氧化锆-活性炭纤维复合材料的制备及其对F-吸附性能

采用水热合成法成功制备了氧化锆-活性炭纤维复合材料,并研究了其对F^-的吸附行为.表征结果表明,复合材料中氧化锆粒子成功负载于活性炭纤维上.吸附实验结果表明,负载了氧化锆的活性炭纤维对F^-有高效的去除效率,其吸附机理包括离子交换和静电作用力,吸附等温线符合Langmuir等温吸附模式,吸附动力学可用拟二级动力学模型拟合.吸附量随着溶液pH的升高而降低,共存离子Cl^-、NO₃^-和SO₄^2-对F^-在氧化锆-活性炭纤维复合材料上的吸附几乎没有影响.     

活性炭纤维吸附的研究：Ⅰ—不同工艺制备的活性炭纤维的性能比较

本文比较研究了五种不同工艺制备的活性炭纤维的产率，比表面积，孔结构，对有机溶剂蒸汽的吸附和脱附性能，对水溶液中亚甲基兰，苯酚和碘的吸附性能以及它们的热稳定性。实验结果表明，水蒸气活化的ＡＣＦ比化学活化的ＡＣＦ有更大的比表面积，但前者产品产率较低而后者很高；不论水蒸气活化还是化学活化的ＡＣＦ，它们对有机溶剂饱和蒸汽的吸附量都较高，脱附和再吸附的性能也都较好，对水溶液中的苯酚都有较好的吸附能力，但化学     

Gd掺杂TiO2/活性炭纤维复合材料的制备及表征

以TiCl4和Gd(NO3)3·6H2O为主要原料,采用酸催化水解法制备Gd掺杂TiO2光催化剂并通过浸涂法将其负载在活性炭纤维(ACF)表面,制得Gd掺杂TiO2/ACF复合材料。 以气相苯为模型物,考察材料的光催化活性。 利用XRD、FTIR及GC-MS对催化剂的晶相结构、光谱特征等进行了表征。 结果表明,Gd掺杂能有效抑制TiO2的晶粒生长。 Gd掺杂量、浸涂次数影响TiO2/ACF光催化活性,Gd2O3掺杂质量分数为0.48%、浸涂2次的TiO2/ACF活性最高。 在苯光催化氧化后的Gd掺杂TiO2/ACF复合材料表面未发现醌类中间产物的存在。 Gd的掺入能减缓催化剂失活,光催化反应100 min后仍能表现出较高活性。     

活性炭纤维吸附脱除硫化氢研究进展

从活性炭纤维(ACF)的结构特点、未改性ACF吸附H2S和改性ACF吸附H2S三方面综述了国内外对ACF吸附H2S的研究进展。归纳了ACF的改性方法、ACF吸附H2S的反应机理和动力学研究。总结了相对湿度、原料气组成、生成物和改性方法等工艺条件对ACF吸附H2S性能的影响。展望了改性ACF吸附脱除H2S的研究前景。     

活性炭纤维对CS2蒸气的动态吸附研究

本文选用国产聚丙烯腈基活性炭纤维(CPANACF)作吸附剂,过热水蒸气作脱附剂,研究了CS_2蒸气的吸附与脱附的动态行为,分析了动态吸附影响因素。结果表明,该吸附体系是以气相界膜外扩散控制为主的,其吸附波遵循恒定模式规则,低温、低浓度、高流速等对吸附有利。     

活性炭纤维对气相低浓度三氯乙烯的动态吸附

研究了3种不同经表面积活性炭纤维（ACF）对气相低浓度三氯乙烯（TCE）的动态吸附。ACF的比表面积为600m^2/g、1400m^2／g和1600m^2/g，TCE的浓度范围为27mg/m^3-2725mg/m^3。结果表明，比表面积为1400m^2/g和1600m^2/g的ACF对TCE的吸附较好；10％穿透时间的对数与TCE匠对数呈线性关系；穿透时间随温度和湿度的增加而缩短；穿透曲线可以用经验公式拟合。拟合值和实测值吻合良好；ACF吸附是去除气相低浓度TCE的有效方法。     

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。     

中孔活性炭纤维对VB12的吸附性能研究

用炭黑政性聚丙烯腈原丝，制得了富含中孔的活性炭纤维，研究了它对大分子物质VB12的吸附性能。     

活性炭纤维吸附-蒸汽脱附回收三氯甲烷工程实例分析

采用活性炭纤维吸附-蒸汽脱附装置对江苏南通某农药厂生产工序中排放的三氯甲烷进行吸附回收。论述了该农药厂有机废气收集和处理现状、吸附剂选择、吸附装置工艺流程及操作参数、必要的安全保障等。现场运行数据表明:装置运行稳定,三氯甲烷回收率稳定在99%左右,自动化控制水平高,安全性能好,回收的三氯甲烷质量好。使用该装置后,每年可回收三氯甲烷约155 t,年净收益38万元。     

Gd掺杂TiO2/活性炭纤维复合材料的制备及表征

以TiCl4和Gd(NO3)3·6H2O为主要原料,采用酸催化水解法制备Gd掺杂TiO2光催化剂并通过浸涂法将其负载在活性炭纤维(ACF)表面,制得Gd掺杂TiO2/ACF复合材料。 以气相苯为模型物,考察材料的光催化活性。 利用XRD、FTIR及GC-MS对催化剂的晶相结构、光谱特征等进行了表征。 结果表明,Gd掺杂能有效抑制TiO2的晶粒生长。 Gd掺杂量、浸涂次数影响TiO2/ACF光催化活性,Gd2O3掺杂质量分数为0.48%、浸涂2次的TiO2/ACF活性最高。 在苯光催化氧化后的Gd掺杂TiO2/ACF复合材料表面未发现醌类中间产物的存在。 Gd的掺入能减缓催化剂失活,光催化反应100 min后仍能表现出较高活性。     

Competitive Adsorption of Chloroform and Iron Ion onto Activated Carbon Fiber

Chloroform in tap water has been a significant problem because it may be a carcinogenic substituent. Iron ion exists in tap water because of dissolution from iron water pipes. Iron ions in tap water cause discoloration and a bad odor. The isotherms of chloroform and iron ion adsorption onto activated carbon fibers in a single solution (chloroform or iron ion) and in a binary mixture solution (chloroform and iron ion) were investigated to estimate the competitiveness between chloroform and iron ions. The amount of adsorbed iron ions increased with increasing pore volume of the activated carbon fibers, while that of chloroform decreased. The amount of chloroform adsorbed onto the activated carbon fibers in the binary mixture solution was greater than that in the single solution. These results indicate that the adsorption of chloroform and iron ion onto activated carbon fibers could be competitive.     

磷在氧化锆-碳纳米管复合材料上的吸附研究

采用水热合成法成功制备了氧化锆-碳纳米管复合材料,并研究了对磷的吸附行为。表征结果表明,碳纳米管经氧化锆修饰后仍具备介孔结构;氧化锆粒子可均匀分散在碳纳米管表面。吸附实验结果表明,氧化锆粒子的粒径越小,氧化锆对磷的标化平衡吸附量越高,吸附速率越快。磷在氧化锆-碳纳米管复合材料上的吸附等温线符合Freundlich等温吸附模式,属于优先吸附,吸附动力学可用拟二级动力学模型描述。降低离子强度和溶液pH可促进磷的吸附,共存离子对磷吸附具有抑制作用,影响顺序依次为F->NO3-≈SO42-,其中F-影响最大,NO3-和SO42-次之。     

染料在剑麻基活性碳纤维上吸附速度的研究

本文研究了单组分染料在活性碳纤维上的吸附速度及双组分染料的竞争吸附速度。研究结果表明,不同染料分子在ＳＡＣＦ上吸附速度差异较大,结晶紫的吸附速度比亚甲基蓝或铬蓝黑Ｒ慢行多。亚甲基蓝和铬蓝黑Ｒ双组分共存时,其吸附速度与单组分时的相近,但初始阶段亚甲基蓝的吸附比铬蓝黑Ｒ快得多。由于染料的分子尺寸与ＡＣＦ的微孔大小相近,染料在活性碳纤维上的七染料孤及活怀碳纤维的孔结构密切相关。因此,不同染料分子在ＡＣＦ     

负载Pt活性炭纤维对NO的吸附活性

 采用电化学方法制备了负载Pt的活性炭纤维，为研究其微孔结构、Pt的分散性以及对NO的吸附活性，分别考察了其对氮气、水和NO的吸附．电沉积Pt活性炭纤维的氮吸附等温线仍呈Langmuir型，表面积和微孔孔径基本不变；对水的初始吸附点数远远大于活性炭纤维．这表明电沉积Pt没有改变活性炭纤维的微孔结构，Pt粒高度分散在活性炭纤维的外表面．而NO的吸附量显著增加，说明存在化学吸附．     

Adsorption of Carbon Dioxide on Activated Carbon

The adsorption of CO2 on a raw activated carbon A and three modified activated carbon samples B, C, and D at temperatures ranging from 303 to 333 K and the thermodynamics of adsorption have been investigated using a vacuum adsorption apparatus in order to obtain more information about the effect of CO2 on removal of organic sulfur-containing compounds in industrial gases. The active ingredients impregnated in the carbon samples show significant influence on the adsorption for CO2 and its volumes adsorbed on modified carbon samples B, C, and D are all larger than that on the raw carbon sample A. On the other hand, the physical parameters such as surface area, pore volume, and micropore volume of carbon samples show no influence on the adsorbed amount of CO2. The Dubinin-Radushkevich (D-R) equation was the best model for fitting the adsorption data on carbon samples A and B, while the Preundlich equation was the best fit for the adsorption on carbon samples C and D. The isosteric heats of adsorption on carbon samples A, B, C, and D derived from the adsorption isotherms using the Clapeyron equation decreased slightly increasing surface loading. The heat of adsorption lay between 10.5 and 28.4 kJ/mol, with the carbon sample D having the highest value at all surface coverages that were studied. The observed entropy change associated with the adsorption for the carbon samples A, B, and C (above the surface coverage of 7 ml/g) was lower than the theoretical value for mobile adsorption. However, it was higher than the theoretical value for mobile adsorption but lower than the theoretical value for localized adsorption for carbon sample D.     

萘在粘胶基活性炭纤维上的吸附

研究了水溶液中萘在粘胶基活性炭纤维(VACF)吸附剂上的等温吸附.用多种吸附方程(Langmuir、Freundlich、Dubinin-Radushkevitch(D-R)、Dubinin-Astalov(D-A)、Langmuir-Freundlich(L-F)、Redlich-Peterson(R-P))对吸附实验数据进行拟合,考察了温度、pH和负载铜离子对萘吸附的影响.方程拟合结果表明微孔吸附容积填充理论对VACF吸附萘有较好的适用性,优于单层吸附理论.在20-40℃之间,萘的吸附是自发进行的,30℃以上时,萘的吸附量显著降低.提出了新的机理来解释pH较低时吸附量显著上升的实验现象.负载铜离子后VACF对萘吸附量降低.     

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.     

Adsorption of p-Nitrophenol in Untreated and Treated Activated Carbon

The adsorption of p-nitrophenol in one untreated activated carbon (F100) and three treated activated carbons (H₂, H₂SO₄ and Urea treated F100) was carried out at undissociated and dissociated conditions.To characterize the carbon, N₂ and CO₂ adsorption were used. X-ray Photoelectron Spectroscopy (XPS) was used to analyze the surface of the activated carbon.The experimental isotherms are fitted via the Langmuir homogenous model and Langmuir binary model. Variation of the model parameters with the solution pH is studied. Both Q _max and the adsorption affinity coefficient (K ₁) were dependent on the PZC of the carbons and solution pH. The Effect of pH must be considered due to its combined effects on the carbon surface and on the solute molecules. Adsorption of p-nitrophenol at higher pH was found to be dependent on the concentration of the anionic form of the solute.