腐殖酸对汞的吸附特性与动力学研究

采用静态吸附法研究了汞在腐殖酸上的吸附特性和动力学特征.结果表明,20℃以下,平衡吸附量随温度的升高而增加,20℃以上,吸附反应受温度的影响却很小.溶液的pH在5～9范围内,具有最高的吸附效率,有利于腐殖酸吸附更大量的汞.吸附过程符合伪二级吸附速率方程,吸附速率常数k2随初始浓度的增加反而减小,这与快吸附反应比例F以及到达F的时间有关.腐殖酸对汞的吸附活化能为20.37kJ/mol,说明吸附反应属于化学吸附过程.     

负载苯基硫脲酚醛型螯合树脂对Ag+的吸附与实验室应用

在四丁基溴化铵(TBAB)相转移催化条件下,线形环氧酚醛树脂(F44)与苯基硫脲(PTU)发生开环加成,合成了负载苯基硫脲的酚醛型螯合树脂(F44-PTU).研究了该树脂对Cu2 、Ni2 、Pb2 、Hg2 、Au3 的吸附容量及温度、离子浓度、pH值对Ag 吸附性能的影响.结果表明,该树脂对Ag 具有较好的吸附性能,吸附符合Freundlich等温式.吸附树脂在5%硫脲～1mol/L HNO3时可洗脱再生,再生后树脂的吸附能力下降,可能在Ag 的吸附过程中伴随有氧化还原作用.将合成树脂处理实验室含银废液,银的回收率可达93.8%.     

Mg/Al水滑石的焙烧产物吸附酸性红88的动力学和热力学机理研究

文章研究了Mg/Al水滑石焙烧产物(LDO)对酸性红88 (AR88)的吸附性能及其机理. 考察了温度对其吸附性能的影响, 探讨了吸附过程的动力学和热力学规律. 热力学研究表明: LDO对AR88的吸附过程稍符合Langmuir等温吸附. 从Langmuir等温式计算的 , 为负值, 表明吸附过程为放热、熵减小的过程, 这是因为LDO在吸附酸性染料后恢复了层状结构|不同温度下 均为负值, 表明吸附过程是自发进行的. 动力学研究表明: 吸附动力学符合准二级动力学模型, 动力学计算吸附过程的活化能E_a＝54.53 kJ•mol^－1. 利用Materials Studio 4.3软件中的CASTEP程序模块和Focite模块模拟了AR88染料分子在Mg/Al水滑石(LDHs)的尺寸大小和排列方式, 推测吸附机理是以表面吸附占主要优势并伴有少部分插层.     

氨基修饰聚苯乙烯树脂对酚酸物质的吸附性能

通过对XAD 4聚苯乙烯树脂的氨基修饰制备了一种亲水性的NDA 10 0树脂 .研究了NDA 10 0树脂对苯酚和对羟基苯甲酸等酚酸类物质的吸附动力学和热力学行为 .结果表明 ,NDA 10 0树脂对苯酚和对羟基苯甲酸具有良好的吸附性能 ,在研究的浓度范围内 ,吸附平衡数据符合Langmuir和Freundlich等温吸附方程 ,吸附为放热的物理吸附过程 .吸附动力学符合Lagergren准二级速率方程 ,颗粒内扩散为吸附速率的主要控制步骤 .     

树脂吸附法分离纯化桑叶总黄酮(I)H103树脂对桑叶水提液中总黄酮的吸附性能

采用大孔吸附树脂法从桑叶水提液中分离黄酮类化合物.通过比较10种大孔吸附树脂对桑叶水提液中总黄酮的吸附特性及机理,发现H103树脂对桑叶总黄酮吸附量大.洗脱容易、吸附速度快,是一种良好的桑叶总黄酮吸附刑.实验表明,H103树脂吸附桑叶黄酮的适宜上样浓度为6.05mg/mL,吸附动力学符合Bangham模型,吸附过程符合内扩散模型.     

大孔树脂对茄尼醇吸附行为的研究

从6种大孔树脂中筛选出用于茄尼醇分离较好的树脂NKA,并进一步研究了其对茄尼醇吸附行为,结果表明,吸附等温线服从Langmuir方程和Freundlich方程,且吸附过程表现为优惠吸附.在温度为283～313K,吸附量为15～35mg/g的条件下,吸附焓变为-16.20～16.57kJ/mol,自由能变为.3.142～3.459kJ/mol,吸附熵变为-47.43～41.17J/mol.K.NKA树脂对茄尼醇吸附速率较快,吸附过程符合一级吸附动力学方程,吸附过程主要受液膜扩散控制.     

离子交换树脂分离发酵液中乳链菌肽工艺

用阳离子交换树脂D113吸附发酵液中乳链菌肽,单位体积D113的吸附量为120000IU/mL,加入90mL 5%KCl溶液,8h时解吸率达到最大值,最终解吸率为48%.在25℃,40℃和50℃下D113的吸附等温线符合Langmuir吸附等温方程.通过对控制机理的判断,25℃时F与t呈线性关系,为液膜扩散控制(FDC);40℃、50℃时[1-3(F)<2/3 2(1-F)]～t曲线呈良好的线性关系,为颗粒扩散控制(PDC).     

丙烯酸Fe3+型树脂在非水介质中对鞣酸的配位吸附及洗脱性能

将Fe3 载于丙烯酸树脂上,制备了在非水介质中对鞣酸具有良好吸附性能的配位吸附树脂.在甲醇中,树脂对鞣酸的吸附符合Langmuir单分子层吸附模型,静态饱和吸附量为34mg/g,吸附为粒扩散控制过程.动态吸附中,树脂对鞣酸的泄漏吸附量为25mg/g,饱和吸附量32mg/g.采用5%的甲胺乙醇溶液作洗脱剂,洗脱率95%.树脂在吸附及洗脱过程中未见Fe3 脱落.     

稻壳灰吸附剂对罗丹明B的吸附性能研究

以发电废弃物稻壳灰为原料,以NaOH为活化剂制备了稻壳灰吸附剂,并将其用于去除水中罗丹明B(Rhodamine B,Rh B)染料。系统考察了溶液pH值、初始浓度、吸附时间、吸附温度以及溶液离子强度对其吸附性能的影响。结果表明:pH=3时,稻壳灰吸附剂对水中Rh B的吸附效果最佳,饱和吸附容量q_m为322. 6mg·g~(-1);吸附热力学研究表明,吸附过程符合Langmuir等温吸附模型。吸附过程焓变ΔH为7. 67 kJ·mol~(-1),ΔS为24. 92 J·mol~(-1)·K~(-1),ΔG0,表明稻壳灰吸附剂对Rh B的吸附过程是自发的吸热熵增过程;吸附过程可在20 min内达到平衡,符合准二级动力学模型;吸附过程的活化能E_a为24. 1 kJ·mol~(-1)。吸附容量随着溶液离子强度的增大而减小,说明其吸附是以静电作用为主的吸附过程。10次循环使用后稻壳灰吸附剂对Rh B的吸附效率仍能保持91%以上,表明该材料可以多次循环使用,是潜在的高效吸附材料。     

纳米TiO2去除氟离子的性能

研究了锐钛型纳米TiO2吸附剂对氟离子的吸附行为,考察了吸附平衡时间、温度、溶液的pH值等因素对吸附过程的影响.结果表明,纳米TiO2对氟离子的吸附在2.0 min基本达到平衡,在pH值2.0～10.0范围内,吸附率大于97％;吸附的氟离子可用0.1 mol/L NaOH溶液洗脱,3.0 min基本达到解析平衡,解析率能达到96％;该吸附过程符合准二级反应动力学模型,其反应的表观活化能(Ea)为6.85 kJ/mol;颗粒内扩散过程为吸附控制步骤,但不是唯一的控制步骤,同时还受液膜扩散的影响;吸附过程符合Langmuir、D-R等温模型,常温下纳米TiO2对氟离子的平均吸附能为4.26 kJ/mol.吸附反应的△G0＜0,焓变△H0＞0,说明该吸附过程是自发的吸热反应.共存阴离子HCO3-和pO43-对氟离子的吸附有影响.纳米TiO2在动态和静态吸附实验中的除氟效果相近.     

介孔碳CMK-3对苯酚的吸附动力学和热力学研究

研究了介孔碳CMK-3对苯酚的吸附性能, 与传统商用活性碳(CAC)进行了比较, 结果表明, CMK-3比CAC的吸附量大、吸附速率快、达到平衡时间短, 是一种较好的吸附剂. 同时探讨了介孔碳CMK-3对苯酚的吸附热力学和动力学特征. CMK-3对苯酚的吸附行为可用Langmuir和Freundlich等温式进行描述, 相关性都较好, 但更符合Freundlich经验公式. 分别采用模拟一阶反应和二阶反应模型考察了吸附动力学, 并计算了这些动力学模型的速率常数. 模拟二级反应模型和实验数据之间有较好的相关性. 分别计算了热力学参数ΔG0, ΔS0和ΔH0, 结果表明, CMK-3对苯酚的吸附过程是吸热和自发的.     

Kinetic and isothermal studies of lead ion adsorption onto palygorskite clay

The use of a natural palygorskite clay for the removal of Pb(II) from aqueous solutions for different contact times, pHs of suspension, and amounts and particle sizes of palygorskite clay were investigated. The variations of the pH value of Pb(II) solutions on natural palygorskite in the adsorption process were determined. Batch adsorption kinetic experiments revealed that the adsorption of Pb(II) onto palygorskite clay involved fast and slow processes. It was found that the adsorption mechanisms in the lead/palygorskite system follow pseudo-second-order kinetics with a significant contribution from film diffusion. SEM observations demonstrated that an important interaction at the lead-granule interface occurred during the adsorption process. The adsorption isotherms were described by means of the Langmuir and Freundlich isotherms and the Langmuir model represents the adsorption process better than the Freundlich model. The maximum adsorption capacity of Pb(II) onto natural palygorskite was 104.28 mg g(-1).     

活性白土对油脂溶液中β-胡萝卜素的吸附热力学及动力学研究

探讨了活性白土(AAB)对油脂溶液中β-胡萝卜素的吸附热力学及动力学特征,AAB对β-胡萝卜素的吸附行为可用Langmuir和Freundlich等温式进行描述,相关性均较好,在高温条件下(75～95℃),AAB对β-胡萝卜素的吸附更符合Freundlich模型的吸附行为.分别采用拟一级反应乖拟二级反应模型描述了吸附动力学数据,表明AAB吸附β-胡萝卜素适合于拟二级吸附动力学行为,且高温有利于提高吸附量和吸附速率.AAB对β-胡萝卜素的吸附表现活化能E_a为38.673kJ/mol,表明整个吸附过程涉及到化学吸附作用;通过对吸附热力学参数△H、△S及△G的分析,表明吸附过程是自发进行且伴随着吸热及熵值的增加,吸附趋势随着温度的升高而有所增大.     

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。     

Estimation of Adsorption Capacity for Dissociating and Non Dissociating Aromatic Compounds on Activated Carbon with Different Models

The process of adsorption of two dissociating and two non-dissociating aromatic compounds from dilute aqueous solutions on an untreated commercially available activated carbon (B.D.H.) was investigated systematically. All adsorption experiments were carried out in pH controlled aqueous solutions. The experimental isotherms were fitted into four different models (Langmuir homogenous Models, Langmuir binary Model, Langmuir-Freundlich single model and Langmuir-Freundlich double model). Variation of the model parameters with the solution pH was studied and used to gain further insight into the adsorption process. The relationship between the model parameters and the solution pH and pK_a was used to predict the adsorption capacity in molecular and ionic form of solutes in other solution.A relationship was sought to predict the effect of pH on the adsorption systems and for estimating the maximum adsorption capacity of carbon at any pH where the solute is ionized reasonably well.N₂ and CO₂ adsorption were used to characterize the carbon. X-ray Photoelectron Spectroscopy (XPS) measurement was used for surface elemental analysis of the activated carbon.     

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.      

Facile synthesis of bioglass nanospheres for the adsorption of cationic and anionic dyes from aqueous solution

A novel adsorbent, bioglass nanospheres (BGN), has been prepared by a facile process. The BGN were spheres with an amorphous structure and a relatively high specific surface area, as indicated by SEM, transmission electron microscopy, BET, FTIR, and XRD. This paper was aimed at evaluating the adsorption behavior of this new material for the adsorptive removal of cationic (methylene blue, neutral red) and anionic (congo red) dyes from aqueous solution. The effects of the initial dye concentration, contact time, solution pH, and temperature were investigated. The adsorption kinetics showed that the adsorption behavior followed the pseudo-second-order kinetic model. The adsorption isotherm fit well to the Langmuir model. Thermodynamic analyses showed that the adsorption was physisorption, and it was also a spontaneous and endothermic process. The BGN exhibited a good reusability after five consecutive cycles for cationic dyes. In addition, the possible adsorption mechanism was also proposed based on the above experimental results.     

Adsorption behavior of Fe(II) and Fe(III) ions on thiourea cross-linked chitosan with Fe(III) as template

A new type of thiourea cross-linked chitosan with Fe(III) as template (TCCTS template) was synthesized. The adsorption of Fe(II) and Fe(III) on this TCCTS template was studied. The factors affecting adsorption such as pH and contact time were considered. The results showed that the optimum pH value for adsorption was pH = 5.0 and the adsorption equilibrium time was about 60 min. The adsorption isotherms and kinetics were investigated, and the equilibrium data agreed very well with the Langmuir model and the pseudo second-order model could describe adsorption process better than the pseudo first-order model. Results also showed that TCCTS template was a favourable adsorbent for Fe(II) and Fe(III) in aqueous solution.     

ZnO/C纳米球的亚甲基蓝单吸附特性:平衡、动力学及机理

采用电弧放电法制备了ZnO/C纳米球,利用FESEM、XRD和N₂吸附/脱附测试进行了表征。在避光条件下研究了复合材料对亚甲基蓝的吸附性能。研究结果表明,随着亚甲基蓝的浓度及接触时间的增长吸附量明显上升,在吸附时间为150 min时达到吸附平衡。采用Langmuir、Freundlich及Temkin等温吸附模式对吸附平衡进行了研究。结果表明,吸附等温线符合Langmuir等温吸附模式,单层吸附饱和容量可达188.68 mg·g^-1。利用动力学模型、内扩散模型和外扩散速率控制模型拟合实验数据,拟合数据表明其动力学符合伪二级动力学模型;内扩散机理不是吸附速率的唯一限制机理,亚甲基蓝的总吸附速率受膜扩散控制。