硅烷化活性炭的吸附性质

本工作测定了25℃和35℃时硅烷化活性炭自水溶液中吸附苯甲酸和苯甲醛的等温线;计算了吸附过程的ΔGⅲ,ΔHⅲ和ΔSⅲ;用Hill-deBoer方程处理了实验结果。所得结果表明:(1)随硅烷化时间延长,苯甲酸和苯甲醛的吸附量(mol.m^-^2)明显增加;-ΔGⅲ和-ΔHⅲ略有升高,ΔSⅲ为正值;(2)吸附分子之间的相互作用很弱,吸附分子与活性炭表面间的作用随硅烷化程度增加而加大;(3)芳香化合物可能是以苯环吸附在炭表面上的。     

甲烷在活性炭上裂解制氢研究

在连续流动石英固定床反应器上研究了甲烷在活性炭上裂解制氢的反应，并对反应前后活性炭的比表面积以及孔径分布等的变化进行了测定。结果表明，甲烷在五种活性炭上的裂解行为基本相同，反应初期转化率最高，随着反应进行转化率逐渐降低直至一个平稳的状态；降低甲烷分压和增加甲烷与活性炭的接触时间可提高甲烷转化率；温度的升高有利于初始转化率的提高，但不利于活性炭的稳定性；反应后活性炭比表面积、孔容及微孔孔容都明显降低，平均孔径增大，孔径分布向中孔方向迁移，说明甲烷的裂解导致了活性炭孔特别是微孔内的炭沉积以及进一步的孔堵塞。     

活性炭电极材料的表面改性和性能

以硝酸、双氧水、氨水三种化学试剂分别对活性炭进行表面改性, 用N2吸附法和FTIR表征炭材料改性前后孔结构和表面官能团的变化. 制备了以改性活性炭为电极材料, KOH溶液为电解质的模拟双电层电容器. 用恒流充放电、循环伏安、交流阻抗等方法考察了双电层电容器的电化学性能. 结果表明, 改性活性炭比表面积和平均孔径有所降低, 并且在炭材料表面引入了含氧或含氮官能团, 如—OH、>CO、—NH2等, 使炭材料的润湿性增强、电阻减小、电化学性能显著提高. 用65%硝酸改性后炭材料的比容量最高达到250 F·g-1, 比原样炭提高了72.4%; 实验电容器的漏电流急剧下降, 只有3-18 μA, 为原来电容器的漏电流(371 μA)的0.8%-4.9%.     

表面功能化的介孔分子筛SBA-3的表征

采用γ-氨丙基三乙氧基硅烷（AM）,通过表面硅烷化反应,对脱模板后的纯 硅六方介孔分子筛SBA-3进行了表面功能化,并通过XRD,TEM,低温N_2吸附, FTIR和吸附染料分子的UV-vis漫反射光谱等对功能化样品的结构、孔性质和表面极 性等进行了详细表征。结果表明,功能分子锚接后,样品的六方结构基本保持。样 品的表面硅羟基由于被消耗而明显减少,导致表面极性降低。另外,由于功能分子 占据了部分孔道空间,样品的孔容、表面积和孔径下降。     

MCM-41分子筛的改性、表面结构与吸附性质的研究

用三甲基氯硅烷、二甲基二氯硅烷、甲基三氯硅烷、四氯化硅与甲基碘改性高硅MCM-41中孔分子筛。XRD,^2^9SiMASNMR,^1^3CMASNMR,以及N~2、水与环己烷吸附的表征,显示改性不同程度地改变了分子筛的表面组成与结构,减小孔径,增加孔壁厚度,因而影响吸附行为,减小吸附容量。硅烷化减少了MCM-41的表面硅羟基含量,增加其疏水性。用CH~3I改性使孔径减小1.4nm,而硅羟基含量并未显著减少。硅烷化以及用CH~3I改性可提高MCM-41分子筛的热稳定性。SiCl~4的改性作用相对不明显。样品的水及环己烷吸附容量与其表面硅羟基含量呈现不同的线性关系,揭示高硅MCM-41分子筛表面吸附中心的本性。     

改性活性炭对噻吩的吸附性能研究

用过硫酸铵、臭氧对椰壳活性炭和煤基活性炭进行氧化改性,研究了改性活性炭对噻吩的吸附性能,材料结构袁征结果表明,经两种方法氧化处理后,椰壳炭的孔结构基本保持不变,而煤基炭的比表面积和孔容有所增加.Boehm滴定发现氧化后活性炭表面含氧官能团数量增加并由FT-TR图谱得到证实.氧化处理提高了噻吩在活性炭表面的吸附容量与Langmuir和Freundlich两种吸附等温线方程的相关性.采用拟一级、拟二级和粒子内扩散模型速率方程来考察吸附动力学,并计算了这些动力学模型的速率常数,拟二级模型和实验数据之间有较好的相关性.同时对影响吸附性能的因素进行了分析.     

葡萄糖加氢用Ru/活性炭催化剂: 改性方法对活性炭表面性能的影响

分别采用超临界甲醇流体、浓硝酸氧化、浓硝酸结合超临界甲醇流体等不同手段对椰壳活性炭进行了表面处理,用N2物理吸附、Boehm滴定、X光电子能谱仪(XPS)、电感耦合等离子原子发射光谱分析(ICP)、透射电镜(TEM)等手段研究了处理方法对活性炭表面孔结构及表面基团的影响;并以活性炭为载体,三氯化钌为活性前驱体,采用等容水浸渍法制备了钌炭催化剂,以葡萄糖加氢生产山梨醇为模型反应对制备的钌基催化剂的催化活性进行了评价.结果表明:各种处理方法对活性炭的比表面、孔径等孔结构性能影响不大;但超临界甲醇处理活性炭可明显减少活性炭表面含氧酸性基团的含量,尤其是羧基等不稳定基团的含量;而硝酸处理活性炭则可大幅度提高活性炭表面含氧酸性基团的含量,尤其是羧基等不稳定基团的含量增加更大.ICP分析结果表明:超临界甲醇处理活性炭并不改变活性炭样品对钌的吸附量,但硝酸氧化处理活性炭却能明显提高样品对钌的吸附能力.活性炭表面的这些含氧基团虽然有利于钌离子的吸附,但却不利于钌在活性炭表面的分散.由于超临界甲醇流体处理活性炭时的表面反应及萃取作用,可有效清除活性炭表面的不稳定含氧酸性基团,避免还原过程中钌的迁移聚集,使负载钌的分散度提高,有利于增强钌与活性炭间的相互作用,使钌部分缺失电子,钌的结合能升高;可明显提高负载钌炭催化剂葡萄糖催化加氢的活性.     

几种典型国产活性炭吸附各种烃类的NMR研究——Ⅱ. 苯、环己烷、正戊烷和正己烷吸附的1H NMR研究

活性炭吸附苯、环己烷、正戊烷和正已烷的测量表明, 在同一种活性炭中各烃的饱和吸附体积相同, 四种烃的吸附量与其摩尔体积成反比。同一种被吸附物在不同活性炭中的吸附量与各活性炭的比孔容和孔径分布有关。活性炭的比孔容大, 且孔径小于3.0 nm的微孔比例大时, 其吸附和解吸容量也大。这些体系的~1H NMR研究进一步证实了孔径小于3.0 nm的微孔中发生毛细管凝聚, 导致吸附和解吸的容量增大。被吸附分子的自旋晶格弛豫时间几乎不随被吸附物的种类而异。他们与活性炭表面上酸性基团总量有较好的曲线关系。     

几种典型国产活性炭吸附各种烃类的NMR研究——Ⅱ.苯、环己烷、正戊烷和正己烷吸附的~1H NMR研究

活性炭吸附苯、环己烷、正戊烷和正已烷的测量表明,在同一种活性炭中各烃的饱和吸附体积相同,四种烃的吸附量与其摩尔体积成反比。同一种被吸附物在不同活性炭中的吸附量与各活性炭的比孔容和孔径分布有关。活性炭的比孔容大,且孔径小于30的微孔比例大时,其吸附和解吸容量也大。这些体系的~1H NMR研究进一步证实了孔径小于30的微孔中发生毛细管凝聚,导致吸附和解吸的容量增大。被吸附分子的自旋晶格弛豫时间几乎不随被吸附物的种类而异。他们与活性炭表面上酸性基团总量有较好的曲线关系。     

石油焦系活性炭的吸附脱硫

选取独山子石油焦为原料，以物理活化法制得比表面积达500m2/g～900m2/g的活性炭，进行吸附脱硫研究。采用酸氧化法对活性炭孔结构和微观孔径分布进行改性。酸氧化使活性炭表面酸性官能团含量明显增加，增加量约为原来的5倍。活性炭吸附脱硫性能随表面酸性官能团含量的增加而增大。理想的酸化条件是浓硝酸120℃氧化40min。通过静态吸附实验，活性炭吸附脱硫的最佳条件是，温度25℃，压力1.0MPa，静态吸附6h。最佳条件下吸附脱硫可使模型化合物硫的质量分数从137.9×10－6降至3.1×10－6。从活性炭孔径匹配考察可知，平均孔直径在0.8nm～2.1nm的活性炭对模型化合物硫的质量分数降低具有明显效果。     

氧化反应对胜利褐煤水蒸气气化反应的促进作用Ⅱ.作用机理研究

在φ80×3 000 mm耐高温不锈钢管反应器中,进行了N2/N2+O2/N2+H2O/N2+O2+H2O气氛下800和900℃的胜利褐煤气化实验,采用红外光谱、X射线光电子能谱、拉曼光谱和烟气在线分析等研究了添加氧气前后半焦的物理结构、官能团及煤气组成的变化,旨在探讨氧化反应促进水蒸气气化反应的作用机理。结果表明,氧化反应对水蒸气气化反应的促进作用可用半焦的微观结构变化和水蒸气气化解离吸附机理解释。氧化反应的开孔和扩孔作用使碳颗粒微孔数量、比表面积、孔容、吸附量明显增加,更多的碳表面活性位暴露出来,也促进了半焦中甲基、亚甲基、C=O键、C-O键的断裂和高活性的羧基COO-和大量氢自由基的生成,这些都有利于水蒸气气化反应的进行,尤其在高温和水蒸气含量较高时。同时,氧气的加入改变了反应气氛中CO2、CO、H2相对含量和水蒸气分子/活性炭原子内能,也有利于水蒸气气化反应的进行,这与水蒸气气化解离吸附机理相吻合。     

The study of controlling pore size on electrospun carbon nanofibers for hydrogen adsorption

Polyacrylonitrile (PAN)-based carbon nanofibers (CNFs) were prepared by using electrospinning method and heat treatment to get the media for hydrogen adsorption storage. Potassium hydroxide and zinc chloride activations were conducted to increase specific surface area and pore volume of CNFs. To investigate the relation between pore structure and the capacity of hydrogen adsorption, textural properties of activated CNFs were studied with micropore size distribution, specific surface area, and total pore volume by using BET (Brunauer-Emmett-Teller) surface analyzer apparatus and the capacity of hydrogen adsorption was evaluated by PCT (pressure-composition-temperature) hydrogen adsorption analyzer apparatus with volumetric method. The surface morphology of activated CNFs was observed by SEM (scanning electron microscope) images to investigate the surface change through activation. Even though specific surface area and total pore volume were important factors for increasing the capacity of hydrogen adsorption, the pore volume which has pore width (0.6-0.7 nm) was a much more effective factor than specific surface area and pore volume in PAN-based electrospun activated CNFs.     

Adsorption study of alkyl-silicas and methylsiloxy-silicas.

We report the synthesis and adsorption study of the lyophobic porous silicas. Four adsorbents were prepared and tested: (1) octyl-silica, (2) hexadecyl-silica, (3) bis(trimethylsiloxy)-silica, and (4) oligo(dimethylsiloxane)-silica. Octyl- and hexadecyl-silicas were prepared via the reaction of silica with (CH3)2NSi(CH3)2CnH(2n+1) (n=8 and 16), the reactions were carried under the optimized conditions yielding high bonding densities of alkyl groups approximately 2.9-3.0 groups/nm2 and highly uniform non-polar adsorbents. Bis(trimethylsiloxy)-silica was prepared via the reaction silica with ClSi(CH3)2(CH2)10Si(CH3)[OSi(CH3)3]2. Oligo(dimethylsiloxane)-silica was prepared via the reaction of silica with ClSi(CH3)2-[OSi(CH3)2]2-Cl. Adsorption of small organic compounds (n-alkanes, alkylbenzene, benzene, diethyl ether) was investigated using two methods, classical static adsorption and gas chromatography. Thermodynamic parameters (heat, Gibbs energy, and entropy) of the adsorption of organic compounds were studied as a function of the nature of adsorbate and of the nature of the bonded layer as well. The results obtained suggest penetration of the adsorbate molecules into the bonded layer and the importance of this process in the retention mechanism in gas chromatography. Energy of the dispersion interactions with the surface decreases in the following order: n-C16H33(CH3)2Si- > n-C8H17(CH3)2Si- > [(CH3)3SiO]2Si(CH3)-(CH2)10(CH3)2Si- > -[[(CH3)2SiO]2]x-(CH3)2Si-. Energy of the electrostatic and hydrogen bonding interactions with the surface, as assessed from the adsorption of benzene and diethyl ether molecules, decreases in the opposite direction, indicating that alkyl-silicas are less polar adsorbents than methylsiloxy-silicas.     

Comparison of dye adsorption by mesoporous hybrid gels: understanding the interactions between dyes and gel surfaces

Without using any templating agents, mesoporous hybrid gels were prepared using mixtures of tetraethoxysilane (TEOS) with n-propyltriethoxysilane (PTES), bis(trimethoxysilyl)hexane (TSH), or bis(trimethoxysilylpropyl)amine (TSPA) as precursors. Fourier transform infrared (FTIR), N2 adsorption/desorption, thermogravimetry (TG), point of zero charge (PZC), and water vapor adsorption measurements were used to characterize the gels. The adsorption of methyl orange (MO), methyl red (MR), bromocresol purple (BP), phenol red (PR), neutral red (NR), and brilliant blue FCF (BBF) by the gels in both 0.01 M HCl and 0.01 M NaOH solutions was compared comprehensively. The gel derived from TEOS/TSH (with -(CH2)6- groups, Gel 2) has the largest specific surface area (695 m2 g(-1)), the smallest pore volume (0.564 cm3 g(-1)), and the smallest average pore size (3.7 nm). The gels derived form TEOS/PTES (with -(CH2)2CH3 groups, Gel 1), and TEOS/TSPA (with -(CH2)3NH(CH2)3- groups, Gel 3) have similar textual properties. The PZC of Gels 1, 2, and 3 was estimated to be 6.28, 6.20, and 6.88, respectively. Gel 3 has the highest PZC due to the presence of -NH- groups. In general, Gel 2 shows the highest dye adsorption among all the gels in both acidic and basic solutions. All the dyes except NR have much lower adsorption in basic solutions than in acidic solutions. In acidic solutions Gels 1 and 2 have similar adsorption trends for the dyes, except for BP, with NR having the highest adsorption, and PR the lowest adsorption. Gel 3 presents a different trend from Gels 1 and 2, with BBF having the highest adsorption, and MR the lowest adsorption. In basic solutions the order of dye adsorption by all the gels is shown to follow the sequence NR>MR approximately BBF>MO>BP approximately PR. The adsorption results can be explained by considering the textural properties of the gels and the interactions between the gel surfaces and the dyes, which include hydrogen bonding, electrostatic, and hydrophobic interactions.     

Effect of carbon pore structure on the CH4/N2 separation

The separation between CH₄ and N₂ bears importance in coalbed methane enrichment, and activated carbon is a major adsorbent for industrial PSA (pressure swing adsorption) separation. However, the adsorption of both gases shows supercritical features, and the physicochemical properties are also similar, which results in similar adsorption behavior and renders the separation difficult. To maximize the separation coefficient, the effect of carbon pore structure on the separation was studied and a series of carbons was prepared at different extent of activation. The effect of specific surface area, pore size and pore volume on the separation coefficient was observed and a linear correlation between the separation coefficient and the small pore (0.7–1.3?nm) volume reduced to unit surface area was shown.     

沥青基球状活性炭气相吸脱附行为研究

本文利用热重法研究了一系列沥青基球状活性炭对蒸汽及正已烷蒸汽的动态吸脱附曲线。结果表明,PSAC对苯蒸汽的吸附及再生性能优良。随吸附温度的降低、比表面积的增大、总孔容及微孔容的增大,PSAC对苯蒸汽的吸附容量增大。PSAC对正已烷的吸附速度大于对苯蒸汽的吸附速度,但其对正已烷的平衡吸附容量小于对苯蒸汽的平衡吸附容量。     

溶剂萃取对烟煤孔隙结构和粒度的影响

用二硫化碳-N-甲基-2-吡咯烷酮（CS2-NMP）(1∶1, V/V) 混合溶剂、丙酮和吡啶对南桐烟煤逐级萃取，得到各级残余物。通过比表面积及孔快速测试仪和扫描电镜，对煤及各萃取残余物的氮气吸附行为、粒度进行测试，考察了溶剂萃取对煤的BET比表面积与BJH孔容、孔面积随孔径分布规律以及粒度的影响。结果表明通过“溶解”小分子物质，溶剂萃取能够有效地改善煤的吸附性、比表面积和孔隙结构，降低其粒度，但不能破坏其基本结构单元，在本质上仍属于物理作用。根据最可几孔径计算出南桐烟煤胶态分子团结构模型中基本结构单元的粒径在3.5 nm左右，证实了煤分子胶态团结构模型的假设。     

Adsorption-Desorption Characteristics of Water Vapor on Functional Cattle Bone-Originated Apatites Powders with Mesopores

Microcrystals of cattle bone-originated apatites (r-HAp) were prepared by the dissolution-precipitation and freeze-drying processes. The r-HAp particles obtained gave 128 m 2 ;g m 1 specific surface area and 0.376 cm 3 ;g m 1 total pore volume and strong basic surface with mesopores. All the adsorption isotherms of water vapor at 288-308 K for the r-HAp powders obeyed IV-type in a classification of the BDDT. In the repeated adsorption-desorption operations, an adsorption hysteresis resulting from mesopores was recognized. The amounts of water vapor adsorbed obtained in the first adsorption operation were larger than those in the second adsorption operation, indicating that some portion of water vapor adsorbed to be irreversible adsorption. The water vapor-adsorption heats for the r-HAp were 45-60 kJ;mol m 1 , whose values were higher than natural diatomite. The amounts of water vapor adsorbed for the r-HAp were larger than those for the adsorbents, such as natural diatomite, aerosol silica, and activated carbon, at the relative partial pressures of 0-0.7.     

Characteristics of Nonafluorobutyl Methyl Ether (NFE) Adsorption onto Activated Carbon Fibers and Different-Size-Activated Carbon Particles

The characteristics of adsorption of 1,1,1,2,2,3,3,4,4-nonafluorobutyl methyl ether (NFE), a chlorofluorocarbon (CFC) replacement, onto six different activated carbon; preparations (three activated carbon fibers and three different-sized activated carbon particles) were investigated to evaluate the interaction between activated carbon surfaces and NFE. The amount of NFE adsorbed onto the three activated carbon fibers increased with increasing specific surface area and pore volume. The amount of NFE adsorbed onto the three different-sized-activated carbon particles increased with an increase in the particle diameter of the granular activated carbon. The differential heat of the NFE adsorption onto three activated carbon fibers depended on the porosity structure of the activated carbon fibers. The adsorption rate of NFE was also investigated in order to evaluate the efficiency of NFE recovery by the activated carbon surface. The Sameshima equation was used to obtain the isotherms of NFE adsorption onto the activated carbon fibers and different-sized-activated carbon particles. The rate constant k for NFE adsorption onto activated carbon fibers was larger for increased specific surface area and pore volume. The rate of NFE adsorption on activated carbons of three different particle sizes decreased with increasing particle diameter at a low initial pressure. The adsorption isotherms of NFE for the six activated carbons conformed to the Dubinin-Radushkevich equation; the constants BE(0) (the affinity between adsorbate and adsorbent) and W(0) (the adsorption capacity) were calculated. These results indicated that the interaction between the activated carbon and NFE was larger with the smaller specific surface area of the activated carbon fibers and with the smaller particle diameter of the different-sized-activated carbon particles. The degree of packing of NFE in the pores of the activated carbon fibers was greater than that in the pores of the granular activated carbons. Copyright 2000 Academic Press.