PAN基活性炭纤维的氮吸附

通过对不同活化方法制备相同原料聚丙烯腈基活性炭纤维进行氮吸附研究,结果表明由不同活化方法所制备的活性炭纤维的孔结构存在较大差异,并对随着活化程度的改变其孔结构的发展进行了研究.结果表明通过简单的改变活化方法即可以制得不同孔隙占主导地位的的炭质吸附剂,由此也预示着对于不同的活化方法其活化机理的差别.     

PAN基活性炭纤维的氮吸附研究

用相同原料不同活化方法制备聚丙烯腈基活性炭纤维,并对其进行了氮吸附研究.结 果表明,由不同活化方法所制备的活性炭纤维的孔结构存在较大差异,并对随着活化程度的 改变其孔结构的发展进行了研究.结果表明,通过简单的改变活化方法即可以制得不同孔隙占 主导地位的炭质吸附剂;也揭示出,不同的活化方法其活化机理有所差别.     

活性炭纤维的微孔结构水吸附

测定了两种活性炭纤维（ACF）的氮气、水吸附等温线和XPS,研究了ACF的微孔结构和表面性质,用αs图分析氮吸附等温线获得了ACF的比表面积、微孔容量和微孔径。XPS表明在ACF表面存在多种不同结合状态的氧。水在ACF上的吸附等温线呈V型,具有很大的脱附滞后环。水通过与ACF表面的氧形成氢键发生吸附。ACF表面的初始吸附点多,则在低、中压时的水吸附量就大。     

活性炭纤维的分形孔径分布及对低浓度苯蒸气的吸附

在Jaroniec提出的J(x)分形孔径分布函数基础上提出了K(x)分形孔径分布函数, 并利用这2个函数对3种不同比表面积的活性炭纤维进行了表征; 通过非极性苯蒸气在活性炭纤维上的等温线与分形孔径分布的比较研究, 揭示了活性炭纤维的分形孔径分布与非极性苯在活性炭纤维上的等温线的关系.     

活性炭纤维对挥发性有机物的吸附及其等温线的拟合

空气中挥发性有机化合物（VOC）严重危害人的身体健康,因而研究VOC的去除具有重要意义。本文研究了不同比表面积粘胶基活性炭纤维（ACF）对低浓度VOC,丁酮和苯的吸附,并用Freundilch方程和DR方程对吸附等温线进行了拟合。结果表明：当丁酮的浓度高于100ppm时,比表面积高的ACF吸附容量高;当浓度低于100ppm时,情形正好相反。在实验浓度范围,较高比表面积的活性炭纤维对苯的吸附表现出了较高的吸附容量。Freundlich方程和DR方程能很好地拟合吸附等温线。     

炭素纤维与活性炭纤维

本文综合介绍了炭素纤维与活性炭纤维的制备、物化性能及其应用。     

应用超临界温度氢吸附数据表征活性炭结构

为准确研究氢在活性炭上的吸附平衡,本文对比分析了由氮和氢在活性炭上吸附数据确定的活性炭的孔径分布(PSD)。首先,应用容积法,在0～12.5MPa压力范围、3个温度(113.15K、193.15K、273.15K)下测定氢在K05活性炭上的吸附平衡数据,并由引入系统内氢的质量衡算确定吸附池内氢的总量。其次,以77K氮吸附数据确定的PSD为初值、以吸附池内氢的总量为基准,通过优化非局域密度泛函理论(NDFT)计算值确定活性炭的PSD,进而比较表征介质、温度及平衡压力对PSD的影响。研究表明,应用氢吸附数据表征孔宽小于0.8nm的超细微孔的微分容积较大;平衡压力较高时,由不同温度氢吸附数据确定的超细微孔的PSD相近;孔宽大于1.2nm时,不同温度氢吸附数据确定的PSD间有明显偏差。须应用超临界温度高压氢或氢在亚临界温度区域的吸附数据,同时结合77K氮吸附等温线来表征吸附剂在超细微孔和微孔范围的PSD。     

活性炭纤维孔结构控制和表面改性

活性炭纤维（ACF-ActivatedCarbonFiber）是本世纪七十年代发展起来的纤维状吸附剂[1]。其吸附性能与表面积、细孔直径、细孔分布等物理结构密切相关，同时与其表面化学结构密不可分，本文综述介绍ACF的孔结构控制方法和表面化学改性与吸附性能的关系。     

活性炭纤维的性能及其在环境卫生中的应用

简要介绍了新型功能材料——活性炭纤维的种类、制备和改性方法，通过与传统的颗粒状活性炭的比较，阐明了活性炭纤维的独特性能；综述了活性炭纤维在环境卫生方面的应用。     

乙烯渣油沥青基活性炭纤维和粘胶基活性炭纤维的表面性质与脱硫活性

研究了在O2和H2O存在下,乙烯渣油沥青基活性炭纤维(ETPACF)和粘胶基活性炭纤维(CelluloseACF)的脱硫活性.结果表明,在比表面积相近的情况下,ETPACF的脱硫活性明显低于CelluloseACF,这可归因于后者具有较强的吸附和催化氧化SO2能力及较大的吸水量,尤其是具有较强的催化氧化SO2的能力,这些能力又与其表面含有含氮官能团以及某些含氧官能团有关,因此ACF的表面官能团对其脱硫活性影响很大.     

通过密度函数理论表征炭质吸附剂的孔径分布

通过密度函数理论（DFT-DensityFunctionalTheory）对炭质吸附剂的孔径分布进行了表征。该法以多孔固体上N2吸附分子模型为依据，用一种方法对多孔固体的孔径分布从微孔到大孔范围进行确定。本文用该法对自制的聚丙烯腈活性炭纤维、国产煤质活性炭及日本产活性炭微球等六种炭质吸附剂的孔径分布进行了表征。     

Porous Structure of Activated Carbon Fibers

The dependence of the microporous structure of activated carbon fibers on the carbonization temperature of hydrate-cellulose fibers was studied by BET, TVFMP, and Horvath and Kawazoe techniques and methods of the nonlocal density functional theory. The surface energy distribution function was obtained, together with the micropore size distribution curves. It was shown that the effective micropore sizes calculated by the TVFMP method are close to the maximum of the distribution function found in terms of the theory of the density functional.     

Nitrogen Adsorption Studies of PAN-Based Activated Carbon Fibers Prepared by Different Activation Methods

Polyacrylonitrile (PAN)-based activated carbon fibers (ACFs) prepared by various activation methods were characterized using low-temperature nitrogen adsorption over a wide relative pressure from 10⁻⁶ to 1. Nitrogen adsorption is a standard tool for determination of porous structure parameters. In the present work, we carried out extensive adsorption studies of a series of PAN-ACFs activated by different methods. It was shown that the high-resolution α_S plot provided valuable information about structural properties of samples under study. The pore size distributions of samples under study were calculated by employing the regularization method according to density functional theory. By these analyses, the pore development and the dominant pores of samples prepared by different methods can be clearly observed. Moreover, the adsorption measurement could provide profound insight into the structural heterogeneity of the ACFs.     

Preparation and Characterization of Activated Carbon Fiber from Paper

Activated carbon fibers (ACFS) with surface area of 1388 m²/g prepared from paper by chemical activation with KOH has been utilized as the adsorbent for the removal of methy-lene blue from aqueous solution. The experimental data were analyzed by Langmuir and Freundlich models of adsorption. The effects of pH value on the adsorption capacity of ACFS were also investigated. The rates of adsorption were found to conform to the kinetic model of Pseudo-second-order equation with high values of the correlation coefficients (R>0.998). The Langmuir isotherm was found to fit the experimental data better than the Feundlich isotherm over the whole concentration range. Maximum adsorption capacity of 520 mg/g at equilibrium was achieved. It was found that pH played a major role in the adsorption process, higher pH value favored the adsorption of MB.     

污泥活性炭的结构特征及表面分形分析

以城市污水厂污泥为主要原料添加适量添加剂, 采用ZnCl₂化学活化法制备的污泥活性炭, 借助XRD, BET法, FT-IR, SEM等现代分析测试方法结合液相吸附法, 表征结构特征和分析表面分形维数. 结果表明: 在适宜的活化温度、活化时间、ZnCl₂浓度、原料粒度等工艺条件下, 加入少量添加剂制备的污泥活性炭, 最可几孔径分布在4.16 nm左右,平均孔容0.4484～0.5122 mL•g^－1, 比表面积为634.8～748 m²•g^－1, IR峰中出现C—OH, C—H, N＝O, C＝C功能组, 孔结构是具有平行壁的狭缝状介孔结构. 由液相吸附法得到的污泥活性炭分维近似为2, 属于低分维二维表面.     

Comparative Adsorption of Crystal Violet and Congo Red onto ZnCl2 Activated Carbon

In this study, the adsorption characteristics of crystal violet (CV) and Congo red (CR) dyes from the aqueous solution onto prepared activated carbon were examined. The activated carbon was prepared from wood apple shell by chemical activation with ZnCl₂. The parameters studied were the effect of contact time, initial dyes concentration, and pH of solution. The experimental equilibrium data were analyzed and fitted to Langmuir, Freundlich, and Temkin isotherms. The maximum monolayer adsorption capacities of CV and CR dyes were found to be 142.85 and 83.33 mg per gram of prepared activated carbon at 298 K. The kinetic data obtained at different concentrations were analyzed using pseudo-first-order, pseudo-second-order, and intra-particle diffusion models. Batch adsorption kinetic studies showed that the adsorption of dyes followed pseudo-second-order kinetics and at four different concentrations of both dyes, indicating that chemisorption is the rate-limiting step. Thermodynamic studies reveal that the removal of dyes from aqueous solution onto activated carbon was a spontaneous, feasible, and endothermic process at a temperature greater than standard equilibrium temperature.     

镍表面单原子台阶对甲烷解离过程影响的DFT研究

使用基于密度泛函理论（DFT）的DMol^3量子力学计算程序模块，采用Ni（211）周期性模型表达镍表面上的单原子台阶结构，计算出CHx（x=0～4）在Ni（211）模型不同活性位上的吸附能和空间构型，并使用LST／QST方法找到了台阶结构上CHx（x=1～4）的解离路径、过渡态和相应的能量数据．计算结果表明，金属表面台阶结构较平台结构更有利于CHx物种的吸附．台阶结构上存在能够降低CHx解离活化能的活性位．处于台阶结构上的特定位置时，CH4解离全过程的关键步骤-CH4和CH解离的活化能会大幅降低。     

水分子在MoO3原子簇模型表面吸附的密度泛函研究

利用密度泛函理论(DFT)的B3LYP方法,在LANL2DZ基组上,计算了水分子吸附前后MoO3原子簇模型物的优化几何构型和电子结构,并进行了二级Mφller-Plesset微扰(MP2)相关能计算.结果表明,当水分子吸附于模型分子后,由于占据了MO5+空位,从原来留有空位的MoO5H4模型转变为MoO5H4·H2O模型的正八面体构型,水分子的氧通过占据在π键轨道中的电子向中心原子Mo的d轨道配位而被吸附,且水分子在模型物质表面呈吸附状态后,体系最稳定,能量最小,吸附过程不必翻越能垒,该过程放热91.39kJ/mol(MP2相关能校正),研究结果对催化剂的使用、失活和再生有较好的指导意义.     

杂多酸在活性炭表面含氧基团上的化学键合作用

杂多酸作为一种新型多功能催化剂，近年来匕成为催化领域的研究热点之一［’l杂多酸在均相对许多反应表现出优异催化性能，正逐步为工业催化过程所采用问．较早的研究表明，吸附在活性炭上的杂多酸可部分牢固地存留干其表面不被溶脱，并可保持一定的催化活性＊．关干活性炭表面上杂多酸吸附作用的本质，一直没有明确的结论．本文通过吸附在活性炭表面和溶于含氧有机溶剂中杂多酸的光谱特征，探讨活性炭表面上杂多酸吸附的化学键合作用．1实验部分（且）药品：杂多酸均为市售商品，未经任何处理，直接使用．硅钨酸分子式为儿出风。0。。‘24…     

Hydrophobic interaction chromatography of proteins. IV. Protein adsorption capacity and transport in preparative mode

The adsorption isotherms of four model proteins (lysozyme, α-lactalbumin, ovalbumin, and BSA) on eight commercial phenyl hydrophobic interaction chromatography media were measured. The isotherms were softer than those usually seen in ion-exchange chromatography of proteins, and the static capacities of the media were lower, ranging from 30 to 110 mg/mL, depending on the ammonium sulfate concentration and the protein and adsorbent types. The protein-accessible surface area appears to be the main factor determining the binding capacity, and little correlation was seen with the protein affinities of the adsorbents. Breakthrough experiments showed that the dynamic capacities of the adsorbents at 10% breakthrough were 20-80% of the static capacities, depending on adsorbent type. Protein diffusivities in the adsorbents were estimated from batch uptake experiments using the pore diffusion and homogeneous diffusion models. Protein transport was affected by the adsorbent pore structures. Apparent diffusivities were higher at lower salt concentrations and column loadings, suggesting that adsorbed proteins may retard intraparticle protein transport. The diffusivities estimated from the batch uptake experiments were used to predict column breakthrough behavior. Analytical solutions developed for ion-exchange systems were able to provide accurate predictions for lysozyme breakthrough but not for ovalbumin. Impurities in the ovalbumin solutions used for the breakthrough experiments may have affected the ovalbumin uptake and led to the discrepancies between the predictions and the experimental results.