改性壳聚糖树脂对利尿剂的吸附性能

用琥珀酸酐、苯甲酸酐、聚乙烯亚胺和 3 氯 2 羟丙基三甲基氯化铵对壳聚糖进行改性 ,分别在其氨基上引入羧基、苯环、多氨基和季胺基 ,并利用红外谱图对于改性后的壳聚糖的结构进行了分析 .应用相转移法制备了 4种改性壳聚糖的微球 ,实验研究了这 4种微球对 9种不同利尿剂的吸附性能 .结果表明 ,由于Lewis酸碱相互作用 ,引入羧基后的壳聚糖树脂对 3种碱性利尿剂的吸附量有了 15 %～ 36 %的提高 ,而引入多氨基的壳聚糖树脂对四种酸性利尿剂的吸附量分别提高了 4 8 5 %～ 2 0 9% ;由于苯环和利尿剂的憎水性基团的相互作用 ,引入苯环后的壳聚糖树脂对所有的利尿剂的吸附量都有所提高 ,其幅度为 15 %～ 6 1% ;因为季胺基团和羧基之间发生的离子交换作用 ,引入季胺基后的树脂对具有羧基的利尿剂吸附量有显著的提高 ,尤其对布美它尼的吸附量提高了 2倍以上 .     

交联壳聚糖多孔微球对染料的吸附平衡及吸附动力学分析

研究了交联壳聚糖多孔微球对染料的吸附平衡规律,探讨了染料溶液在不同的初始浓度、pH值及不同吸附剂用量条件下吸附动力学规律及吸附动力学控制机理。结果表明,壳聚糖微球对染料的吸附规律可较好地符合Langmuir吸附等温式,吸附动力学模型可以用表观二级速率方程来描述。     

胺基化壳聚糖树脂吸附分离茶多酚的研究

对珠状壳聚糖树脂进行胺基化改性,制备了胺基化珠状壳聚糖树脂,并用FTIR对胺基化珠状壳聚糖树脂进行了结构表征。利用该树脂对绿茶中茶多酚进行吸附分离,探讨了其吸附条件,考察了其吸附性能。结果表明,胺基化壳聚糖树脂对茶多酚的吸附既符合Langmuir等温式,也符合Freundlich等温式;本实验最佳吸附条件为:温度25℃,茶汤溶液pH值5,吸附时间2h;最大吸附量达到486.0mg/g。     

胺基化PGMA交联微球对胆红素的吸附机理

通过胺基与环氧键之间的开环反应, 用己二胺及多乙烯多胺等小分子胺化试剂对聚甲基丙烯酸缩水甘油酯(PGMA)交联微球进行了化学改性, 制得了胺基化的PGMA交联微球, 研究了该功能微球对胆红素的吸附特性, 考察了胺化试剂的分子结构、介质pH值、离子强度及温度等因素对其吸附性能的影响, 较深入地研究了吸附机理. 实验结果表明, 胺基化微球对胆红素具有强吸附作用, 吸附容量可达17.80 mg·g-1, 等温吸附服从Freundlich方程. 胺基化微球与胆红素分子之间的作用力以静电相互作用为主, 同时也存在氢键作用与疏水相互作用. 在pH 值为6 的介质中二者之间的静电作用最强, 胆红素吸附容量最高. 高离子强度不利于静电相互作用, 盐度增大使吸附容量减小. 温度升高有利于疏水相互作用而不利于氢键作用, 两种作用中占优势者主导温度对吸附容量的影响. 用己二胺改性的微球, 由于疏水相互作用的强化以及较长连接臂导致较小的空间位阻, 使其对胆红素的吸附能力明显高于多乙烯多胺改性的微球.     

染料壳聚糖微球的制备及其对牛血清白蛋白(BSA)吸附性能的研究

采用反相悬浮交联法制备壳聚糖微球,对微球进行羟丙基氯化及氨基化,并偶联色素配体Cibacron Blue F3GA,得到一种新型染料亲和吸附剂.以牛血清白蛋白(BSA)为目标蛋白,考察了该染料亲和吸附剂的吸附性能,发现其对BSA有较高的吸附量(95.2mg/g),吸附行为满足Langmuir吸附等温式.负载牛血清白蛋白的微球容易洗脱,洗脱率高达99％.     

新型胺基壳聚糖树脂的合成及其对胆红素吸附性能的研究

以壳聚糖为原料，经羟丙基氯化、胺基化，制备了一种新型胺基壳聚糖树脂，研究了该树脂对胆红素的吸附性能。结果表明：胺基壳聚糖树脂的胺基含量比壳聚糖高，该树脂对游离胆红素的吸附在3h基本达到平衡，吸附量随着胺基含量增加而增加，树脂的吸附性能受温度、离子强度影响。胺基壳聚糖树脂对血清白蛋白结合胆红素的吸附量大于壳聚糖，但低于对游离胆红素的吸附。     

磁性壳聚糖硅胶复合微球的制备及其吸附Cu~(2+)的性能研究

以壳聚糖与正硅酸四乙酯为原料,采用溶胶-凝胶法,用戊二醛辅助交联合成了磁性壳聚糖硅胶复合微球。通过红外光谱、扫描电镜、X-射线衍射等方法对磁性壳聚糖硅胶复合微球的形态和组成特性进行分析,制备的磁性复合微球中壳聚糖与硅胶材料复合均匀,材料粒径均一,机械强度较高。考察了制备的磁性壳聚糖硅胶复合微球对Cu~(2+)的吸附性能,结果表明微球对Cu~(2+)具有较好的吸附性能,吸附容量达到98.7mg/g。     

壳聚糖吸附Cd2+的机理

壳聚糖分子中的大量氨基及部分酰胺基的存在 ,能够选择性地配位或吸附一些金属离子 ,尤其是对过渡金属离子具有较好的螯合能力。Ｐｉｒｏｎ等[2 ] 利用放射性85Ｓｒ研究了壳聚糖的氨基与碳酸锶离子对Ｓｒ2 +、ＣＯ2 -3 之间形成的三元络合物的结构。季君晖[3] 通过光电子能谱研究发现 :壳聚糖螯合Ｃｕ2 +,只与壳聚糖中的—ＮＨ2 配位。Ｔｓｅｚｏｓ[4] 利用ＩＲ、ＭＳ和ＥＰＲ说明铀与壳聚糖的络合点为氨基的氮原子。Ｇｕｉｂａｌ等[5] 用ＩＲ、ＣＰ ＭＡＳ1 3ＣＮＭＲ及反射光谱法证实吸附机理涉及氨基。含镉废水是危害较大的工业废水之一 …     

磁性壳聚糖微球的制备及对Cr(Ⅵ)的吸附性能研究

用壳聚糖包埋磁流体,用戊二醛交联制成磁性壳聚糖微球,并用红外光谱表征其结构。用制备的磁性壳聚糖微球吸附Cr(Ⅵ)离子,考察了其对Cr(Ⅵ)离子的吸附性能;探讨了吸附时间、溶液pH值、吸附剂用量、温度、Cr(Ⅵ)起始浓度以及其他离子存在对Cr(Ⅵ)离子去除率的影响。实验结果表明,磁性壳聚糖微球吸附Cr(Ⅵ)离子的最佳条件为:吸附平衡时间40 min,最佳吸附pH值6左右,磁性壳聚糖微球用量10 mg,温度升高有利于提高磁性壳聚糖微球的吸附效率,Cr(Ⅵ)离子起始质量浓度为12μg/mL,无机盐的存在引起磁性壳聚糖微球的吸附性能降低。并且考察了吸附剂的再生性能,实验结果表明磁性壳聚糖微球具有良好的重复使用性。     

球状壳聚糖负载噻二唑树脂的合成及其吸附性能

用苯甲醛保护胺基后,将2-氨基-5-巯基-1,3,4-噻二唑引入到大孔壳聚糖微球上,合成了亲水性的多孔球状吸附树脂(CTS-AMT)。 对比研究了CTS-AMT和母体微球(CTS)对Zn2+、Cu2+、Cd2+、Pb2+、Ag+和Hg2+的吸附性能。 结果表明,pH=5.0,T=298.15 K时,CTS-AMT树脂对上述金属离子的吸附在1.5 h内基本达到平衡,对金属离子Hg2+、Ag+和Pb2+的静态饱和吸附量分别为2.54、2.31和1.71 mmol/g。 在实验浓度范围内该树脂对Hg2+的吸附过程符合 Langmuir等温吸附模型。     

A novel and simple method for finding the heterogeneity of adsorbents on the basis of adsorption kinetic data

The heterogeneity of adsorbent was characterized by a novel and simple method that uses adsorption kinetic data from solution. On the basis of different simulated adsorption kinetic data for heterogeneous adsorbents with two different adsorption sites, it was found that there is a deviation from linearity in pseudo-second-order adsorption kinetic models. The patterns of obtained diagrams (t/qt vs t) shows five main classes of adsorption. On the basis of this novel and simple method it is possible to show that the surface of adsorbents is homogeneous or heterogeneous, and in the case of heterogeneous surfaces it is possible to find the differences between adsorption sites. For finding kinetic constants of adsorption on heterogeneous surfaces with two different sites, a new equation was presented and called the two-site pseudo-second-order (TS-PSO) model. Finally, some experimental kinetic data of adsorption were analyzed by the new method.     

D301R树脂对水溶液中硝基苯的吸附性质

研究了D301R弱碱性阴离子交换树脂对水中硝基苯的吸附作用,测定了不同温度下吸附的动力学曲线和吸附等温线,提出了吸附动力学模型,计算了平衡吸附量、吸附活化能和吸附焓等。 实验结果表明,吸附动力学符合表面过程控制的准二级反应模型,其速率常数k2在300 K时为3.74×10-2 g/(mg·min),并随温度的升高而升高;平衡吸附量在300 K时为5.02 mg/g,且随温度的升高而降低;吸附活化能为39.02 kJ/mol;吸附等温线符合Langmuir吸附模型,吸附焓为-22.47 kJ/mol,吸附作用力主要是氢键。     

Isolation and partial characterization of a biosurfactant mixture produced by Sphingobacterium sp. isolated from soil

The concentration decay curves for the adsorption of phenol on organobentonite were obtained in an agitated tank batch adsorber. The experimental adsorption rate data were interpreted with diffusional models as well as first-order, second-order and Langmuir kinetic models. The surface diffusion model adjusted the data quite well, revealing that the overall rate of adsorption was controlled by surface diffusion. Furthermore, the surface diffusion coefficient increased raising the mass of phenol adsorbed at equilibrium and was independent of the particle diameter in the range 0.042-0.0126 cm. It was demonstrated that the overall rate of adsorption was essentially not affected by the external mass transfer. The second-order and the Langmuir kinetic models fitted the experimental data quite well; however, the kinetic constants of both models varied without any physical meaning while increasing the particle size and the mass of phenol adsorbed at equilibrium.     

Synthesis, characterization, thermodynamic and kinetic investigations on uranium (VI) adsorption using organic-inorganic composites: Zirconyl-molybdopyrophosphate-tributyl phosphate

Zirconyl-molybdopyrophosphate-tributyl phosphate (ZMPP-TBP) was a novel organic-inorganic composite adsorbent prepared by co-precipitation method and used in the adsorption of uranium from aqueous solution in batch adsorption experiments. The as-obtained product was characterized using SEM, energy dispersive X-ray spectroscopy (EDX), XRD and BET-N₂ adsorption measurements. The study had been conducted to investigate the effects of solution pH, temperature, contact time, initial concentration and coexisting ions. A maximum removal of 99.31% was observed for an initial concentration 5 mg/L, at pH 6.0 and an adsorbent dose of 1.0 g/L. The isothermal data were fitted with both Langmuir and Freundlich equations, but the data fitted the former better than the latter. According to the evaluation using the Langmuir equation, the maximum adsorption capacity of uranium (VI) was 196.08 mg/g at 293 K and pH 6.0. The pseudo-first-order kinetic model and pseudo-second-order kinetic model were used to describe the kinetic data, and the pseudo-second-order kinetic model was better. The thermodynamic parameter ΔG was calculated, the negative ΔG values of uranium (VI) at different temperature showed that the adsorption process was spontaneous. The good reusability of ZMPP-TBP also indicated that the ZMPP-TBP was a very promising adsorbent for uranium adsorption from aqueous solution.     

Adsorption kinetics at the solid/solution interface: statistical rate theory at initial times of adsorption and close to equilibrium

The kinetics of solute adsorption at the solid/solution interface has been studied by statistical rate theory (SRT) at two limiting conditions, one at initial times of adsorption and the other close to equilibrium. A new kinetic equation has been derived for initial times of adsorption on the basis of SRT. For the first time a theoretical interpretation based on SRT has been provided for the modified pseudo-first-order (MPFO) kinetic equation which was proposed empirically by Yang and Al-Duri. It has been shown that the MPFO kinetic equation can be derived from the SRT equation when the system is close to equilibrium. On the basis of numerically generated points ( t, q) by the SRT equation, it has been shown that we can apply the new equation for initial times of adsorption in a larger time range in comparison to the previous q vs radical t linear equation. Also by numerical analysis of the generated kinetic data points, it is shown that application of the MPFO equation for modeling of whole kinetic data causes a large error for the data at initial times of adsorption. The results of numerical analysis are in perfect agreement with our theoretical derivation of the MPFO kinetic equation from the SRT equation. Finally, the results of the present theoretical study were confirmed by analysis of an experimental system.     

Kinetics and Equilibria of Synthesized Anionic Surfactant onto Berea Sandstone

We present static adsorption studies of anionic surfactants on crushed Berea sandstone. The maximum adsorption density was 0.9604 mg/g. The kinetics of adsorption process was modeled using pseudo-first-order and pseudo-second-order rate equations at 25°C and 70°C. The equilibrium adsorption process was validated using Langmuir and Freundlich adsorption models. In addition, the effects of different parameters that govern the effectiveness of these surfactants such as pH and temperature were also investigated. The kinetic study results show that the surfactant adsorption is a time dependent process. The apparent rate constant of adsorption process determined by the first-order kinetic model at 25°C and 70°C were 0.11768 and ?0.04513, respectively. The rate constant for pseudo-second-order kinetic model was 0.0086 at 25°C and 0.0101 at 70°C. The adsorption of anionic surfactant followed pseudo-second-order kinetic model. The Freundlich and Langmuir model constant were 1.6509 × 10^?4 and ?9.775 × 10^?5, respectively. The equilibrium results showed that the adsorption of anionic surfactant onto Berea sandstone was well described by Langmuir adsorption model. It was concluded that anionic surfactants performed better at higher pH and temperature.      

Kinetics and equilibrium parameters of Hg(II) adsorption on silica-dithizone

Sílica-dithizone (Sil-dtz) was synthesized and used to adsorb Hg(II) in solution at pH 6.0. Increasing the temperature accelerates the mass transfer of Hg(II) to the silica surface. The kinetic data were evaluated using the traditional pseudo-first-order Lagergren equation and an alternative Avrami kinetic equation. From the latter equation, two regions presenting distinct kinetic parameters were found, at 25 and 35 degrees C, and the use of the parameter n was also related to the determination of distinct kinetic orders. Variations of the adsorption kinetic rate in relation to the time and the temperature were also calculated and are discussed. The adsorption isotherms data were well fitted to the Freundlich model. Interestingly, good adsorption data correlation of the Langmuir model and experimental values was observed only at 45 and 50 degrees C, suggesting, for this temperature range, the formation of complexes with the proportion Hg:dithizone 1:1 on the silica surface.     

Inhibition of nitrobenzene adsorption by water cluster formation at acidic oxygen functional groups on activated carbon

The inhibition effect of nitrobenzene adsorption by water clusters formed at the acidic groups on activated carbon was examined in aqueous and n-hexane solution. The activated carbon was oxidized with nitric acid to introduce CO complexes and then outgassed in helium flow at 1273 K to remove them completely without changing the structural properties of the carbon as a reference adsorbent. The amounts of acidic functional groups were determined by applying Boehm titration. A relative humidity of 95% was used to adsorb water onto the carbon surface. Strong adsorption of water onto the oxidized carbon can be observed by thermogravimetric analysis. The adsorption kinetic rate was estimated to be controlled by diffusion from the kinetic analysis. Significant decline in both capacity and kinetic rate for nitrobenzene adsorption onto the oxidized carbon was also observed in n-hexane solution by preadsorption of water to the carbon surface, whereas it was not detected for the outgassed carbons. These results might reveal that water molecules forming clusters at the CO complexes inhibited the entrance of nitrobenzene into the interparticles of the carbon.     

HPD-100树脂吸附小檗碱的热力学及动力学研究

研究了小檗碱在HPD-100树脂上的吸附热力学和动力学行为。考察了小檗碱在HPD-100树脂上的吸附等温曲线和吸附动力学曲线,确定了吸附过程的热力学及动力学参数。结果表明,HPD-100树脂对小檗碱的等温吸附可采用Langmuir方程描述、吸附为自发进行的放热型物理吸附过程;Dunwald–Wagnen内扩散方程能较好地拟合吸附动力学数据,吸附过程以颗粒内扩散为主要控制步骤,该吸附过程的表观活化能为29.11kJ/mol。本文为HPD-100树脂分离富集小檗碱类生物碱的实际应用提供基础数据及指导。     

亲水性p-乙酰氨基酚树脂对茶碱的吸附性能

用氯球和p-乙酰氨基酚合成了亲水性p-乙酰氨基酚树脂(简记为GQ-01),研究乙酰氨基和酚羟基两类氢键作用位点修饰的GQ-01树脂对茶碱的吸附性能。实验表明:在相同茶碱起始浓度下,GQ-01树脂对茶碱的吸附量是XAD-4商业树脂对茶碱吸附量的1.9倍;GQ-01树脂对茶碱的吸附为放热、自发的过程;GQ-01树脂对茶碱的吸附动力学数据符合Lagergren一级速率方程,颗粒内扩散是吸附速率的主要控制步骤,GQ-01树脂对茶碱的吸附动力学可采用HSDM模型加以描述;GQ-01树脂对茶碱的动态吸附及脱附实验表明GQ-01树脂对水溶液中茶碱的饱和吸附量达到102.13mg/mL,树脂可以通过80%C2H5OH和1mol/L HCl的混合溶液再生。