Acid Blue 25 adsorption on base treated Shorea dasyphylla sawdust: Kinetic, isotherm, thermodynamic and spectroscopic analysis

The potential of base treated Shorea dasyphylla (BTSD) sawdust for Acid Blue 25 (AB 25) adsorption was investigated in a batch adsorption process. Various physiochemical parameters such as pH, stirring rate, dosage, concentration, contact time and temperature were studied. The adsorbent was characterized with Fourier transform infrared spectrophotometer, scanning electron microscope and Brunauer, Emmett and Teller analysis. The optimum conditions for AB 25 adsorption were pH 2, stirring rate 500 r/min, adsorbent dosage 0.10 g and contact time 60 min. The pseudo second-order model showed the best conformity to the kinetic data. The equilibrium adsorption of AB 25 was described by Freundlich and Langmuir, with the latter found to agree well with the isotherm model. The maximum monolayer adsorption capacity of BTSD was 24.39 mg/g at 300 K, estimated from the Langmuir model. Thermodynamic parameters such as Gibbs free energy, enthalpy and entropy were determined. It was found that AB 25 adsorption was spontaneous and exothermic.     

干活性污泥吸附水中染料的试验研究

以城市污水处理厂干活性污泥为吸附剂对染料直接深棕M、酸性媒介棕RH进行了吸附研究,结果表明,吸附过程能很好地用二级速率表达式表示,同时也可用Lagergren一级速率方程描述。其一级吸附速率常数k1分别为0.0204min-1和0.0068min-1,二级吸附速率常数k2分别为0.00592和0.00589gmg-1min-1。两者的吸附特性不同,其吸附等温线前者符合Freundlich方程,后者既符合Freundlich方程也符合Langmuir方程。吸附平衡时间、去除率亦不同,前者明显大于后者,达到吸附平衡的时间分别为120min和240min。两种染料的正辛醇/水分配系数logP计算数值分别为4.65和-0.22,这一顺序与两种染料在干污泥上的吸附行为相符。     

Influence of particle size and salinity on adsorption of basic dyes by agricultural waste： dried Seagrape （Caulerpa lentiUifera）

Green macroalga Caulerpa lentillifera was found to have reasonable adsorption capacity for basic dyes, Astrazon Blue FGRL （AB）, Astrazon Red GTLN （AR）, and Astrazon Golden Yellow GL-E （AY）. The initial dye concentration was in the range of 100-1,800 mg/L. The dried algal sorbent was ground and sieved into 3 sizes： S （0.1-0.84 mm）, M （0.84-2.0 mm）, and L sizes （larger than 2.0 mm）. For all conditions examined in this work （at 25℃ in batch systems）, the adsorption reached equilibrium within the first hour. The kinetic data corresponded well with the pseudo second order kinetic model where the rate constant, k2, decreased as the sorbent size increased for all dyes. The adsorption isotherms followed both Langmuir and Freundlich models. Among three sorbent sizes, S size gave the highest adsorption capacity followed by M and L sizes. A reduction of sorbent size increased the specific surface area for mass transfer, and also increased the total pore volume, thus providing more active sites for adsorption. The adsorption of AB was adversely influenced by the protonation of algal surface at low pH. On the other hand, the adsorption of AR and AY could be due to weak electrostatic interaction, which was not significantly affected by pH. Increasing salinity of the system caused a decrease in adsorption capacity possibly due to the competition between Na^＋ and the dye cations for the binding sites on algal surface. Moreover, an increase in salinity generated a compressed electrical double layer on the algal surface which exerted repulsive force, retarding the adsorption of positive charged molecules such as the basic dyes.     

Adsorption behavior of Azo Dye C. I. Acid Red 14 in aqueous solution on surface soils

Azo dyes have received considerable attention because of their association with various human health problems. The aim of the investigation is to determine the adsorption behavior ofazo dyes in aqueous solution on DG06, GSE17200, and GSE17201 soils using C. I. Acid Red 14 （AR14） as example. The experimental results indicate that the Freundlich model expresses the adsorption isotherm better than the Langmuir model and the pseudo-second-order model achieves adsorption of AR14 on the three soils well. Based on the pseudo-second-order model, the adsorption thermodynamic of AR14 on DG06 soil have been studied and the thermodynamics parameter of AGO is determined and AGO value shows the adsorption process of AR14 on DG06 is mainly physical in nature. Furthermore, the effects of temperature, pH and salinity （NaC1） on adsorption have been investigated. The decrease in pH or the increase in salinity enhances the adsorption of AR14 by DG06, GSE17200, and GSE17201.     

改性壳聚糖的制备及其对水中酞酸酯的吸附

以柠檬醛化学改性壳聚糖,制备柠檬醛交联壳聚糖树脂。采用红外光谱(IR)、X射线衍射(XRD)、扫描电镜(SEM)、比表面测定及孔径分析方法表征柠檬醛交联壳聚糖树脂的结构。在25℃,pH为7条件下,考察柠檬醛交联壳聚糖树脂对3种酞酸酯(PAEs)邻苯二甲酸二甲酯(DMP)、邻苯二甲酸二丁酯(DBP)和邻苯二甲酸2-乙基己酯(DEHP)的吸附性能,剖析吸附机理。研究结果表明,壳聚糖对DMP、DEHP和DBP的吸附容量分别为92、113和87 mg/g,而柠檬醛交联壳聚糖树脂对DMP、DEHP和DBP的吸附容量分别为147、166和190 mg/g,柠檬醛交联壳聚糖树脂对3种PAEs的吸附效果明显提高,吸附动力学均满足一级动力学方程。经吸附剂再生实验,柠檬醛交联壳聚糖树脂对PAEs的脱附率达到96.5%~97.1%,可重复使用。     

污泥活性炭对染料的吸附动力学研究

以城市污水处理厂脱水污泥作为原料,采用化学活化法(ZnCl2作为活化剂)制得污泥活性炭,全面研究了污泥活性炭对活性艳红K-2BP、酸性大红GR和直接紫N这3种染料的吸附动力学行为.结果表明,污泥活性炭可以有效地吸附染料,实现污泥的资源化;3种染料的平衡吸附量qe均随着染料初始浓度和温度的增大而增大,相同条件下平衡吸附量qe的大小顺序为:酸性大红GR＞活性艳红K-2BP＞直接紫N;伪二级动力学模型能够很好地描述3种染料在污泥活性炭上的吸附动力学行为;对于活性艳红K-2BP和直接紫N,颗粒内扩散过程是该吸附速率的控制步骤,但不是唯一的速率控制步骤,吸附速率同时还受颗粒外扩散过程的控制,而对于酸性大红GR,颗粒内扩散过程不是吸附速率的控制步骤;污泥活性炭对3种染料的吸附是一个吸热过程,吸附活化能较小,主要为物理吸附过程.     

掺杂聚乙烯醇的壳聚糖小球对铜离子-腐殖酸的单一和连续吸附行为

以三聚磷酸钠作为离子交联剂,合成了一种掺杂聚乙烯醇的壳聚糖小球,采用SEM和FTIR表征了小球的表面性能及官能团分布情况,进一步研究了这种小球对腐殖酸和铜离子的单独吸附行为、连续吸附行为及两者共存状态下的吸附行为,并通过XPS能谱分析了吸附过程的机理.结果表明:在单独吸附过程中,壳聚糖小球与腐殖酸和铜的作用方式主要是通过静电引力和络合作用;在连续吸附过程中,先吸附了腐殖酸的小球,后续对铜离子的吸附效果变弱;而先吸附了铜离子的小球,后续对腐殖酸的吸附能力变强,说明这种小球在吸附过程中可以被连续使用.而在腐殖酸和铜离子共存的吸附实验中发现,壳聚糖小球除了会吸附溶液中的铜离子和腐殖酸外,还导致它们的聚集沉降.     

纳米磁性颗粒Fe3O4用于吸附水相中酸性红73及其机理研究

利用纳米磁性颗粒处理含酸性红73废水以利于进一步降低其色度.实验以酸洗废液制备的纳米磁粉Fe3O4作为吸附剂,并通过单因素实验和吸附动力学及热力学的分析探讨其对酸性红73的表面吸附的吸附机理.结果表明:纳米磁粉Fe3O4对酸性红73的表面吸附符合假二级动力学方程,其反应活化能为49.05 kJ·mol-1.磁粉对酸性红73的吸附是快速的表面物理吸附,其表面吸附行为符合Langmuir等温吸附式,是放热和熵减的自发过程.在温度T为303 K的条件下,20 min内的饱和吸附量能可达到40.1 mg·g-1.因此,用纳米磁粉Fe3O4吸附处理含偶氮染料废水,吸附平衡可在很短的时间内实现.     

β-环糊精接枝壳聚糖对酸性红R的吸附研究

为改善壳聚糖的吸附性能,用苯甲醛保护壳聚糖氨基,通过与环氧氯丙烷和β-环糊精的反应合成了新的吸附剂β-环糊精接枝壳聚糖,研究了其对偶氮染料酸性红R的吸附行为,考察了酸性红R的初始浓度、pH对吸附效果的影响。结果发现当酸性红R的浓度≤100mg/g时,合成物的吸附量随酸性红R浓度的增大而增加,当浓度进一步增大时,吸附量趋于平衡。合成物对酸性红R的吸附效果在pH为2～4之间最好。相比于Freundlich吸附等温式(R2=0.8476),β-环糊精接枝壳聚糖对酸性红R的吸附规律明显更符合Langmuir吸附等温式(R2=0.9977)。吸附动力学采用了准一级速率方程(R2=0.8609)和准二级速率方程来描述,结果表明吸附动力学符合准二级速率方程(R2=0.9945)。β-环糊精接枝后的壳聚糖对酸性红R的平衡吸附容量可以提高20.2mg/g。     

Comparison of four supports for adsorption of reactive dyes by immobilized Aspergillus fumigatus beads

Four materials, sodium carboxymethylcellulose (Na-CMC), sodium alginate (SA), polyvinyl alcohol (PVA), and chitosan (CTS), were prepared as supports for entrapping fungus Aspergillus fumigatus. The adsorption of synthetic dyes. Reactive Brilliant Blue KN-R, and Reactive Brilliant Red K-2BP, by these immobilized gel beads and plain gel beads was evaluated. The adsorption efficiencies of Reactive Brilliant Red K-2BP and Reactive Brilliant Blue KN-R by CTS immobilized beads were 89.1% and 93.5% in 12 h, respectively. The adsorption efficiency by Na-CMC immobilized beads was slightly lower than that of mycelial pellets. But the dye culture mediums were almost completely decolorized in 48 h using the above-mentioned two immobilized beads (exceeding 95%). The adsorption efficiency by SA immobilized beads exceeded 92% in 48 h. PVA-SA immobilized beads showed the lowest adsorption efficiency, which was 79.8% for Reactive Brilliant Red K-2BP and 92.5% for Reactive Brilliant Blue KN-R in 48 h. Comparing the adsorption efficiency by plain gel beads, Na-CMC plain gel beads ranked next to CTS ones. SA and PVA-SA plain gel beads hardly had the ability of adsorbing dyes. Subsequently, the growth of mycelia in Na-CMC and SA immobilized beads were evaluated. The biomass increased continuously in 72 h. The adsorption capacity of Reactive Brilliant Red K-2BP and Reactive Brilliant Blue KN-R by Na-CMC immobilized beads was 78.0 and 86.7 mg/g, respectively. The SEM micrographs show that the surface structure of Na-CMC immobilized bead is loose and finely porous, which facilitates diffusion of the dyes.     

磁性壳聚糖的制备及处理亚甲基蓝废水

以戊二醛为交联剂,Fe₃O₄为磁核制备磁性壳聚糖,探究了其去除废水中亚甲基蓝的性能,以及吸附动力学、吸附等温线、吸附热力学特征.结果表明,在磁性壳聚糖投加量为0.5g/L、pH=10、反应时间为60min的条件下,对亚甲基蓝的去除率和吸附容量分别达到97.6%和39.0mg/g,远高于天然壳聚糖的59.8%和23.9mg/g.磁性壳聚糖对亚甲基蓝的吸附过程符合准二级反应动力学方程（R²=0.99902）和Langmuir等温线方程（R²=0.99961）,吸附过程是热力学自发过程,吸附反应是放热反应.     

聚烯丙基磺酸钠接枝空心玻璃微珠的制备及其吸附性能研究

通过将烯丙基磺酸钠（SAS）和硅烷偶联剂接枝到空心玻璃微珠表面,制备出新型空心玻璃微珠基吸附剂（KNH-g-PSAS）并采用扫描电子显微镜,能量分散光谱,X射线光电子能谱,傅里叶变换红外光谱,热重分析和X射线衍射仪等对其进行了充分的表征,显示了SAS的成功接枝.此外,系统地研究了溶液的pH值,接触时间,初始浓度和温度对KNH-g-PSAS吸附阳离子染料的影响.准二级动力学模型和Langmuir等温线模型分别很好地描述了吸附动力学和吸附等温线,表明吸附是发生在吸附剂表面且均匀的单层吸附.吸附实验表明,在最佳条件下,KNH-g-PSAS对碱性品红、金胺O、结晶紫和孔雀石绿的吸附能力分别为2247.19mg/g,2317.46mg/g,2557.54mg/g,2808.98mg/g.KNH-g-PSAS具有出色的自上浮性能和回收表现.     

壳聚糖的改性及其去除废水中染料物质的性能研究

采用戊二醛交联FeCl_3制备改性壳聚糖吸附处理染料废水,以20 mg·L~(-1)的亚甲基蓝溶液作为处理对象,探究氯化铁改性壳聚糖(FeCl_3-CTS)投加量、废水p H值、反应时间对其处理亚甲基蓝废水性能的影响,并对吸附动力学、吸附等温线过程进行拟合.结果表明,FeCl_3-CTS对亚甲基蓝废水的处理效果远高于未改性壳聚糖(N-CTS),尤其是在投加量为0.1 g·L~(-1)、p H=6的条件下,经FeCl_3-CTS处理50 min后,亚甲基蓝废水的脱色率高达99.4%,FeCl_3-CTS对亚甲基蓝的吸附容量高达198.8 mg·g~(-1),与N-CTS的54.8%和109.6 mg·g~(-1)相比,均有显著的提高.吸附动力学、吸附等温线拟合结果显示,FeCl_3-CTS对亚甲基蓝废水的吸附过程符合准二级反应动力学方程(R2=0.9992)和Langmuir等温线方程(R~2=0.9995).     

壳聚糖/改性平菇复合吸附剂对Cr(VI)的吸附特性

以壳聚糖和经酒石酸改性的平菇粉末为材料,通过戊二醛进行交联反应,制得壳聚糖-改性平菇凝胶小球（CMPOD）复合生物吸附剂,用于水溶液中Cr（VI）的吸附去除.结果表明,在实验所测pH值（2~10）范围内,复合吸附剂对Cr（VI）的吸附量随着pH值上升而降低;随着Cr（VI）初始浓度或温度的提高,吸附剂对Cr（VI）的吸附量均相应增加,当Cr（VI）初始浓度为600mg/L,温度为50℃,Cr（VI）吸附量可达190mg/g以上;Cr（VI）的吸附符合准二级动力学方程及Freundlich等温吸附模型;热力学分析表明,吸附剂对Cr（VI）的吸附过程为自发的吸热反应.扫描电镜（SEM）分析显示,吸附剂具有发达的网状结构,吸附Cr（VI）后网状孔隙被填充,且能谱分析（EDS）出现明显的Cr（VI）吸收峰;傅立叶红外光谱分析（FTIR）表明,壳聚糖中的氨基成功引入复合吸附剂中,在Cr（VI）吸附中为主要作用官能团.     

改性硅藻土对三种有机染料的吸附作用研究

以天然硅藻土分别负载十六烷基三甲基溴化铵(CTMAB)、四甲基溴化铵(TMAB)和壳聚糖,制得一系列改性硅藻土,研究了改性硅藻土吸附水中的阴离子染料(活性红120)、阳离子染料(亚甲基蓝)、酸性染料(玫瑰红B)的适宜条件及吸附机理.结果表明,天然硅藻土对亚甲基蓝、四甲基溴化铵改性硅藻土对玫瑰红B和壳聚糖改性硅藻土对活性红120的饱和吸附量分别为51.15、49.56、56.64mg.L-1,效果良好,可被直接利用.延长吸附时间、增大吸附剂用量、控制溶液的pH值(<6)都能提高改性硅藻土吸附剂的吸附效果;3种染料在各自吸附剂上的平衡吸附量Qe与平衡浓度Ce之间的关系均符合Freundlich等温吸附方程,表明改性硅藻土吸附染料以分配作用、弱的溶质吸收为主.改性剂的引入可以改变硅藻土的表面电性,从而对不同类型染料的吸附能力产生不同影响.     

固定化铜绿假单胞菌吸附Cu~(2+)的特性

首次利用聚丙烯酰胺与壳聚糖形成的互融聚合物网络凝胶固定非活性的铜绿假单胞菌,并研究了这种新型的固定化微生物颗粒对Cu2+的吸附特性。该固定化微生物吸附剂表现出较好的吸附性能,对Cu2+的吸附很迅速,在40min内吸附基本达到平衡。对吸附动力学及平衡的研究表明,Cu2+在固定化微生物吸附剂上的吸附过程符合准二级动力学方程,吸附平衡符合Langmuir模型。     

Removal of phosphate from wastewater using alkaline residue

Alkaline residue(AR) was found to be an efficient adsorbent for phosphate removal from wastewater. The kinetic and equilibrium of phosphate removal were investigated to evaluate the performance of modified alkaline residue. After treatment by NaOH(AR-NaOH), removal performance was significantly improved, while removal performance was almost completely lost after treatment by HCl(AR-HCl). The kinetics of the removal process by all adsorbents was well characterized by the pseudo second-order model. The Langmuir model exhibited the best correlation for AR-HCl, while AR was effectively described by Freundlich model. Both models were well fitted to AR-NaOH. The maximum adsorption capacities calculated from Langmuir equation were in following manner: AR-NaOH AR AR-HCl. Phosphate removal by alkaline residue was pH dependent process. Mechanisms for phosphate removal mainly involved adsorption and precipitation, varied with equilibrium pH of solution. For AR-HCl, the acid equilibrium pH( 6.0) was unfavorable for the formation of Ca-P precipitate, with adsorption as the key mechanism for phosphate removal. In contrast, for AR and ARNaOH, precipitation was the dominant mechanism for phosphate removal, due to the incrase on pH( 8.0) after phosphate removal. The results of both XRD and SEM analysis confirmed CaHPO4·2H2O formation after phosphate removal by AR and AR-NaOH.     

Dyes adsorption using a synthetic carboxymethyl cellulose-acrylic acid adsorbent

Removal of noxious dyes is gaining public and technological attention. Herein grafting polymerization was employed to produce a novel adsorbent using acrylic acid and carboxymethyl cellulose for dye removal. Scanning electron microscopy and Fourier-transform infrared spectroscopy verified the adsorbent formed under optimized reaction conditions. The removal ratio of adsorbent to Methyl Orange, Disperse Blue 2BLN and malachite green chloride reached to 84.2%, 79.6% and 99.9%, respectively. The greater agreement between the calculated and experimental results suggested that pseudo second-order kinetic model better represents the kinetic adsorption data. Equilibrium adsorptions of dyes were better explained by the Temkin isotherm. The results implied that this new cellulose-based absorbent had the universaiity for removal of dyes through the chemical adsorption mechanism.     

聚天冬氨酸对土壤吸附、解吸汞的机制研究

为揭示土壤中添加聚天冬氨酸（PASP）后其对汞的吸附、解吸过程,探究了不同PASP用量对土壤吸附解吸汞的机制及有机质、pH、汞初始浓度等因素的影响。结果表明,PASP可显著抑制土壤对汞的吸附,促进土壤对汞的解吸,在PASP用量为300 mg时,其吸附量、解吸量分别是未添加PASP时的0.68、27倍;有机质与PASP之间在土壤吸附汞时表现为拮抗作用,在土壤解吸汞时表现为协同作用;在较宽pH范围（4.0～7.0）和不同汞浓度（5～200 mg/L）下,PASP均能抑制土壤对汞的吸附;PASP作用于整个吸附进程;土壤对汞的吸附特征符合Langmuir、Freundlich方程和准二级动力学方程,而PASP的存在均使其特征方程偏离;原土和去除有机质的土壤对汞的最大吸附量（q_m）分别为2.1和2.0 mg/g,比未添加PASP的处理分别下降了65.47%和12.94%。本研究为PASP应用于汞污染土壤的修复奠定了研究基础。     

壳聚糖对染料的吸附动力学研究

通过壳聚糖吸附酸性染料普拉蓝RAWL和阳离子蓝染料X-GRRL的试验，研究了壳聚糖对这两种水溶性染料吸附的动力学行为，包括吸附速率K和颗粒内有效扩散系数Di′，同时通过对吸附焓△H的试验计算，初步分析了它们的吸附机理。