黑曲霉吸附弱酸性艳蓝RAWL机理研究

考察了黑曲霉对染料吸附性能的pH响应模式,红外光谱表征了菌体表面的主要官能团组成,化学修饰定量研究了不同官能团的染料吸附贡献.结果显示,在低pH条件下,菌体表现出最优的染料吸附特性:随着pH值由2.0升至6.0,染料吸附量由39.6mg/g降至9.3mg/g.菌体表面含有氨基、羧基和磷酸根.高pH下,羧基和磷酸根电离导致菌体表面带负电并与染料发生静电斥力,使得染料吸附量下降;低pH下,氨基的质子化使得菌体带正电并通过静电吸引提高染料吸附.甲基化氨基在酸性条件下仍然可以质子化,故氨基甲基化修饰后染料吸附性能不变;乙酰化氨基在酸性体系中失去质子化能力,乙酰化修饰菌体染料吸附性能下降51.6%.氨基质子化引起的菌体正电性和染料负电性之间的静电引力是染料吸附的重要机制.图6参10     

汽车尾气净化非贵金属催化剂SO2中毒机理研究

用TPD,IR,XPS等方法研究了汽车尾气净化的复合氧化物催化剂SO_2中毒机理。结果表明,催化剂SO_2中毒失(?),首先是SO_2在催化剂活性中心上进行化学吸附,然后部分SO_2与活性组分生成相应的亚硫酸盐和硫盐酸,从而使催化剂失活。SO_2的化学吸附及部分生成相应的亚硫酸盐,与生成硫酸盐相比,对催化剂失活的影响,前者更为明显。     

青霉菌对活性艳蓝 KN-R的吸附作用

研究了青霉菌(Penicillium X5)对活性艳蓝KN—R的吸附作用．通过对培养液的波谱分析和宏观现象的观察，结果表明，在72h内，脱色是由吸附引起的．当染料的浓度为100mg/L时，活菌体对染料的吸附率可达88．66％．本实验还研究了对实际应用和吸附过程有影响的几个因素，包括葡萄糖、NaCl、温度和pH.结果表明：葡萄糖浓度在0-20g／L时，随着葡萄糖浓度的增加，菌体的干重相应增加，说明对活性艳蓝KN—R的吸附具有促进作用，但浓度在10-20g／L时，吸附作用不显著；而随着NaCl浓度(0-2％)的增加，吸附率却显著降低．最佳脱色温度为25℃，pH为4．0．活菌体与死菌体的生物吸附均符合Langmuir方程，活菌体比死菌体具有更好的吸附性能．吸附在菌丝体上的染料可以用甲酵进行洗脱，菌丝球在下次使用前用蒸馏水冲洗至pH中性，此菌丝球可重复使用3次．固8表2参11     

预处理青霉菌对中性红和孔雀绿的吸附

以青霉菌(Penicillium sp.)为吸附剂,对水溶液中染料中性红和孔雀绿进行了吸附研究.试验考察了预处理方法、pH值和重金属离子对吸附的影响,并对吸附机理进行了探讨.结果表明,在试验选用的预处理剂中,碳酸氢钠预处理的菌体吸附效果最好;溶液的pH值为5-6时,对染料的吸附量达到最大.当溶液中含有50mg·l-1Pb2+Zn2+Cu"任一种金属离子时,对菌体吸附中性红和孔雀绿均有抑制作用.碳酸氢钠处理菌体对中性红和孔雀绿的吸附过程可用准二级动力学模型来描述,相关系数均为0.9997.菌体吸附中性红和孔雀绿过程中有Na+,K+和Mg2+的释放,表明吸附过程中存在离子交换吸附机制.此外,吸附过程中静电吸附也起到一定的作用.     

壳聚糖交联螺旋藻小球对Cr(Ⅵ)的吸附作用研究

以壳聚糖和螺旋藻粉为原料,采用滴加成球的方法制备一种新型的重金属吸附剂——壳聚糖交联螺旋藻小球。通过反应温度、搅拌速度、提取时间和交联剂的加入量的条件控制研究壳聚糖交联螺旋藻小球的成球效果;通过正交试验设计研究壳聚糖交联螺旋藻小球对Cr(Ⅵ)的最佳吸附条件;通过SEM分析其表面和局部结构;通过吸附动力学实验研究其对Cr(Ⅵ)吸附过程。实验结果表明,(1)制备壳聚糖交联螺旋藻小球的成球效果受反应温度、搅拌速度、提取时间和交联剂的加入量的影响。交联剂戊二醛的最佳质量分数为50%,反应温度应控制在65℃左右。(2)各个因素对壳聚糖交联螺旋藻小球吸附Cr(Ⅵ)的影响强弱顺序为:Cr(Ⅵ)溶液的初始质量浓度壳聚糖与螺旋藻配比搅拌时间初始p H值。理论上壳聚糖交联螺旋藻小球吸附Cr(Ⅵ)溶液的最佳条件组合为:壳聚糖与螺旋藻配比为1∶1,Cr(Ⅵ)溶液初始质量浓度为120 mg·L~(-1),初始p H值为6,搅拌时间为2.5 h。利用此组合对Cr(Ⅵ)进行吸附研究,得出壳聚糖交联螺旋藻小球的吸附量达到24.795 mg·g~(-1),比正交试验中最大吸附量高出13.80 mg·g~(-1)。(3)壳聚糖交联螺旋藻小球的电镜扫描结果显示小球表面粗糙,具有疏松多孔网状结构。(4)吸附过程符合准二级动力学模型,基本符合准一级动力学模型。     

蒽醌染料中间体溴氨酸降解酶的特性

从污染地分离筛选出的菌株BX26对蒽醌染料中间体溴氨酸有显著的降解脱色作用,降解过程受降解酶的控制,试验结果表明,降解酶为溴氨酸诱导的胞外酶,该酶在温度高于50℃处理后失活,盐度对该酶失活有影响,盐度高于1%会显著降低该酶活力,酶对溴氨酸的催化脱色要有氧参加,氮气气氛中酶活受抑制。     

模拟酸雨对噬藻体PP失活率、野生藻的吸附率、裂解周期及释放量的影响

研究不同pH值的模拟酸雨对噬藻体PP失活率及噬藻体PP感染野生藻的吸附率、裂解周期及释放量的影响.用离心法测定了噬藻体PP对宿主藻的失活率、吸附率,用一步生长曲线法获得了噬藻体PP对宿主藻的裂解周期及释放量.结果表明,在pH 4.0～7.01的条件下:噬藻体PP 7 h的失活率分别为81.9%、74.8%、72.8%、67.1%,且pH4.0组的失活率显著高于与pH7.0组(对照组);噬藻体PP对野生藻的吸附率在45 min时达到最大值,分别为54%、56.9%、67.9%、68.8%,各处理组的最大吸附率均显著低于对照组;噬藻体PP感染野生藻的潜伏期均介于30～90 min之间,释放量分别约为42、52、29、104 PFU·mL-1,各处理组与对照组的释放量存在极显著差异.表明模拟酸雨对噬藻体感染动力学过程的影响具有重要的意义.     

好氧颗粒污泥对水溶液中酸性淡黄2G的生物吸附

利用好氧颗粒污泥对酸性淡黄2G溶液进行吸附脱色研究,考察了pH值、吸附剂用量、初始酸性淡黄2G的浓度、温度以及NaCl浓度对吸附过程的影响.实验结果表明,吸附过程对溶液pH值具有很高的依赖性,其最佳pH值为2.0.Temkin等温线在整个实验染料浓度范围内能够很好地描述吸附过程.吸附动力学符合准二级动力学模型.内部扩散和边界层扩散都可能影响生物吸附速率.热力学分析表明,吸附过程是一个自发的放热过程.采用FTIR分析的结果进一步揭示了颗粒污泥上官能团(如胺基、羧基和羟基等)可能是染料生物吸附的活跃结合位点.这些结果表明,好氧颗粒污泥可以作为吸附剂以去除水中的酸性淡黄2G。     

铁屑法处理含染料废水中铁屑表面化学研究

采用扫描电镜和X射线光电子能谱技术对铁屑法处理含染料废水中铁屑反应前后的表面进行了研究,结果表明：铁屑表面主要由Fe,C,O,S,Si以及其它构成铸铁的微量元素等组成．铁屑表面快速氧化是染料脱色的关键和前提步骤,铁屑表面铁的羟基氧化物增多是铁屑失活的重要原因．超声方法是铁屑再生方法之一,铸铁中的硫有助于染料脱色．     

NKY功能化树脂静态吸附混合染料的研究

探讨了NKY功能化树脂对混合染料(活性艳蓝：KN-R和活性艳橙K-GN)的静态吸附行为．结果表明：NKY树脂吸附单组分染料的能力大于其对混合染料的吸附，而且对混合体系中的染料有一定的选择性，吸附KN-R的速率较大．从动力学研究来看，NKY对混合染料的吸附速率其决定步骤是液膜扩散．等温曲线的结果显示，NKY对混合染料中每种组分的吸附行为同吸附单组分体系的类似，同时，随温度的升高，吸附速率常数增大，标准自由能变的绝对值增大。     

聚乙烯醇-海藻酸钠固定香菇废弃物吸附Pb和Cd的最佳配方

选用香菇废弃物作为生物吸附剂,用聚乙烯醇(PVA)-海藻酸钠(SA)同定香菇粉制成PVA-SA固定香菇,以吸附溶液中铅(Pb)和镉(Cd)的能力为主要评价指标,结合成球性、机械强度和耐酸性等,通过正交试验确定出吸附Pb的PVA-SA固定香菇最佳配方是8%PVA+1%SA+3%香菇粉+2%CaCl2的饱和H3BO3,对Pb的吸附率为95.4%,吸附Cd的PVA-SA同定香菇的最佳配方是5%PVA+1%SA+3%香菇粉+2%CaCl2的饱和H3BO3,对Cd的吸附率为63.7%.二小球的成球性、机械强度和耐酸性都较好.Langmuir等温吸附模型能最好地拟合香菇吸附Pb的热力学过程,相关系数R2达0.993 9;Freundlich模型能更好地描述香菇吸附Cd的热力学过程,R2为0.999 3.Freundlich等温吸附模型适合描述PVA-SA同定香菇吸附Pb和Cd的热力学过程,R2分别为0.958 7和0.982 3.自由香菇对Cd的理论最大吸附量qm-Langmuir (2.832 1 mg g-1)小于PVA-SA固定香菇的理论最大吸附量qm-Langmuir (6.447 5 mg g-1),自由香菇吸附Pb的Freundlich模型参数k(0.312 7)小于PVA-SA固定香菇吸附Pb的k(0.431 0),香菇固定后吸附Cd和Pb的能力有所提高.PVA-SA固定香菇吸附Pb和Cd的吸附平衡时间分别为3 h和7 h,比自由香菇吸附Pb和Cd的平衡时间(1 h)长.伪二级动力学模型能很好地拟合固定香菇吸附Pb和Cd的动力学过程,R2分别为0.999 9和0.994 6,由该模型计算出的对Pb和Cd的平衡吸附量理论值分别为0.453 6 mg g-1和0.2060 mg Cd g-1.伪二级动力学模型能很好地拟合同定香菇吸附Pb和Cd的动力学过程,由该模型计算出的固定香菇对Pb和Cd的平衡吸附量理论值分别为0.453 6 mg g-1和0.206 0 mg g-1,自由香菇对Pb和Cd的平衡吸附量理论值分别为1.817 2 mg g-1和0.842 5 mg g-1.PVA-SA固定香菇吸附Pb/Cd的伪二级动力学反应速率常数k2为1.324 1/1.253 1,自由香菇吸附Pb/Cd的k2为0.780 510.213 0,自由香菇吸附Pb/Cd的k2大于固定香菇的k2,表明固定香菇吸附Pb/Cd达到平衡所需要的时间比自由香菇所需要的时间长.图3表6参16     

Biosorption of Cd2+ and Cu2+ on immobilized Saccharomyces cerevisiae

The biosorption of Cd²⁺ and Cu²⁺ onto the immobilized Saccharomyces cerevisiae (S. cerevisiae) was investigated in this study. Adsorption kinetics, isotherms and the effect of pH were studied. The results indicated that the biosorption of Cd²⁺ and Cu²⁺ on the immobilized S. cerevisiae was fast at initial stage and then became slow. The maximum biosorption of heavy metal ions on immobilized S. cerevisiae were observed at pH 4 for Cd²⁺ and Cu²⁺. by the pseudo-second-order model described the sorption kinetic data well according to the high correlation coefficient (R ²) obtained. The biosorption isotherm was fitted well by the Langmuir model, indicating possible mono-layer biosorption of Cd²⁺ and Cu²⁺ on the immobilized S. cerevisiae. Moreover, the immobilized S. cerevisiae after the sorption of Cd²⁺ and Cu²⁺ could be regenerated and reused.     

Removal of Novacron Golden Yellow dye from aqueous solutions by low-cost agricultural waste: Batch and fixed bed study

The present work describes the removal of Novacron Golden Yellow (NGY) dye from aqueous solutions using peanut hulls. The experiments were performed with native, pretreated and immobilised forms of peanut hulls. The effect of various operational parameters (pH, biosorbent dose, initial dye concentration and temperature etc.) was explored during batch study. NGY showed maximum removal at low pH and low biosorbent dose. High initial dye concentration facilitated the biosorption process. Maximum dye removal with native, pretreated and immobilised biomass was found to be 35.7, 36.4 and 15.02 mg/g respectively. The experimental data were subjected to different kinetic and equilibrium models. The kinetic data confirmed the fitness of pseudo-second-order rate law for NGY biosorption. The equilibrium modelling was carried out by Freundlich, Langmuir and Temkin models. The isothermal data of NGY removal were best described by Freundlich adsorption isotherm. Negative values of Free energy change (Δ G⁰) for NGY with native and pretreated biomass depicted the spontaneous nature of biosorption process. In column mode, the effects of bed height, flow rate and initial dye concentrations were optimised. Maximum NGY biosorption (7.28 mg/g) was observed with high bed height, low flow rate and high initial concentration in continuous mode. Bohart–Adams model best fitted to the data obtained from column studies. The results indicated that the peanut hulls could be used effectively for the removal of dyes containing wastewater.     

溶液中多种金属离子共存对毛木耳生物吸附能力的影响

用毛木耳(Auricularia polytricha)菌丝体的死细胞作为生物吸附剂吸附溶液中的Cd 2+、Cu 2+和Pb 2+.用原子吸收分光光度计测定吸附前后溶液金属离子的变化,研究了溶液中两种离子共存对毛木耳吸附能力的影响.结果表明:溶液中Pb2+的存在抑制了毛木耳对Cd2+的吸附,是负向干扰;Cd2+的存在促进了毛木耳对pb2+的吸附,是正向干扰;Cu2+的存在促进了毛木耳对pb2+的吸附,是正向干扰;Pb2+的存在抑制了毛木耳对Cu2+的吸附,是负向干扰;Cd2+对Cu2+的影响作用不如Cu2+对Cd2+的影响明显.实验结果为毛木耳作为重金属污染废水的处理材料提供理论依据.     

Equilibrium,kinetics and thermodynamics of hexavalent chromium biosorption on pristine and zinc chloride activated Senna siamea seed pods

Hexavalent chromium contamination in water is an issue of huge concern due to its use at a high scale, toxicity and non-biodegradability. Biosorption is a cost effective and unconventional strategy for the elimination of Cr(VI). Here, a novel biosorbent Senna siamea seed pod biomass and its chemically activated form have been investigated for the elimination of hexavalent chromium from aqueous solution. The biosorbent was characterized by using BET, FTIR, FESEM-EDX and TGA techniques. Parameters controlling the biosorption process were optimized as pH 2.0, temperature 30°C, initial Cr(VI) concentration 500?mg/L, biosorbent dose 0.5?g/L. Optimized contact time was 210 and 180 min for pristine biomass and activated carbon, respectively. Langmuir isotherm correlated well with experimental data revealing that the biosorption occurred in monolayer pattern. Maximum biosorption capacity calculated by Langmuir biosorption isotherm was 119.18 and 139.86?mg/g for S. siamea pristine biomass and activated carbon, respectively. Pseudo-second order kinetic model correlated well with experimental data. Thermodynamic studies suggested that the biosorption process occurs in a non-spontaneous, stable and endothermic manner. These interesting findings on Cr(VI) biosorption by S. siamea seed pod biomass and S. siamea zinc chloride activated carbon vouches for its potential application as an unconventional biosorbent.     

Modelling the kinetics and equilibrium properties of cadmium biosorption by river green alga and water hyacinth weed

Cadmium biosorption properties of non-living, dried river green alga from a river source, and water hyacinth weed, Eichhornia crassipes from a lake in Zimbabwe have been investigated. The cadmium uptake was found to depend on initial pH, uptake being apparently minimal at low pH values and increasing with an increase in pH. Cadmium biosorption kinetics by both samples is fast, with 80% of total uptake occurring within 60?min. The effect of initial solution pH and initial cadmium concentration on cadmium biosorption from a cadmium solution has been studied. The data for algal biomass fitted the Langmuir monolayer adsorption isotherm, while the biosorption of the metal by water hyacinth weed fitted the Freundlich adsorption isotherm with 1/n values all less than 1. Maximum metal uptake capacities were recorded using 0.35?g of biomass and a 250?mg?L^?1 cadmium solution at pH 6.5 and at 25°C and these were about 85 and 50?mg?L^?1 for water hyacinth weed and green alga, respectively, showing that water hyacinth weed offered a greater potential for cadmium uptake. The absorption was described by pseudo-second order rate model and the rate constant and equilibrium sorption capacity are reported.     

Kinetic and equilibrium models for the biosorption of Cr(III) on Streptomyces rimosus

This study focused on the biosorption of trivalent chromium onto mycelial bacterium (Streptomyces rimosus) biomass from effluent of tannery. The biomass was prepared by treatment with alkali. Fourier transforms-infra red analysis of the mycelial bacterial revealed the presence of carboxyl groups as possible binding sites. Experimental parameters affecting biosorption processes such as pH contact time were studied. Langmuir, Freundlich, and Temkin models were applied to describe the biosorption isotherms. The Langmuir model fitted the equilibrium data better than the Freundlich isotherm. The biosorption capacity of S. rimosus biomass for trivalent chromium was found to be 83 mg g^?1 at pH 4.8 and 3 g L^?1 biomass dosage, 300 min equilibrium time and 20°C. Kinetic evaluation of experimental data showed that the biosorption processes of trivalent chromium followed pseudo-second-order kinetics well.     

Biosorption of low level Cd~（2＋） in water by Aspergillus sojae

以酱油曲霉（Aspergillus sojae）为吸附剂,对水溶液中微量Cd2＋进行了吸附研究.实验考察了预处理方法、菌体用量、pH、温度和吸附时间对吸附的影响,同时分析了其吸附动力学和吸附等温线特性,并对酱油曲霉菌体吸附Cd2＋的可能作用机理进行了探讨.结果表明,碱预处理的菌体吸附效果最好.在菌体用量为0.08 g时,对Cd2＋的吸附量达到最大,为0.095 mg.g-1.pH值在3.4—8之间,酱油曲霉菌体对Cd2＋的吸附效果比较稳定,其最大吸附率出现在pH 3.4.温度在15℃—30℃之间时,菌体对Cd2＋的吸附率差异很小,吸附率在88.3%—94.4%之间.二级动力学方程能很好地表征酱油曲霉吸附微量Cd2＋的过程,R2在0.99以上,其吸附平衡时间大约2.5 h,线性模型更适于描述该吸附平衡过程.SEM、FTIR分析得出,Cd2＋可能是与酱油曲霉菌体表面的羟基、酰胺基、羧基、磷酸基和胺基等基团相络合而被吸附,也可能是形成颗粒沉淀而附着在菌丝上.     

Biosorption of Cu2+ from aqueous solutions by pretreated Cladosporium sp

In this paper, adsorption properties of a pretreated of Cladosporium sp. for Cu2 were studied. The fungi pretreated with some chemical reagents exhibited higher Cu2+ removal capacities than native biomass. The optimum chemical reagent was 0.2M NaOH. After 0.2M NaOH pretreatment, optimum conditions of biosorption were found to be pH 5.0, temperature 35 degrees C, and stirring speed of 100rpm. Equilibrium isotherms were obtained from adsorption experiments and the biosorption maximun capacity obtained was at 28.31mg/g. The biosorbed metal ions were effectively eluted by 0.05M HNO3 solution. After eluting, the biosorbed metal ions biomass was regenerated by washing with deionized water and then contacted with a solution containing 0. 1M of Ca2+, Mg2+ ions before further adsorption tests. The pretreated fungi biomass could be used for three cycles: biosorption, elution of biosorbed ion, regeneration of biomass.     

Biosorption of hexavalent chromium and malachite green from aqueous effluents,using Cladophora sp.

Biosorption potential of green macroalgae Cladophora sp., (GAC) for the removal of hexavalent chromium (Cr(VI)) and malachite green (MG) from aqueous medium was investigated. Optimal conditions for biosorption experiments were determined as a function of initial pH, GAC dosage, temperature and initial concentration of Cr(VI) and MG. The biosorption equilibrium data were fitted with the isotherm models of Langmuir, Freundlich, Kiselev, Frumkin and Jovanovic, while the experimental data were analysed using the kinetic models such as pseudo-first-order, pseudo-second-order, Ritchie's and intraparticle diffusion. The Langmuir maximum biosorption capacity was calculated as 100.00?mg/g (Cr(VI)) and 142.85?mg/g (MG). The biosorption kinetic data showed better agreement with the pseudo-second-order kinetic model. The thermodynamic parameters indicated spontaneous and endothermic nature of the biosorption process for Cr(VI) removal, whereas exothermic in the case of MG removal. Furthermore, the biosorption efficiencies of the GAC reusability were found significant up to five cycles and tested using 0.1, 0.5 and 1.0?M HCl, respectively. The results of the present study indicated that GAC is a suitable biosorbent for the sequestration of Cr(VI) and MG from aqueous solutions.