper ions by G-26 and MTS9570, respectively. The experimental data of copper adsorption were analyzed using the Langmuir, Freundlich, and Temkin isotherm models. The highest metal uptakes of 41.67 and 37.70 mg/g were observed for Dowex G-26 and MTS9570, respectively. It was found that both resins had higher adsorption capacities than the substances reported in the literature. The adsorption kinetic studies showed that the copper adsorption process could be better described by the pseudo-second order model. Adsorption occurs spontaneously under endothermic conditions, which indicates the endothermic nature of the process.     

NiCoFe三元金属基LDHs对水中三价砷的吸附性能研究

采用共沉淀法制备了硝酸根型层状复合金属氢氧化物NiCoFe-LDHs,研究其对水中的三价砷的吸附性能,系统研究溶液初始浓度、吸附时间以及溶液pH值等因素对吸附性能的影响。结果表明,当As(Ⅲ)溶液浓度为2 mg/L时,吸附率达到了81.1%,吸附量在As(Ⅲ)溶液浓度为4 mg/L时,达到了15.72 mg/g,而溶液pH值为8时,吸附性能最好,且吸附过程在30 min内可以达到平衡。热力学和等温吸附式的研究表明NiCoFe-LDHs对As(Ⅲ)的吸附过程,符合Langmuir模型和伪二级动力学模型,因此吸附过程发生在吸附剂表面,且吸附过程为化学吸附。