花生壳粉作为生物吸附剂去除水溶液中偶氮染料的研究

用低值的花生壳粉作为生物吸附剂对苋菜红、日落黄两种偶氮染料进行了吸附研究,目的是寻求经济的染料废水处理方法。考察了PH、染料浓度、吸附剂量、吸附剂粒径、离子强度和吸附时间等因素对染料吸附的影响,确定了最佳吸附条件。结果显示,初始pH2,两种偶氮染料的去除率较高。吸附等温线符合Langmuir和Freondlich模式,吸附过程符合准一级反应动力学方程。研究结果表明,花生壳是一种很有前途的偶氮染料废水处理生物材料。     

铜离子和亚甲蓝在柠檬酸酯化麦草上的吸附行为

以固相酯化法制备一种具有羧基的柠檬酸改性麦草阳离子吸附剂.用批次实验法研究了不同实验条件下(pH值、吸附剂量、吸附质浓度和吸附时间)水溶液中铜离子和亚甲蓝在酯化麦草上的吸附行为.结果表明：溶液初始pH≥40时,铜离子和亚甲蓝达到最大吸附值.≥2.0 g·L^-1的酯化麦草能去除铜浓度为100 mg·L^-1溶液中96%的铜及亚甲蓝浓度为250 mg·L^-1溶液中99%的亚甲蓝.酯化麦草对铜离子和亚甲蓝的吸附符合Langmuir等温模型,其最大吸附能力分别为79.37 mg·g^-1和312.50 mg·g^-1.铜离子和亚甲蓝达到吸附平衡的时间分别为75 min和5 h,准一级和准二级反应动力学方程可分别描述酯化麦草对铜离子和亚甲蓝的吸附过程.     

球衣菌对工业废水中Cu2+吸附条件的研究

利用球衣菌FQ32制备生物吸附剂,研究其对Cu^2＋的耐受能力,并以连江某工厂含Cu^2＋废水为样液,对其进行吸附条件试验,分析了影响吸附率和吸附量的因素,结果表明,球衣菌FQ32对Cu^2＋的耐受能力大于150mg／L。在工业废水中Cu^2＋的浓度为23．1mg／L,吸附剂用量为0．2g／L,30℃,pH值6．0,吸附时间10min的条件下,该吸附剂对Cu^2＋的吸附率达到85．2％,吸附量达91．21mg／g。     

皂化麦麸对锌的吸附性能

以麦麸制备生物吸附剂研究其对重金属Zn~(2+)的吸附作用。利用DPS软件进行回归正交试验,分析pH、麦麸生物吸附剂加入量、温度、初始Zn~(2+)浓度和吸附时间对吸附率影响,得出最佳吸附条件,与活性炭、麦麸纤维吸附效果作比较,对皂化麦麸进行解吸;同时研究等温吸附和吸附动力学,电镜和傅立叶红外光谱图研究吸附机理。吸附时间3 h、加入量0.2 g、pH值9、70℃、Zn~(2+)溶液浓度为80 mg/L时,吸附率达最大值,且低浓度时,麦麸生物吸附剂吸附效果优于活性炭与麦麸纤维,至少可以进行四次重复利用。麦麸生物吸附剂对Zn~(2+)吸附符合Freundich等温式,更适合拟二级动力学模型,即符合多分子层多位点物理化学混合吸附。SEM知皂化麦麸有明显褶皱,疏松多孔,表面积增大;FTIR分析出,麦麸生物吸附剂含-OH、-NH-、-C≡C-、-C≡N等多个官能团,对吸附过程起到很大的作用。     

啤酒废酵母对镉离子的吸附研究

以啤酒酿造厂的啤酒废酵母为生物吸附剂,研究啤酒废酵母对Cd2 的生物吸附行为。利用原子吸收光谱法测定Cd2 含量。结果表明,啤酒废酵母吸附Cd2 受吸附时间、吸附温度、溶液pH值、酵母添加量和Cd2 起始浓度等因素的影响。实验确定了啤酒废酵母对Cd2 的最佳吸附条件。即:pH值6,Cd2 浓度为50mg/L,酵母添加量为1.0g/L,吸附温度25℃,吸附时间30min,此时啤酒废酵母对Cd2 的吸附量可达42.92mg/g干酵母。吸附Cd2 的啤酒废酵母用1.0mol/L的HCl解吸,解吸率达75.46%。对未吸附Cd2 的空白酵母和吸附Cd2 的酵母进行红外光谱分析,结果显示啤酒废酵母吸附Cd2 后羟基和羧基吸收峰发生明显变化,因此认为羟基和羧基在生物吸附中起着重要作用。     

壳聚糖改性竹炭对铜吸附性能研究

为了提高竹炭去除废水中重金属离子能力,采用交联法设计合成新型的磁性壳聚糖改性竹炭复合吸附剂,并采用傅里叶红外光谱对改性竹炭复合吸附剂进行表征,同时开展不同Cu2+初始浓度、吸附剂投加量、吸附时间、pH和温度等因素对Cu2+吸附去除率的影响。结果表明,吸附效率与Cu2+初始浓度和吸附剂投加量成正效应;吸附平衡时间约8 h;在作用温度范围内,吸附效率随温度升高而上升;pH为7时吸附效果最好。振荡条件吸附效果优于静置处理。该结果为废水重金属深度处理及水环境保护提供依据。     

废啤酒酵母吸附水溶液中Cu2+的性能及机理研究

用废啤酒酵母吸附水溶液中Cu2+,考察了溶液pH值、Cu2+浓度和吸附时间对Cu2+吸附的影响。结果表明：废啤酒酵母吸附Cu2+在4-6个小时内达到吸附平衡,酸性条件利于吸附,以pH为5时最佳,吸附等温曲线符合Langmuir模式。用电位滴定及FTIR分析的方法确定生物吸附剂主要含有磺酸基、羧基及氨基等功能团。生物吸附剂对Cu2+的吸附以单分子层的化学吸附为主,功能团在不同的pH条件下呈现不同的电离性能,在吸附过程中发挥重要作用。     

东方栓孔菌菌丝体生物吸附剂对染料的脱色作用及其吸附机制研究

利用东方栓孔菌Trametes orientalis菌丝体制得的生物吸附剂,对刚果红、结晶紫、铬天青、亚甲基蓝和中性红5种染料进行了脱色试验,对脱色效果较好的染料进行了影响因子优化,并通过红外光谱分析、化学修饰等方法研究其吸附作用的机制。结果显示：东方栓孔菌菌丝体生物吸附剂对结晶紫有相对较好的脱色效果;在优化的影响因子中,0%–3.0%（m/v）浓度范围内,盐度对染料脱色有促进作用;表面活性剂促使脱色率增加,吐温60浓度为1.5%（v/v）时脱色率可达83.84%;温度为43℃、初始pH为3.0、振荡培养10d后吸附率最高达91.54%。红外光谱分析及化学修饰结果表明菌丝体对染料的吸附作用主要是由它们之间的静电作用力所致。     

青霉吸附水体重金属铬条件与特性研究

目的:研究青霉(Penicillium lh-1)作为吸附剂去除水体中六价铬的吸附条件与吸附特性.方法:菌种摇瓶培养收获茵体,干燥粉碎分选,添加吸附剂到体积100ml浓度50mg/L六价铬溶液中,对最优吸附温度、pH、共存离子以及铬被吸附形式进行研究.结果:①温度28℃以及酸性环境(pH 3)为最优吸附条件,10 h内,Cr(Ⅵ)的生物吸附去除效率达99%.②铬的生物吸附主要以六价形式,约占80%,部分Cr(Ⅵ)被还原成Cr(Ⅲ),约占20%.③溶液中共存离子对六价铬吸附的影响不同,一价阴离子与Cu2+对Cr(Ⅵ)的吸附几乎没有影响,二价阴离子和Ni2+的存在却明显地影响了生物吸附剂对Cr(Ⅵ)的吸附.结论环境温度、溶液pH以及溶液中共存离子对铬的生物吸附有显著的影响.     

根霉吸附水体中重金属铬与吸附机理的研究

以根霉RhizopusLH2死菌体为吸附剂进行水体中六价铬的吸附研究.结果表明,Cr(VI)的生物吸附最优条件为:温度28℃,pH为2;线性回归相关系数为0.98,符合Langmuir吸附等温线模型;傅立叶红外变换光谱分析推断吸附机理为质子化氨基在Cr(VI)的生物吸附中起主要作用.     

Adsorption of metal complex dyes from aqueous solutions by pine sawdust

An attempt to alleviate the problem caused by the presence of metal complex dyes, mostly used in textile industries, in the textile effluents was undertaken. The effects of adsorbent particle size, pH, adsorbent dose, contact time and initial dye concentrations on the adsorption of metal complex dyes by pine sawdust was investigated. Acidic pH was favorable for the adsorption of metal complex dyes. A contact time of 120 min was required to reach the equilibrium. The experimental isotherm data were analyzed using the Langmuir, Freundlich and Temkin equations. The equilibrium data fit well the Langmuir isotherm. The monolayer adsorption capacities are 280.3 and 398.8 mg dye per g of pine sawdust for Metal Complex Blue and Metal Complex Yellow, respectively. The results indicate that pine sawdust could be employed as low-cost alternative to commercial activated carbon in aqueous solution for the removal of metal complex dyes.     

Removal of methylene blue dye from aqueous solutions by adsorption using yellow passion fruit peel as adsorbent

The removal of color from aquatic systems caused by presence of synthetic dyes is extremely important from the environmental viewpoint because most of these dyes are toxic, mutagenic and carcinogenic. In this present study, the yellow passion fruit (Passiflora edulis Sims. f. flavicarpa Degener) peel a powdered solid waste, was tested as an alternative low-cost adsorbent for the removal of a basic dye, methylene blue (MB), from aqueous solutions. Adsorption of MB onto this natural adsorbent was studied by batch adsorption isotherms at room temperature. The effects of shaking time and pH on adsorption capacity were studied. An alkaline pH was favorable for the adsorption of MB. The contact time required to obtain the maximum adsorption was 56 h at 25 degrees C. Yellow passion fruit peel may be used as an alternative adsorbent to remove MB from aqueous solutions.     

Cationized starch-based material as a new ion-exchanger adsorbent for the removal of C.I. Acid Blue 25 from aqueous solutions

This article describes the use of a cationized starch-based material as new ion-exchanger adsorbent for the removal of C.I. Acid Blue 25 (AB 25) from aqueous solutions. Batch adsorption studies concerning the effects of contact time, pH and temperature are presented and discussed. Adsorption experimental data showed that: (i) the process was uniform and rapid: adsorption of dye reached equilibrium in 50 min in the wide pH range of dye solutions; (ii) adsorption kinetics followed the pseudo-second order model; (iii) the Langmuir model yielded a much better fit than the Freundlich model for the dye concentration range under study; (iv) this adsorbent exhibited interesting adsorption capacities: on the basis of the Langmuir analysis, the maximum adsorption capacity was determined to be 322 mg of dye per gram of material at 25 degrees C; (v) the adsorption capacity decreased with increasing temperature; and (vi) the negative value of free energy change indicated the spontaneous nature of adsorption.     

Uptake of cationic dyes from aqueous solution by biosorption onto granular kohlrabi peel

A new, low cost, locally available biomaterial was tested for its ability to remove cationic dyes from aqueous solution. Granules prepared from kohlrabi peel had been utilized as a sorbent for uptake of three cationic dyes, methylene blue (MB), neutral red (NR) and acridine orange (AO). The effects of various experimental parameters (e.g., dye concentration, particle size, initial pH, contact time and other factors) were investigated and optimal experimental conditions were ascertained. Above the value of initial pH 4, three dyes studied could be removed effectively. The isothermal data fitted the Langmuir model in the case of NR sorption and the Freundlich model for all three dyes sorption. The biosorption processes followed the pseudo-first-order rate kinetics. The results in this study indicated that kohlrabi peel was an attractive candidate for removing cationic dyes from the dye wastewater.     

Equilibrium and kinetic analysis of methyl orange sorption on chitosan spheres

Chitosan can be used as adsorbent in the treatment of effluents from the textile industry, especially for negatively charged dyes, due to its cationic polyelectrolyte nature. In this work, the sorption of a model dye, methyl orange, on chitosan hydrobeads is analyzed in terms of equilibrium and kinetic approaches. Equilibrium studies showed that dye adsorption had a mixed Freundlich-Langmuir behavior that had its Langmuir character increased as the pH was increased. In terms of adsorption kinetics, it was found to be of nth-pseudo-order, with fractional n increasing from approximately 2 to approximately 2.5 as pH and initial dye concentration in the continuous phase were increased. The increase in the apparent pseudo-order was related to changes in mathematical approximation for the solution of the sorption rate equation, which were the result of the decrease in the ratio (number of active sites for adsorption)/(number of adsorbate molecules).     

Utilization of unconventional lignocellulosic waste biomass for the biosorption of toxic triphenylmethane dye malachite green from aqueous solution

Biosorption potential of novel lignocellulosic biosorbents Musa sp. peel (MSP) and Aegle marmelos shell (AMS) was investigated for the removal of toxic triphenylmethane dye malachite green (MG), from aqueous solution. Batch experiments were performed to study the biosorption characteristics of malachite green onto lignocellulosic biosorbents as a function of initial solution pH, initial malachite green concentration, biosorbents dosage, and temperature. Biosorption equilibrium data were fitted to two and three parameters isotherm models. Three-parameter isotherm models better described the equilibrium data. The maximum monolayer biosorption capacities obtained using the Langmuir model for MG removal using MSP and AMS was 47.61 and 18.86 mg/g, respectively. The biosorption kinetic data were analyzed using pseudo-first-order, pseudo-second-order, Elovich and intraparticle diffusion models. The pseudo-second-order kinetic model best fitted the experimental data, indicated the MG biosorption using MSP and AMS as chemisorption process. The removal of MG using AMS was found as highly dependent on the process temperature. The removal efficiency of MG showed declined effect at the higher concentrations of NaCl and CaCl₂. The regeneration test of the biosorbents toward MG removal was successful up to three cycles.     

Equilibrium study of dried orange peel for its efficiency in removal of cupric ions from water

Excess of copper ion (>2 mg/L) in water is toxic to human beings and the ecosystem. Various water treatment technologies for copper remediation have been investigated in the past. Along with industrial effluents, Bordeaux mixture is also a noteworthy copper contamination source in the agricultural ecosystem. In our study, the biosorbent efficiency of dried orange peel was investigated through an environment-friendly process for the removal of cupric ions. Effects of pH, adsorbate concentration, adsorbent dosage, and temperature for the removal of Cu (II) were studied. Slightly acidic environment (pH = 6) was found to be optimum for removal of copper. The equilibrium data were well fitted with the Langmuir and Freundlich isotherms. The surface morphology of the adsorbent was studied using scanning electron microscope. Crystalline nonhomogenous surface was observed after copper adsorption. Desorption study indicated that 0.1N H₂SO₄ is the best eluent for the removal of adsorbed copper from the powdered dried orange peel.