石棉尾矿酸浸渣作为一种吸附剂去除水溶液中的Co(II)

本文采用XRD, FT-IR, SEM 和 BET等手段分别对石棉尾矿,石棉尾矿酸浸渣,以及煅烧的石棉尾矿酸浸渣进行表征。利用煅烧的石棉尾矿酸浸渣对Co(II)进行吸附研究。研究了吸附剂浓度、吸附时间、pH值和温度对Co(II)在磁性伊利石上吸附的影响,并采用Lagrange准二级动力学方程、Langmuir等温线方程、Freundlich等温线方程和D-R等温线方程对实验数据进行拟合。结果表明: pH值、离子强度和温度对Co(II)在煅烧的石棉尾矿酸浸渣上的吸附影响较大;Co(II)在煅烧的石棉尾矿酸浸渣上的吸附符合Lagrange准二级动力学方程;热力学符合Langmuir等温线方程,并且高温利于吸附。利用石棉尾矿作为吸附材料,是一个“以废治废”的工程。     

石棉尾矿酸浸渣作为一种吸附剂去除水溶液中的Co(Ⅱ)（英文）

本文采用XRD、FT-IR、SEM和BET等手段分别对石棉尾矿、石棉尾矿酸浸渣,以及煅烧的石棉尾矿酸浸渣进行表征。利用煅烧的石棉尾矿酸浸渣对Co(II)进行吸附研究。研究了吸附剂浓度、吸附时间、p H、离子强度和温度对Co(II)在磁性伊利石上吸附的影响,并采用Lagrange准二级动力学方程、Langmuir等温线方程、Freundlich等温线方程和D-R等温线方程对实验数据进行拟合,计算出热力学参数。结果表明,Co(II)在煅烧的石棉尾矿酸浸渣上的吸附是自发吸热过程,符合Lagrange准二级动力学方程;p H、离子强度和温度对Co(II)在煅烧的石棉尾矿酸浸渣上的吸附影响较大;热力学符合Langmuir等温线方程,并且高温利于吸附。     

活性炭吸附CO2与其微孔体积的关系

对五种活性炭样品进行液氮温度下的N2吸附、碘吸附测定和冰点下的CO2吸附表征。结果表明,碘吸附值测定法和基于N2吸附等温线的BET方程、D-R方程,孔结构参数都不能正确反映活性炭对CO2的吸附特性;由CO2吸附等温线得到的D A模型参数也不适合分析活性炭吸附CO2特性;CO2吸附等温线的密度泛函理论（DFT）分析结果表明,CO2在活性炭上的吸附发生在极微孔内,DFT分析的微孔孔容与吸附等温线反映的吸附性能完全一致。因此,根据CO2吸附等温线的DFT模型是准确反映活性炭吸附CO2特性的表征分析方法。     

分子连接性指数与溶液吸附自由能的相关性

测定了硅胶自四氯化碳中吸附脂肪醇及活性炭自水中吸附芳香化合物的吸附等温线, 等温线均可用Langmuir方程描述。利用Langmuir参数计算了各体系的吸附标准自由能变化。计算了各种吸附质的分子连接性指数。各种分子的分子连接性指数与吸附标准自由能变化间有相关性, 并给出了相关方程, 同时作了初步的讨论。     

沥青基球形活性炭对葡萄糖分子的吸附行为研究

考察了沥青基球形活性炭(PSAC)对葡萄糖分子的吸附行为,以探讨其治疗糖尿病的可能性.在不同吸附时间、不同活性炭用量及不同浓度等条件下,测定沥青基球形活性炭对葡萄糖分子的吸附量,根据Langmuir和Freundlich等温线方程对吸附等温线数据进行拟合,检验实验数据与方程的吻合度,确定方程参数.同时,研究了葡萄糖和α-淀粉酶在沥青基球形活性炭上的竞争吸附行为.结果表明,所选用沥青基球形活性炭对葡萄糖分子的吸附在5h内达到吸附平衡;葡萄糖的初始浓度为3g/时,平衡吸附量为71mg/g;平衡吸附量受葡萄糖分子空间构象的影响,且随葡萄糖浓度的升高而增加,吸附等温线数据与Langmuir方程吻合,说明该吸附为单分子层吸附.在葡萄糖分子和α-淀粉酶的共存环境下,沥青基球形活性炭对葡萄糖有较好的吸附选择性.     

硅沸石完美骨架上的吸附Ⅲ.氯氟烃在MFI和FAU上的吸附热

测定不同温度下三种氯氟烃F-11(CFCl3),F-12(CF2Cl2)和F-22(CHF2Cl)在疏水高硅MFI和FAU沸石上的吸附等温线,以研究其吸附热效应。根据Clapeyron-Clausius方程,由吸附等温线,计算不同覆盖度C的等量吸附热Qst(C)和平均吸附热Qst^*(△Ha)。上述吸附质在两种沸石上吸附热的大小顺序均为：△Ha(MFI)＞△Ha(FAU)。在同种沸石上,吸附热的大小顺序为：△Ha(F-11)＞△Ha(F-12)＞△Ha(F-22).298K时的吸附等温线和△Ha的变化趋势显示,对能允许氯氟烃分子自由进出其孔道的FAU沸石,吸附质分子越大,低分压吸附量(V)越大,吸附热(△Ha)也越大。而孔道对吸附质分子有空间限制作用的MFI沸石,其吸附热、分子尺寸与饱和吸附量(Vm)间关系比较复杂。选择去除氯氟烃的沸石吸附剂应综合考虑△Ha与饱和吸附容量Vm。     

乙酰苯胺修饰的吸附树脂对苯酚和对氯苯酚的吸附研究

通过Friedel-Crafts后交联及化学修饰反应,合成了乙酰苯胺基修饰的超高交联吸附树脂ZH-05,通过红外光谱(IR)和比表面及孔径分析(BET)对其结构进行表征.以Amberlite XAD-4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ZH-05树脂对水溶液中苯酚和对氯苯酚的吸附性能和机理.结果表明,与XAD-4树脂相比,ZH-05树脂对苯酚和对氯苯酚均具有更佳的吸附性能.Langmuir和Freundlich方程均能较好拟合ZH-05树脂对苯酚和对氯苯酚的吸附等温线.ZH-05树脂对苯酚和对氯苯酚的吸附以焓推动的自发物理吸附过程为主,吸附过程放热;吸附符合准一级动力学吸附方程,颗粒内扩散是吸附过程的主要控制步骤.     

硅沸石完美骨架上的吸附Ⅲ.氯氟烃在MFI和FAU上的吸附热

测定不同温度下三种氯氟烃F-11(CFCl3),F-12(CF2Cl2)和F-22(CHF2Cl)在疏水高硅MFI和FAU沸石上的吸附等温线,以研究其吸附热效应。根据Clapeyron-Clausius方程,由吸附等温线,计算不同覆盖度C的等量吸附热Qst(C)和平均吸附热Qst^*(△Ha)。上述吸附质在两种沸石上吸附热的大小顺序均为：△Ha(MFI)＞△Ha(FAU)。在同种沸石上,吸附热的大小顺序为：△Ha(F-11)＞△Ha(F-12)＞△Ha(F-22).298K时的吸附等温线和△Ha的变化趋势显示,对能允许氯氟烃分子自由进出其孔道的FAU沸石,吸附质分子越大,低分压吸附量(V)越大,吸附热(△Ha)也越大。而孔道对吸附质分子有空间限制作用的MFI沸石,其吸附热、分子尺寸与饱和吸附量(Vm)间关系比较复杂。选择去除氯氟烃的沸石吸附剂应综合考虑△Ha与饱和吸附容量Vm。     

弱酸强碱两性树脂吸附盐的平衡研究

本文采用静态吸附法研究了各种盐溶液在弱酸强碱两性树脂上的吸附平衡规律，证明了其满足 Ｌａｎｇｍｕｉｒ的吸附等温线方程，并从该方程中的 ｂ值推断出各种离子对两性树脂的选择性顺序以及破坏内盐键的能力大小。     

疏水界面上标准蛋白质吸附等温线的研究

测定了几种具有代表性的标准蛋白质在疏水色谱填料上的吸附等温线.除溶菌酶和牛血清白蛋白的吸附近似呈线性外,细胞色素-c、肌红蛋白、胰岛素、α-淀粉酶和卵清蛋白均呈凸型吸附.用Langmuir、计量置换吸附模型(SDM-A)、BET和Jovanovic吸附模型对这些蛋白的吸附等温线拟合后发现,SDM-A关系式能够良好描述这7种蛋白的吸附,Langmuir关系仅能较好地描述后5种蛋白质的吸附.而Jovanovic和BET关系式对上述两类蛋白质吸附的描述欠妥.实验发现对于不同盐浓度条件下卵清蛋白的吸附,用SDM-A和Langmuir公式拟合所得的参数与盐浓度之间呈现出一定的规律性.     

New theoretical expressions for the five adsorption type isotherms classified by BET based on statistical physics treatment

New theoretical expressions to model the five adsorption isotherm types have been established. Using the grand canonical ensemble in statistical physics, we give an analytical expression to each of five physical adsorption isotherm types classified by Brunauer, Emett, and Teller, often called BET isotherms. The establishment of these expressions is based on statistical physics and theoretical considerations. This method allowed estimation of all the mathematical parameters in the models. The physicochemical parameters intervening in the adsorption process that the models present could be deduced directly from the experimental adsorption isotherms by numerical simulation. We determine the adequate model for each type of isotherm, which fixes by direct numerical simulation the monolayer, multilayer, or condensation character. New equations are discussed and results obtained are verified for experimental data from the literature. The new theoretical expressions that we have proposed, based on statistical physics treatment, are rather powerful to better understand and interpret the various five physical adsorption type isotherms at a microscopic level.     

Guggenheim-Anderson-de Boer isotherm equation as applied to determining texture parameters of sorbents with compounds grafted to their surfaces

By processing the data on benzene adsorption on the surface of silicas containing compounds grafted to their surface, it is shown that the potential of the BET adsorption isotherm equation is greatly limited for determining the texture parameters of these sorbents. The three-parameter Guggenheim-Anderson-de Boer adsorption isotherm equation is recommended to be used rather than the two-parameter BET adsorption isotherm equation for more reliable assessment of structural characteristics of these sorbents.     

The effect of heat treatment on the adsorption properties of solids. II. The effect of heat treatment on the character of the adsorption isotherm

In this study the nitrogen adsorption isotherms of heat-treated zinc oxalate, sintered magnesium oxide, and some oxidised pitch resins are considered. It is shown that characterisation of the adsorption isotherm can be via the monolayer capacity, the BET constant C, or plots of the degree of coverage of the surface at various relative vapour pressures. These parameters are critically assessed and shown to be dependent upon the closeness to the manner in which the complete adsorption isotherm is described by the BET equation. In considering the complete adsorption isotherm it is considered best to characterise the adsorption data by quoting the statistical monolayer capacity and the value of C at this point on the adsorption isotherm. The adsorption isotherms are then best compared by plotting as the number of statistical layers against the relative pressure. The further characterisation by plotting the apparent variation in C or the degree of coverage of the surface against the relative pressure has a usefulness if the limitations of the method are noted.     

What is the correct form of BET isotherm for modeling liquid phase adsorption?

In this work subtleties of application of BET isotherm for liquid phase adsorption is presented. It has been shown that direct use of the classical BET equation (which was developed for gas phase adsorption) to liquid phase adsorption leads to ambiguous and erroneous results. Some cases of misuse of BET equation for liquid phase adsorption have been revisited. By close examination of the development of the classical equation, the causes of misunderstandings were elucidated and the suitable form of the BET equation for liquid phase adsorption was developed. As case studies, the classical form of the BET equation along with the correct form of the equation for liquid phase have been applied for modeling liquid phase adsorption of methyl tert-butyl ether (MTBE) on perfluorooctyl alumina, phenol on activated carbon and pentachlorophenol on carbonized bark. It has been shown that direct application of the classical BET isotherm to liquid phase adsorption results in poor and erroneous estimation of the equation parameters. For example, in aqueous phase adsorption of MTBE on perfluorooctyl alumina, the monolayer adsorption capacity of the adsorbent was calculated as 9.7 mg/g instead of 3.3 mg/g or the saturation concentration of MTBE in water was calculated as 1212 mg/L instead of 42000 mg/L.     

Theoretical and Experimental Study on the Adsorption and Desorption of Methane by Granular Activated Carbon at 25 ℃

A theoretical and experimental study was conducted to accurately determine the amount of adsorption and desorption of methane by various Granular Activated Carbon(GAC)under different physical conditions.To carry out the experiments,the volumetric method was used up to 500 psia at constant temperature of 25℃.In these experiments,adsorption as well as desorption capacities of four different GAC in the adsorption of methane,the major constituent of natural gas,at various equilibrium pressures and a constant temperature were studied.Also,various adsorption isotherm models were used to model the experimental data collected from the experiments.The accuracy of the results obtained from the adsorption isotherm models was compared and the values for the regressed parameters were reported.The results shows that the physical characteristics of activated carbons such as BET surface area,micropore volume,packing density,and pore size distribution play an important role in the amount of methane to be adsorbed and desorbed.     

基于光波导分光光谱技术研究蛋白质与亚甲基蓝的竞争吸附行为

通过利用时间分辨光波导分光光谱技术原位测量从蛋白质-亚甲基蓝(MB)混合水溶液吸附到亲水玻璃光波导表面的MB可见光吸收谱,观测到在溶液pH值低于蛋白质等电点时MB与牛血清蛋白(BSA)以及MB与血红蛋白(Hb)存在竞争吸附行为,进一步测得这种竞争吸附行为对蛋白质浓度十分敏感,可以用于简单测定溶液中的蛋白质含量.基于Langmuir等温吸附理论推导出了两种分子竞争吸附的动力学方程,并利用该动力学方程对实验测得的吸光度随时间变化曲线进行了最佳拟合,揭示了玻璃表面吸附的MB分子个数在达到最大值后随时间呈指数衰减,同时得出拟合参数与蛋白质浓度呈准线性关系.     

Separation of the First Adsorbed Layer from Others and Calculation of the BET Compatible Surface Area from Type II Isotherms

In the previous paper it has been proven that a BET compatible specific surface area, asc(N2, 77), can be calculated from any Type I isotherm measured below the critical temperature. In this paper it is proven that the same calculation can be performed from any Type II isotherms if the isotherm has a pure monolayer domain. In order to distinguish the mono- and multilayer adsorption the relative free energy of the surface as a function of the adsorbed amount, pir(ns), and the functions psi(pr) and psi(ns) are applied, both defined by the differential expression (ns/pr)(dpr/dns). When the multilayer adsorption becomes the dominant process then the function pir(ns) has a point of inflexion and functions psi(pr) and psi(ns) have maximum values. It has been demonstrated that in most of the Type II isotherms the mono- and multilayer domains can be separated, so the monolayer component isotherm can be calculated by the T (Tóth) equation. Therefore, it is possible to calculate the BET compatible specific surface area discussed in detail in the previous paper. It has also been proven that there are Type II isotherms which describe only multilayer adsorption; i.e., the functions psi(pr) and psi(ns) do not have maximum values. In these cases the Harkins-Jura equation should be applied. Copyright 1999 Academic Press.