对苯二甲酸-锌配合物孔结构的研究

以硝酸锌和对苯二甲酸为反应物,N,N′-二甲基甲酰胺(DMF)为溶剂,用溶剂热法合成出结构稳定的对苯二甲酸-锌配位化合物(MOF-L)。并采用XRD、TG、低温N₂吸附等测试手段对合成的MOF-L进行了表征。结果表明,样品的孔径分布均呈双峰型,孔结构主要由孔径小于1 nm的微孔和少量1.5～2.0 nm的超微孔组成,且小于0.7 nm的极微孔丰富;其表面在极微孔和超微孔范围存在两种吸附位。300 ℃煅烧的样品,Langmuir比表面积和单点总孔容分别为1 243 m²·g^-1和0.46 cm³·g^-1,在77 K、1.0 bar时的储氢容量为1.3wt%。400 ℃煅烧后,骨架扭曲坍塌,Langmuir比表面积、总孔容及储氢容量分别下降为1 113 m²·g^-1、0.43 cm³·g^-1和0.8wt%。     

常温合成硫掺杂微孔碳及其二氧化碳的吸附性能

常温下以间苯三酚和3-甲醛苯并噻吩作为原料,一步法合成了含硫酚醛树脂。在氩气保护下碳化,成功制备出了硫掺杂多孔碳（S-PC）。并利用扫描电镜（SEM）、X射线光电子能谱（XPS）、X射线衍射（XRD）和氮气吸附-脱附仪对材料进行了形貌、结构和性能的表征。实验结果表明,所得样品具有较高比表面积和大量的微孔,经过调控,可以使制备的硫掺杂多孔碳的BET比表面积达到997 m²·g^-1,并使其微孔孔体积达到0.44 cm³·g^-1。得益于较高的比表面积以及其富含微孔的特性,当材料应用于二氧化碳吸附时,具有较高的CO₂吸附量,在273和298 K时分别高达5.13,3.22 mmol·g^-1,并具有良好的选择性。     

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.     

电化学双电层电容器电极材料——豌豆荚基活性炭的制备与表征

以豌豆荚为碳源、ZnCl₂或KOH为活化剂制备了活性炭, 并用作双电层电容器的电极材料. 采用比表面及孔隙度分析仪表征了豌豆荚基活性炭的孔结构. 通过KOH或ZnCl₂活化后, 活性炭比表面积从1.69 m²·g^-1增大到2237或621 m²·g^-1. 采用循环伏安法和恒流充放电测试技术表征了豌豆荚基活性炭的电化学特性. 结果表明: 在6 mol·L^-1 KOH溶液中经KOH活化处理的活性炭的质量比电容高达297.5 F·g^-1, 并具有良好的充放电稳定性, 在5 A·g^-1的高电流密度下循环充放电500次后, 质量比电容仅衰减8.6%.     

功能化有序介孔碳对重金属离子Cu(II)、Cr(VI)的选择性吸附行为

以三嵌段共聚物F127为模板剂, 酚醛树脂为碳源, 正硅酸乙酯为硅源, 三组分共组装合成介孔碳?氧化 硅纳米复合物, 再经HF去除氧化硅, 得到有序介孔碳(OMC). X射线衍射(XRD)、透射电子显微镜(TEM)、低温 N2吸脱附(BET)等测试表明, 所得样品具有高度有序的介孔结构, 比表面积和孔容分别为1330 m²·g^-1和2.13 cm³·g^-1, 平均孔径6.4 nm. 对其先氧化、后氯化、再胺化, 得到不同胺基接枝量的胺化介孔碳(C-NH₂(m), m为加入的乙二胺的质量(g)). 傅里叶变换红外(FT-IR)光谱表征结果证实, 胺基官能团成功接枝到有序介孔碳表面.TEM测试表明介孔碳的有序孔道结构得到了较好的保持. 以有序介孔碳、胺化介孔碳作吸附剂对Cu(II)、Cr(VI)进行选择性吸附研究. 结果表明: 功能化修饰前, 样品对Cu(II)、Cr(VI)饱和吸附量分别为213.33、241.55 mg·g^-1; 修饰后饱和吸附量可分别达到495.05、68.21 mg·g^-1. 功能化介孔碳表现了较强的选择性吸附Cu(II)的能力.     

溶液燃烧法制备的Ni基催化剂及其浆态床甲烷化催化性能

分别以硝酸铝、硝酸氧锆、硝酸镧和硝酸铈为载体前驱体,与硝酸镍和尿素配制水溶液,采用溶液燃烧法制备了Ni-Al₂O₃、Ni-ZrO₂、Ni-La₂O₃和Ni-CeO₂催化剂,研究了浆态床CO甲烷化催化性能,并进行了低温N₂吸附-脱附、XRD、SEM、TEM、H₂-TPR和H2化学吸附等表征分析.结果表明,以硝酸铝为前驱体制备Ni-Al₂O₃催化剂时燃烧火焰稳定且持续时间长,达23 s,样品比表面积(468 m²·g^-1)和金属Ni表面积(10 m²·g^-1)均较大、Ni粒径小(3~5 nm)且分散度高,CO甲烷化催化活性和稳定性好,CO转化率和CH₄选择性分别达到94%和95%,在100 h的甲烷化反应中未出现明显失活;以硝酸氧锆和硝酸镧为前驱体制备样品时未出现明显的燃烧火焰,持续时间仅为12 s和5 s,催化剂比表面积、金属表面积及催化活性均较低;以硝酸铈为前驱体制备样品时燃烧过程迅速而剧烈,样品比表面积(22 m²·g^-1)和金属Ni表面积(5 m²·g^-1)小、Ni粒径大且分散性差,甲烷化催化性能最差,CO转化率仅为41%,CH₄选择性仅为89%.     

微孔共轭聚合物热解制备氮、硫杂原子硬炭及其储锂性能

选取溴代噻唑和三乙炔基苯为单体,利用聚合反应自下而上构建含噻唑共轭微孔聚合物(NSCMP),通过热解和KOH活化热解NSCMP制备了氮、硫杂原子硬炭(NSHC)和活化NSHC(KNSHC)。利用扫描电子显微镜、能量色散谱、氮气吸附-脱附和恒流充放电等表征2个样品的结构与电化学性能。研究表明KNSHC中N和S的质量分数分别为10.42%和2.23%,KNSHC比表面积高达2 140 m²·g^-1。在0.2 A·g^-1电流密度下循环500次后KNSHC和NSHC的可逆比容量分别为946.2和493.7 mAh·g^-1。KNSHC的优异电化学性能归因于其独特的孔结构和氮、硫杂原子的协同作用。     

Jeffamine聚醚胺改性合成介孔及超微孔氧化硅微球

通过对Jeffamine ED2003进行硬脂酸接枝,获得了一种在水溶液中能够进行自组装的新型聚醚酰胺高分子表面活性剂,命名为ED2003-fa-18。以ED2003-fa-18聚醚酰胺高分子表面活性剂为模板,以正硅酸乙酯(TEOS)为无机硅源,在酸性条件下水热合成了介孔及超微孔氧化硅微球。利用粉末X射线衍射(XRD)、N₂物理吸附、红外光谱(IR)、核磁共振波谱(¹H NMR)、扫描电镜(SEM)和透射电镜(TEM)等方法对合成样品进行了表征。研究结果表明,通过改变合成体系中表面活性剂的浓度,可控合成出了有序的介孔及超微孔氧化硅材料。当ED2003-fa-18的浓度为1wt%时,合成的材料为介孔氧化硅,样品的最可几孔径约为2.2nm。当ED2003-fa-18的浓度从3wt%增加到7wt%时,样品的最可几孔径从1.98nm减小到1.94nm,得到的样品为超微孔氧化硅材料。样品的比表面积在500m²·g^-1左右,孔体积在0.3cm³·g^-1左右。由SEM照片可知,所合成的介孔及超微孔氧化硅材料均为由20~30nm的球形纳米颗粒进一步团聚形成的2~4μm的紧密堆积的实心微球。     

Jeffamine聚醚胺改性合成介孔及超微孔氧化硅微球

通过对Jeffamine ED2003进行硬脂酸接枝,获得了一种在水溶液中能够进行自组装的新型聚醚酰胺高分子表面活性剂,命名为ED2003-fa-18.以ED2003-fa-18聚醚酰胺高分子表面活性剂为模板,以正硅酸乙酯(TEOS)为无机硅源,在酸性条件下水热合成了介孔及超微孔氧化硅微球.利用粉末X射线衍射(XRD)、N₂物理吸附、红外光谱(IR)、核磁共振波谱(¹H NMR)、扫描电镜(SEM)和透射电镜(TEM)等方法对合成样品进行了表征.研究结果表明,通过改变合成体系中表面活性剂的浓度,可控合成出了有序的介孔及超微孔氧化硅材料.当ED2003-fa-18的浓度为1wt%时,合成的材料为介孔氧化硅,样品的最可几孔径约为2.2 nm.当ED2003-fa-18的浓度从3wt%增加到7wt%时,样品的最可几孔径从1.98 nm减小到1.94 nm,得到的样品为超微孔氧化硅材料.样品的比表面积在500 m²·g^-1左右,孔体积在0.3 cm³·g^-1左右.由SEM照片可知,所合成的介孔及超微孔氧化硅材料均为由20~30 nm的球形纳米颗粒进一步团聚形成的2~4 μm的紧密堆积的实心微球.     

活性炭的孔径分布对CH4和CO2的吸附性能的影响

采用不同炭化温度和活化温度,以椰壳作为前驱体制备了系列结构性能相同,表面吸附基团相似,不同孔结构的活性炭。分别采用密度函数理论(DFT)吸附法和BJH估算了系列活性炭的孔径分布。结果表明,随炭化温度和活化温度的升高系列活性炭中微孔量先增加后减少。当炭化温度为700 ℃,活化温度为800 ℃时,制备的活性炭微孔量达到最大。随炭化温度和活化温度的升高,系列活性炭的中孔依次增加。考查了CH₄,CO₂在系列活性炭上的吸附性能。结果表明该系列活性炭对CO₂有很强的吸附能力,在常温常压下对CO₂的吸附量均高于1.0 mmol·g^-1;系列活性炭对CH₄的吸附能力有较大的差异,在对CO₂具有最大吸附量的活性炭上对CH₄具有最小的吸附量。采用变压吸附法测试了该系列活性炭在25 ℃时对n_CH4∶n_CO2=9∶1的混合气体的分离性能。结果表明炭化温度为700 ℃,活化温度为800 ℃时制备的活性炭对CH₄-CO₂混合气具有最好的分离效果,是变压吸附分离CH₄,CO₂混合气的优异吸附剂。     

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.     

有序介孔碳的微波快速合成和表面修饰及其负载性能

以低聚合度酚醛树脂为碳源、三嵌段共聚物F127(Mw=12600,PEO106PPO70PEO106)为模板导向剂,以微波辐照替代传统的烘箱热聚合,在常见功率下(400～800W)快速(15～60min)聚合,并高温碳化获得介孔碳。XRD、TEM、低温N2吸脱附等测试表明所得样品具有高度有序的介孔结构,比表面积和孔容分别可达614m2·g-1和0.47cm3·g-1。合成的介孔碳经NaBH4和胶体钯溶液两步修饰处理,表面被活化并沉积了Pd颗粒,导电性和亲水性均得到改善,载Pt的量和分散性明显提高,Pt/C催化剂的电化学活性面积由4m2·g-1增加到29m2·g-1。     

Hydrogen adsorption in transition metal carbon nano-structures

Templated microporous carbons were synthesized from metal impregnated zeolite Y templates. Scanning Electron Microscopy (SEM) and Transmission Electron Microscopy (TEM) were employed to characterize morphology and structure of the generated carbon materials. The surface area, micro- and meso-pore volumes, as well as the pore size distribution of all the carbon materials were determined by N₂ adsorption at 77 K and correlated to their hydrogen storage capacity. All the hydrogen adsorption isotherms were Type 1 and reversible, indicating physisorption at 77 K. Most templated carbons show good hydrogen storage with the best sample Rh-C having surface area 1817 m²/g and micropore volume 1.04 cm³/g, achieving the highest as 8.8 mmol/g hydrogen storage capacity at 77 K, 1 bar. Comparison between activated carbons and synthesized templated carbons revealed that the hydrogen adsorption in the latter carbon samples occurs mainly by pore filling and smaller pores of sizes around 6 Å to 8 Å are filled initially, followed by larger micropores. Overall, hydrogen adsorption was found to be dependent on the micropore volume as well as the pore-size, larger micropore volumes showing higher hydrogen adsorption capacity.     

TiO2-SiO2复合气凝胶：常压干燥制备及性能表征

以廉价的四氯化钛和工业水玻璃为原料,通过溶胶-凝胶法制得TiO2-SiO2复合湿凝胶,用三甲基氯硅烷(TMCS)/乙醇(EtOH)/正己烷(Hexane)混合溶液对湿凝胶进行改性,常压干燥制备了TiO2-SiO2复合气凝胶.利用扫描电子显微镜(SEM)、透射电子显微镜(TEM)、红外光谱(FTIR)、X射线衍射(XRD)及N2吸附/脱附法对复合气凝胶的形貌和性质进行了分析.结果表明,TiO2-SiO2复合气凝胶具有连续多孔结构,150℃干燥后复合气凝胶的比表面积为1 076 m2·g-1,孔体积为4.96 cm3·g-1;经550 ℃热处理后,复合气凝胶仍然具有高的孔隙率,比表面积为856 m2·g-1,孔体积为3.46 cm3·g-1.吸附和光催化降解罗丹明B的结果表明,复合气凝胶同时具有较好的吸附和光催化性能,其吸附/光催化协同作用活性优于纯SiO2气凝胶和锐钛矿TiO2粉末;且重复利用四次降解率仍然可达到89%.     

α-Fe_2O_3空心球的水热法制备及其对苯酚的吸附性能

以铁氰化钾、磷酸二氢铵等为反应物,采用水热法合成了α-Fe2O3空心球,并用XRD,TEM,FESEM(场发射扫描电镜)、UV-Vis和低温氮吸附脱附对其进行了表征。结果表明,α-Fe2O3空心球直径在200～560nm之间,其BET比表面积为80m2·g-1,平均孔径为8.5nm。考察了反应时间、反应物用量和反应温度等对α-Fe2O3空心球形貌和大小的影响,提出了其可能的形成机理。研究了室温下α-Fe2O3空心球吸附苯酚的性能,吸附达平衡时,其吸附苯酚的量达97mg·g-1。     

A study on pore-opening behaviors of graphite nanofibers by a chemical activation process

In this work, porous graphite nanofibers (GNFs) were prepared by a KOH activation method in order to manufacture porous carbon nanofibers. The process was conducted in the activation temperature range of 900-1100 degrees C, and the KOH:GNFs ratio was fixed at 3.5:1. The textural properties of the porous carbons were analyzed using N2 adsorption isotherms at 77 K. The BET, D-R, and BJH equations were used to observe the specific surface areas and the micro- and mesopore structures, respectively. From the results, it was found that the textural properties, including the specific surface area and the pore volumes, were proportionally enhanced with increasing activation temperatures. However, the activation mechanisms showed quite significant differences between the samples activated at low and high temperatures.     

Influence of surface treatments on micropore structure and hydrogen adsorption behavior of nanoporous carbons

The scope of this work was to control the pore sizes of porous carbons by various surface treatments and to investigate the relation between pore structures and hydrogen adsorption capacity. The effects of various surface treatments (i.e., gas-phase ozone, anodic oxidation, fluorination, and oxygen plasma) on the micropore structures of porous carbons were investigated by N(2)/77 K isothermal adsorption. The hydrogen adsorption capacity was measured by H(2) isothermal adsorption at 77 K. In the result, the specific surface area and micropore volume of all of the treated samples were slightly decreased due to the micropore filling or pore collapsing behaviors. It was also found that in F(2)-treated carbons the center of the pore size distribution was shifted to left side, meaning that the average size of the micropores decreased. The F(2)- and plasma-treated samples showed higher hydrogen storage capacities than did the other samples, the F(2)-treated one being the best, indicating that the micropore size of the porous carbons played a key role in the hydrogen adsorption at 77 K.     

Porous properties of silylated mesoporous silica and its hydrogen adsorption

Porous properties of mesoporous silica silylated with various organic silanes were examined and their hydrogen adsorption properties were measured at 77 K. By silylation of the mesoporous silica, the specific surface area, pore radius and pore volume steeply decreased depending on both the size of the silane and the amount actually incorporated into the mesoporous framework. The pores reduced in size depending on the amount of modifying silane and vanished completely in the samples silylated with 3-aminopropyltriethoxysilane and phenyltrichlorosilane. Hydrogen adsorption isotherms of the silylated samples were measured at 77 K. With the exception of the sample with phenyltrichlorosilane, hydrogen adsorption volumes were proportional to the surface area with a slope of around 1.1 molecules/nm². On the other hand, for the sample treated with phenyltrichlorosilane, a large hydrogen adsorption volume of around 38.1 molecules/nm² was obtained. On heating the silylated compounds at 500 °C, micropores formed and the hydrogen adsorption volume increased by 1.5 times or more due to the development of micropores.     

蒸汽活化生物质焦吸附模拟烟气中SO2和NO的研究

以麦秆和稻壳生物质为研究对象,在不同的热解温度、热解速率以及蒸汽活化温度条件下制备了生物质焦,采用比表面积与孔隙度分析仪测定生物质焦的比表面积和孔隙结构参数。利用固定床吸附装置,研究了热解温度、热解速率、活化温度和模拟烟气中SO₂和NO浓度等因素对生物质焦吸附SO₂和NO性能的影响。结果表明,蒸汽活化可以显著提高生物质焦的BET比表面积、D-R比表面积、D-R微孔容积和总孔容,降低其平均孔径,并显著增加蒸汽活化生物质焦对SO₂与NO吸附的起始穿透时间和吸附量。快速热解下制得的蒸汽活化焦对SO₂和NO的吸附效果优于慢速热解,热解温度为873 K的蒸汽活化焦的吸附性能明显好于热解温度为673与1 073 K的蒸汽活化焦。在973~1 173 K下,随着蒸汽活化温度的提高,蒸汽活化生物质焦对SO₂和NO的吸附量呈现先上升后下降的趋势。随着模拟烟气中SO₂与NO浓度的降低,蒸汽活化生物质焦对SO₂与NO吸附的起始穿透时间延长,但相应的SO₂和NO吸附量下降。在873 K、快速热解和1 073 K条件下制得的蒸汽活化麦秆焦对SO₂和NO吸附量最大,其值分别为109.02和21.77 mg/g。     

Comparative study for the removal of methylene blue via adsorption and photocatalytic degradation

Physically and chemically activated carbons were prepared from date pits and olive stones. Titania and WO(x)-TiO(2)/MCM-41 were prepared as photoactive catalysts. Surface characterizations were investigated from ash content, pH, base neutralization capacities and FT-IR techniques. The textural characteristics, namely specific surface area (S(BET)) and pore texture, were determined from low temperature adsorption of N(2) at 77 K. The decolorization of aqueous solution of methylene blue was performed by means of two alternative methods. Steam-activated carbons own higher surface area compared with ZnCl(2)-activated carbons, and the micropore surface area represents the major contribution of the total area. Steam-activated carbons were the most efficient decolorizing adsorbents owing to its higher surface area, total pore volume and the basic nature of the surface. The calculated values of DeltaG(0), DeltaH(0) and DeltaS(0) indicate the spontaneous behavior of adsorption. The photocatalytic degradation is more convenient method in decolorizing of methylene blue compared with the adsorption process onto activated carbons.