三乙烯四胺修饰啤酒废酵母吸附Hg（Ⅱ）的性能

将三乙烯四胺修饰到戊二醛交联的啤酒废酵母菌表面,合成了一种新的生物吸附剂。 研究了它吸附Hg(Ⅱ)的性能及影响吸附行为的因素。 结果表明,修饰啤酒废酵母菌吸附Hg(Ⅱ)的适宜条件是:2.5 ℃,吸附溶液的pH=2.8,吸附平衡时间20 min,对汞的吸附容量为132.6 mg/g,是未修饰菌的6.3倍。 该法静态处理含汞模拟废水(4.9~17.5 mg/L),汞去除率可达100%。 吸附动力学用准二级方程拟合,相关系数R2=0.999 9。 判定Langmuir模型更适合描述吸附Hg(Ⅱ)的过程,表明是单分子层吸附。     

辛巴蓝F-3GA修饰的啤酒废酵母菌亲和吸附溶菌酶

利用j嗪染料辛巴蓝F-3GA修饰经戊二醛交联的啤酒废酵母菌,得到一种新型染料亲和吸附剂.辛巴蓝F-3GA的固载量为161.1 mg/g.以溶菌酶为研究对象,考察吸附时间、酶初始浓度、pH值、离子强度等因素对吸附率的影响.结果表明:当pH=7.0时,其对溶菌酶有较高的吸附量(229.1 mg/g),吸附性能明显优于未接枝...     

纳米金/碳催化剂的合成及其在多巴胺电化学检测中的应用(英文)

建立了一种合成碳负载型金纳米颗粒(AuC)的新方法.将酵母菌、葡萄糖及HAuCl4溶液混合后置于恒温摇床中,在310K下振荡数天得到酵母菌吸附的金前体盐(AuY);将AuY在氮气气氛中1 273K下煅烧得到AuC.采用扫描电镜和透射电镜观察了AuC的形貌;将AuC修饰在玻碳电极上并用于多巴胺的电化学检测.结果表明,AuY培养3d后,其酵母菌颗粒粒径分布不均匀,这主要是由于大量葡萄糖的吸附和包裹以及酵母孢子的存在所致;而AuY培养6d后得到的金颗粒粒径分布均匀,粒径约为10nm.此外,AuC在多巴胺电化学检测中具有非常好的响应,且检出限较低,其电化学过程为混合动力学控制过程.     

化学修饰吸附树脂对水中邻苯基苯酚的吸附研究

研究了以不同基团修饰的吸附树脂对水中邻苯基苯酚的吸附行为,考察了吸附温度、时间、溶液浓度和吸附剂的种类对邻苯基苯酚的吸附效率的影响.结果表明:实验条件下,化学修饰的吸附树脂对邻苯基苯酚较佳的吸附温度为303K,具有丰富羰基基团修饰同时具有合适孔径的吸附树脂及更好的吸附效果,吸附等温线更符合Langmuir方程,吸附动力学符合Lagergren准一级动力学吸附方程.     

吸附树脂的修饰官能团设计及其吸附机理研究

利用AM1半经验计算法计算出用不同官能团修饰的聚苯乙烯型吸附树脂的前线轨道能量值.设计筛选出合适的官能团,根据吸附质的分子尺寸,修饰合成出具有匹配孔径、较大比表面积的吸附树脂.在303K下,测定了它们对不同取代基的酚类化合物的吸附等温线.以Amberlite XAD-4作参照,比较了吸附剂的吸附效果,并阐明了吸附机理.     

介孔材料氨基表面修饰及其对CO2的吸附性能

采用接枝方法在介孔材料MCM-41和SBA-15的孔道内表面进行氨基化修饰, XRD、29Si-NMR、FT-IR、TGA、BET等测试结果表明, 氨丙基三乙氧基硅烷(APTS)和氨乙基氨丙基甲基二甲氧基硅烷(AEAPMDS)都分别接枝在介孔材料的孔道内, 表面氨基修饰量约为1.5-2.9 mmol·g-1. 表面修饰后介孔材料的孔道仍高度有序, 但比表面积减小. 表面修饰前后介孔材料对CO2的吸附性能发生显著变化, 由于物理吸附转化为以氨基为活性中心的化学吸附, 吸附量从修饰前的0.67 mmol·g-1提高到2.20 mmol·g-1.     

氨基修饰超高交联树脂对没食子酸的吸附性能

以亲水性小分子有机酸没食子酸作为研究对象,研究了氨基修饰超高交联树脂对没食子酸的吸附行为和机理.结果表明,氨基修饰超高交联树脂WJN-10对没食子酸有较高的吸附容量和吸附作用力;π-π共轭作用是树脂WJN-10吸附没食子酸主要作用力;WJN-10吸附没食子酸是物理吸附主导;吸附速率主要受控于颗粒内扩散过程;WJN-10对没食子酸有较好的吸附-脱附性能.     

富羧类吸附树脂对水溶液中HIPI的吸附研究

以NDA99和NDA150树脂作为参照,通过等温吸附实验和吸附动力学实验探讨了修饰后的树脂对水溶液中5-对羟基苯基海因(HIPI)的吸附性能和机理.结果表明:羧基修饰的超高交联吸附树脂(FZH124)比NDA99和NDA150树脂对水溶液中HIPI具有更好的吸附效果,而且在303K时吸附效果最好.Langmuir和Freundlich方程均能较好拟合修饰树脂对HIPI的吸附等温线.HIPI在FZH124树脂上的动态吸附符合准一级动力学方程,303K时,树脂对HIPI的吸附速率最大,颗粒内扩散过程是该吸附过程的主要控制步骤.     

偏苯三酸酐修饰的树脂对邻苯二甲酸的吸附研究

用颗粒活性炭作比较,通过等温吸附实验和吸附动力学实验研究了偏苯三酸酐修饰的吸附树脂对邻苯二甲酸的吸附性能及吸附机理。结果表明,偏苯三酸酐修饰的树脂对邻苯二甲酸具有良好的吸附效果,吸附量随着温度的升高而下降。Freundlich吸附等温方程很好地拟合邻苯二甲酸在偏苯三酸酐修饰的树脂上的吸附行为。吸附焓变结果表明,吸附过程是以放热的物理吸附为主,且焓变的绝对值均随着吸附量的增大而减小。邻苯二甲酸在偏苯三酸酐修饰的树脂上的吸附过程符合准一级动力学方程,颗粒内扩散是吸附过程的主要控制步骤。     

复合功能树脂对水体中天然有机酸的吸附

合成了胺基修饰复合功能树脂WJN-07, 研究了富里酸、单宁酸和没食子酸在树脂上的吸附行为. 与去除DOM的商品树脂XAD-7相比, 树脂WJN-07对3种天然有机酸有较高的吸附容量, 这是由于新型树脂表面具有修饰的化学官能团和丰富的微孔结构所致. 选择单宁酸作为吸附质进行吸附热力学研究, 结果表明, 树脂WJN-07对单宁酸的吸附为吸热过程, 以化学吸附为主导. 溶液中重金属离子Pb²⁺作为影响树脂吸附性能的重要因素在实验中得到证实, 其作用机理也得到合理解释.     

Insight into the adsorption of dyes onto chitin in aqueous solution: An experimental and computational study

This study aimed to get an insight into the adsorption of three synthetic dyes onto chitin using experimental and computational approaches. The successful preparation of α-chitin was confirmed using the Fourier Transform Infrared (FTIR) and X-ray Diffraction (XRD). In addition, the presence of porous and fiber on the surface of the extracted chitin was revealed by the Scanning Electron Microscopy (SEM) analysis. The extracted α-chitin was then used as an adsorbent to remove synthetic dyes, namely Malachite green, Basic red 18, and Alizarin yellow R. The kinetic study showed that the adsorption of dyes was well-described using a pseudo-second-order model, whereas the isotherm adsorption obeyed the Freundlich model. The Frontier Molecular Orbital (FMO) revealed several locations of dyes and chitin molecules that are potentially active sites for adsorption. The adsorption trend could be related to the Highest Occupied Molecular Orbital (HOMO) – Lowest Unoccupied Molecular Orbital (LUMO) energy gap and electrophilicity index of the dyes. The Conductor-like Model for Real Solvent (COSMO-RS) model demonstrated, for the first time, that several interactions occurred during the adsorption of dyes onto α-chitin. For the Malachite green and Basic Red 18, the Van der Waals forces of the dyes controlled its adsorption behavior. In contrast, the hydrogen bonding interaction governed the adsorption behavior of Alizarin yellow R dye onto α-chitin. The gathered insight from this work might guide us better to understand the molecular level of dyes–chitin interactions and, ultimately, to design adsorbents to remove synthetic dyes from wastewater.     

Synthesis and Dyes Adsorption Properties of Calix[4]crown-grafted Chitosan Chelating Polymer

By the Schiff-base condensation of formacyl calix[4]crown(2) with raw chitosan, a novel calix[4]crown- grafted chitosan chelating polymer(3) was conveniently prepared in good yield. The structure of polymer 3 was confirmed by elemental analysis, infrared(IR) spectrometry and X-ray diffraction(XRD) analysis. The elemental analysis suggests that the grafting degree of calixcrown unit was 22% on the amino groups of chitosan. The morphological characteristic of polymer 3 was studied by scanning electron microscopy(SEM). Polymer 3 possessed loose porous and smooth morphology of surface. The dyes adsorption abilities of polymer 3 for a series of organic dyes[Orange I(OI), Neutral red(NR), Victoria blue B(VB) and Brilliant green(BG)] were studied by solid-liquid adsorption experiments. The adsorption percentages increased from 45%―60%(raw chitosan for dyes) to 75%―90%(polymer 3 for dyes). The highest adsorption percentage reached 89% for VB. The saturated adsorption capacities for OI, NR, VB and BG were as high as 622, 564, 854 and 781 mg/g, respectively. The adsorption abilities kept stable at 70%―90% in the scope of pH=5―9. The adsorption abilities for anionic dye(OI) decreased gradually with the increase of pH and the opposite trend was observed for cationic dyes(NR, BG, VB). The adsorption percentages were 70%―90% after five times' cycles for adsorption.     

Adsorption of direct dyes from aqueous solutions by carbon nanotubes: determination of equilibrium, kinetics and thermodynamics parameters

This study examined the feasibility of removing direct dyes C.I. Direct Yellow 86 (DY86) and C.I. Direct Red 224 (DR224) from aqueous solutions using carbon nanotubes (CNTs). The effects of dye concentration, CNT dosage, ionic strength and temperature on adsorption of direct dyes by CNTs were also evaluated. Pseudo second-order, intraparticle diffusion and Bangham models were adopted to evaluate experimental data and thereby elucidate the kinetic adsorption process. Additionally, this study used the Langmuir, Freundlich, Dubinin and Radushkevich (D-R) and Temkin isotherms to describe equilibrium adsorption. The adsorption percentage of direct dyes increased as CNTs dosage, NaCl addition and temperature increased. Conversely, the adsorption percentage of direct dyes decreased as dye concentration increased. The pseudo second-order model best represented adsorption kinetics. Based on the regressions of intraparticle diffusion and Bangham models, experimental data suggest that the adsorption of direct dyes onto CNTs involved intraparticle diffusion, but that was not the only rate-controlling step. The equilibrium adsorption of DR86 is best fitted in the Freundlich isotherm and that of DR224 was best fitted in the D-R isotherm. The capacity of CNTs to adsorb DY86 and DR224 was 56.2 and 61.3 mg/g, respectively. For DY86, enthalpy (DeltaH(0)) and entropy (DeltaS(0)) were 13.69 kJ/mol and 139.51 J/mol K, respectively, and those for DR224 were 24.29 kJ/mol and 172.06 J/mol K, respectively. The values of DeltaH(0), DeltaG(0) and E all indicate that the adsorption of direct dyes onto CNTs was a physisorption process.     

Removal of cationic dyes by modified waste biosorbent under continuous model: Competitive adsorption and kinetics

Modified waste sugarcane bagasse (SCB) was prepared to remove cationic dyes: methylene blue and rhodamine B from aqueous solution by using a continuous mode. Effects of flow rate on adsorption of the two dyes in fixed bed column were studied. Competitive adsorption kinetics of the two dyes in binary system was investigated in detail. Results showed that the adsorption capacities of the modified sorbent for methylene blue and rhodamine B in one component system were 1.7 and 0.4 mmol g^?1, respectively. Competitive adsorption process in the binary system could be divided into three phases: free adsorption, substitution adsorption and adsorption equilibrium. 0.19 mmol of rhodamine B absorbed was replaced by 0.35 mmol of methylene blue in the second phase. Simple modified Yoon–Nelson model was used to predict the adsorption kinetics for the first time. The obtained adsorption rate constants for the two dyes in the three phases both followed the order: phase I > phase III > phase II, demonstrating that substitution adsorption phase is the rate determining step. Desorption experiment showed that the loaded two dyes could be separated and recycled by using the mixture solution of HCl (0.1 mol L^?1) and ethanol as eluent. The prepared fixed bed column had great potential in industrial wastewater treatment.     

循环伏安法研究光谱增感染料在溴化银上的吸附

用循环伏安法和电子显微镜研究了不同类型的染料在溴化银上的吸附,使用了电沉积在铂上的溴化银电极作为照相乳剂的模型,证明了由于染料电荷的不同,其在AgBr/Br^-表面上的吸附也不同,正性染料被吸附时,形成难溶的表面络合物,和负性染料相作用时,形成易溶的表面络合物,而当AgBr与非菁负性染料作用时,则由于负电排斥而不形成络合物。因此,利用循环伏安法可以判断不同染料的吸附情况。本文还研完了超增感及Riester提出的‘强色增感’中的吸附情况。实验结果表明在AgBr上染料的排列次序取决于其吸附强度。本工作还证明了Reister所提出的‘强色增感剂’的作用机理是可信的。     

Adsorption of basic dyes onto montmorillonite

Ca-montmorillonite (Ca-Mont) was exchanged with titanium cations and the adsorption equilibrium and kinetics of Basic Green 5 (BG5) and Basic Violet 10 (BV10) on these montmorillonites were measured to examine the ion-exchange effects on the basic dyes adsorption. The relationship between the dye adsorption and the alteration of pore structures of montmorillonite induced by ion-exchange processes was discussed. Moreover, the changes in the surface and pore structure of montmorillonites during adsorption were characterized based on classical and fractal analyses of the nitrogen adsorption isotherms as well as the XRD patterns. The decrease in BET surface area of montmorillonites after adsorption of dyes was interpreted in terms of both the coverage of some surface roughness (surface screening effect) and the inhibition of the movement of nitrogen molecule into some pores (pore blocking effect). The surface fractal dimension D was used to examine whether or not the surface screening effect exists and the pore blocking effect was examined with the changes of mean pore size before and after adsorbing basic dyes.     

Adsorption studies on the removal of Vertigo Blue 49 and Orange DNA13 from aqueous solutions using carbon slurry developed from a waste material

Waste material (carbon slurry), from fuel oil-based generators, was used as adsorbent for the removal of two reactive dyes from synthetic textile wastewater. The study describes the results of batch experiments on removal of Vertigo Blue 49 and Orange DNA13 from synthetic textile wastewater onto activated carbon slurry. The utility of waste material in adsorbing reactive dyes from aqueous solutions has been studied as a function of contact time, temperature, pH, and initial dye concentrations by batch experiments. pH 7.0 was found suitable for maximum removal of Vertigo Blue 49 and Orange DNA13. Dye adsorption capacities of carbon slurry for the Vertigo Blue 49 and the Orange DNA13 were 11.57 and 4.54 mg g(-1) adsorbent, respectively. The adsorption isotherms for both dyes were better described by the Langmuir isotherm. Thermodynamic treatment of adsorption data showed an exothermic nature of adsorption with both dyes. The dye uptake process was found to follow second-order kinetics.     

具有超高阳离子染料去除能力的磺酸功能化球形共价有机框架

通过三醛基间苯三酚(TFP)与2,2′-联苯胺二磺酸(BDSA)的席夫碱反应, 合成了β-酮烯胺连接的磺酸功能化球形共价有机框架(TFP-BDSA COF). 所得阴离子型TFP-BDSA可迅速吸附如亚甲基蓝(MLB)、 结晶紫(CV)和罗丹明B(RhB)等阳离子染料, 而对如甲基橙(MO)和荧光素钠(FS)等阴离子染料则难以吸附, 该COF可实现基于电荷模式的阴离子、 阳离子染料的分离. TFP-BDSA对阳离子染料的吸附动力学均遵循拟二级吸附动力学模型, 吸附过程符合Langmuir吸附模型, 其对MLB, CV和RhB的最大吸附容量分别高达1116, 1429和1638 mg/g. 与其它COFs材料相比, TFP-BDSA对CV和RhB的吸附容量最高. 该工作可为开发功能COFs材料实现对废水中有机污染物的快速吸附和有效去除提供参考.     

Adsorption of xanthene dyes by lysozyme crystals

Adsorption characteristics of cross-linked lysozyme crystals of different morphologies (tetragonal, orthorhombic, triclinic and monoclinic) were examined using four anionic dyes (fluorescein, eosin, erythrosin, and rose bengal), one zwitterionic dye (rhodamine B), and one cationic dye (rhodamine 6G). The adsorption isotherms were of the Langmuir type for all examined systems with the exception of rhodamine B adsorption by monoclinic crystals. The weakest adsorption was observed for the cationic dye, rhodamine B, whereas dianionic dyes, eosin, rose bengal, and erythrosin were strongly adsorbed on the protein surface. The adsorption capacities of the crystals for the dyes were found to depend on both charge and hydrophobicity of the dye, reflecting the heterogeneous character of the lysozyme pore surface. The adsorption affinity of the crystals for the dyes was a function of the dyes' hydrophobicity. Furthermore, the crystal morphology was identified as an additional factor determining capacity and affinity for dye adsorption. Differences between crystals prepared in the presence of the same precipitant were lower than between morphologies prepared with different precipitants.