CO2 Adsorption of Metal Organic Framework Material

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《SBA-16及沸石改性的HKUST-1用于CO2吸附性能研究》范文

《SBA-16及沸石改性的HKUST-1用于CO2吸附性能研究》范文

《SBA-16及沸石改性的HKUST-1用于CO2吸附性能研究》篇一SBA-16及沸石改性HKUST-1在CO2吸附性能研究中的应用一、引言随着全球气候变化和环境污染问题日益严重,减少温室气体排放、特别是减少二氧化碳(CO2)的排放,已成为当今社会的重要议题。

为了应对这一挑战,研究者们正在积极寻找高效的CO2吸附材料。

其中,SBA-16及沸石改性的HKUST-1因其独特的结构和良好的吸附性能,在CO2吸附领域展现出巨大的潜力。

本文旨在探讨SBA-16及沸石改性的HKUST-1在CO2吸附性能方面的研究与应用。

二、SBA-16材料及其CO2吸附性能SBA-16是一种具有高比表面积和有序介孔结构的材料,其独特的结构使其在CO2吸附领域具有显著优势。

研究表明,SBA-16的孔径和表面化学性质对其CO2吸附性能具有重要影响。

首先,SBA-16的介孔结构提供了大量的吸附位点,有利于CO2分子的快速扩散和吸附。

此外,其高比表面积使得SBA-16具有更高的吸附容量。

通过引入亲CO2的化学基团,可以进一步增强SBA-16对CO2的吸附能力。

三、沸石改性的HKUST-1材料及其CO2吸附性能HKUST-1是一种常见的金属有机骨架(MOF)材料,具有良好的CO2吸附性能。

然而,其稳定性及循环使用性能有待提高。

通过沸石改性,可以优化HKUST-1的结构和性能,提高其CO2吸附能力及循环稳定性。

沸石改性HKUST-1的方法主要是通过将沸石的骨架结构与HKUST-1的金属离子相结合,从而增强HKUST-1的稳定性。

同时,引入沸石表面的亲CO2基团,可以提高HKUST-1对CO2的吸附能力。

此外,沸石改性还可以改善HKUST-1的孔结构和表面性质,有利于提高其循环使用性能。

四、SBA-16及沸石改性的HKUST-1在CO2吸附性能方面的比较研究通过对SBA-16及沸石改性的HKUST-1进行CO2吸附性能的比较研究,我们发现:1. SBA-16具有较高的CO2吸附容量和快速扩散性能;2. 沸石改性的HKUST-1在提高稳定性和循环使用性能方面具有优势;3. 通过结合两种材料的优点,可以进一步优化CO2吸附性能。

C02/CH4/H2中MOFs和COFs吸附分离性能的比较

C02/CH4/H2中MOFs和COFs吸附分离性能的比较

C02/CH4/H2中MOFs和COFs吸附分离性能的比较Yunhua Liu, Dahuan Liu, Qingyuan Yang, Chongli Zhong,* andJianguo MiLaboratory of Computational Chemistry, Department of ChemicalEngineering, Beijing Uni V ersity of Chemical Technology, Beijing100029, China在本文中,采用巨正蒙特卡罗法(GCMC)进行模拟研究来评估分离共价有机骨架化合物(COFs)与金属—有机骨架化合物(MOFs)对CH4 / H2 / CO2混合物进行分离的性能。

模拟结果表明, MOFs和COFs的吸附选择性很相似。

骨架电荷在COFs中的静电贡献虽然比在MOFs中的小,但仍需要被考虑。

另外,目前的研究表明,理想的吸附溶液IAST预测理论适用于大多数COFs。

1.引言:金属—有机骨架材料(Metal.Organic Frameworks。

MOFs)是混合多孔纳米材料的一份子,是由金属离子与有机配体组装而成的配位聚合物,它们在不同领域表现出了很宽广的应用前景,比如在储气方面,分离方面和催化方面等。

最近, 另一个新型的多孔材料“共价—有机骨架材料”(Covalent.Organic Frameworks.COFs) 已经出现。

COFs是由有机基团结合了氧化硼的集群共价键的新型材料。

这种材料的密度比MOFs低,同时保留了MOFs的独特特性。

比如拥有更大面积的孔隙容量,因此受到了更为广泛的关注。

目前, 在实验和理论方面,研究主要集中在COFs对纯组分的吸附等领域上, 对于采用COFs 对混合气体的分离研究是非常重要的,,在许多工业环节中对纯组分的吸附,还处于稀缺的未涉及领域。

为了达到对COFs的分离性能的研究了解,以及与MOFs有一个对比,。

配位不饱和金属-有机骨架材料吸附CO2的研究进展

配位不饱和金属-有机骨架材料吸附CO2的研究进展

2017年第36卷第5期 CHEMICAL INDUSTRY AND ENGINEERING PROGRESS·1771·化 工 进展配位不饱和金属-有机骨架材料吸附CO 2的研究进展赵倩,冯东,汪洋,赵文波(昆明理工大学化学工程学院,云南 昆明 650500)摘要:配位不饱和金属-有机骨架(MOFs )材料是一种极具潜力的小分子气体吸附分离储存材料。

本文回顾了近几年MOFs 材料在捕集CO 2领域的发展状况,对近年来研究比较集中的几种金属配位不饱和MOFs 材料进行了详细的介绍与比较,如MIL 系列、Cu-BTC 系列及MOF-74等。

该工作为系统地认识MOFs 和拓展其未来在CO 2吸附分离领域的应用提供了帮助。

本文同时也进一步指出不饱和金属配位的存在对多孔MOFs 材料的吸附性能起着重要作用。

在多孔MOFs 材料对CO 2捕集效果仍不能满足工业需求的现状下,预测合理设计MOFs 的金属配位中心且通过活化处理调控MOFs 中金属的配位状况,甚至对其孔道表面功能化修饰将是该类型材料的发展方向,并在最后从制备方法、金属中心的选择与表面改性3方面作了总结。

关键词:配位不饱和;金属-有机骨架;多孔MOFs 材料;CO 2捕集;吸附;表面改性 中图分类号:TB34 文献标志码:A 文章编号:1000–6613(2017)05–1771–11 DOI :10.16085/j.issn.1000-6613.2017.05.027Research progress of CO 2 adsorption using coordinatively unsaturatedMOFs materialsZHAO Qian ,FENG Dong ,WANG Yang ,ZHAO Wenbo(Faculty of Chemical Engineering ,Kunming University of Science and Technology ,Kunming 650500,Yunnan ,China )Abstract :MOFs are a kind of potentially ideal adsorbents with coordinative unsaturated metal sites (UMSs ). It can be used to separate and store small molecule gas. This article reviewed the development of MOFs materials in CO 2 capture in recent years. We summarized some typical coordinatively unsaturated metal-organic materials ,such as MIL series ,Cu-BTC ,MOF-74 and so on ,which are suitable for capturing CO 2. This work would help us to understand the metal-organic porous materials and expand their application in CO 2 capture in the future. At the same time ,this paper also pointed out that open metal sites play an important role on the adsorption performance of the porous MOFs materials. At present ,the efficiency of porous MOFs materials for CO 2 capture is far from the industrial requirement ,so reasonable design of MOFs metal center ,activating treatment after syntheses and the functionalized modifications on the pore channel surface would be the development directions for these type materials. At the end ,we made the conclusions from the aspect of the preparation methods ,the metal centers and surface modification.Key words :coordinatively unsaturated metal sites ;MOFs ;porous MOFs material ;CO 2 capture ;adsorption ;surface modification收稿日期:2016-08-22;修改稿日期:2017-01-12。

提高了吸收吸附二氧化碳效率 英文

提高了吸收吸附二氧化碳效率 英文

提高了吸收吸附二氧化碳效率英文The improvement of CO2 absorption and adsorption efficiency has been a hot topic in recent years due to the increasing levels of atmospheric carbon dioxide and the urgent need to reduce greenhouse gas emissions. This article will discuss the steps taken to enhance the absorption and adsorption efficiency of CO2 in various fields.Step 1: Developing New MaterialsOne way to improve CO2 absorption and adsorption efficiency is to develop new materials. Researchers have been exploring and synthesizing various materials, including zeolites, metal-organic frameworks (MOFs), carbon nanotubes, and graphene oxide. These materials have a high surface area and can effectively adsorb CO2, making them suitable candidates for CO2 capture and storage.Step 2: Optimizing Process ConditionsAnother strategy to improve CO2 absorption and adsorption efficiency is to optimize the process conditions. This involves adjusting various parameters, such as temperature, pressure, and flow rate, to maximize the amount of CO2 captured or adsorbed. For instance, researchers have used temperature swing adsorption (TSA) and pressure swing adsorption (PSA) to increase CO2 capture.Step 3: Developing Advanced TechniquesIn addition to developing new materials and optimizing process conditions, researchers have also developed advanced techniques to improve CO2 absorption and adsorption efficiency. For example, electrochemical CO2 reduction hasbeen proposed as a promising method for CO2 capture and utilization. This method involves converting CO2 into useful chemicals, such as methanol and formic acid, using renewable energy sources.Step 4: Integrating Multiple TechnologiesA more comprehensive approach to improving CO2 absorption and adsorption efficiency is to integrate multiple technologies. For example, researchers have combined absorption with membrane separation to enhance CO2 capture efficiency. This process involves using a membrane to separate the CO2 from other gases that are produced during the absorption process.In conclusion, the improvement of CO2 absorption and adsorption efficiency requires a multi-disciplinary effort, combining material science, engineering, and chemistry. By developing new materials, optimizing process conditions, developing advanced techniques, and integrating multiple technologies, we can make significant progress in reducing greenhouse gas emissions and mitigating climate change.。

CO2与环氧化物耦合制备环状碳酸酯的多相催化体系研究进展

CO2与环氧化物耦合制备环状碳酸酯的多相催化体系研究进展

化工进展Chemical Industry and Engineering Progress2024 年第 43 卷第 3 期CO 2与环氧化物耦合制备环状碳酸酯的多相催化体系研究进展刘方旺1,韩艺1,张佳佳1,步红红1,王兴鹏1,于传峰1,刘猛帅2(1 潍坊职业学院化学工程学院,山东 潍坊 262737;2 青岛科技大学化工学院,山东 青岛 266045)摘要:作为最主要的温室气体,二氧化碳(CO 2)的过度排放已导致了严重的环境问题。

同时,CO 2也属于储量丰富、廉价、安全和可再生利用的C 1资源,被认为是有机合成的理想碳材料。

高效且绿色的化学固定CO 2耦合制备具有高沸点、高极性、低挥发性和可生物降解性等优点的环状碳酸酯是CO 2资源化利用的有效方式,已引起社会各界的广泛关注。

本文首先简述了目前合成环状碳酸酯的现有反应路径。

然后,以CO 2和环氧化物的耦合反应为出发点,着重分析了该反应发生所涉及的反应机理以及催化该反应时多相催化体系的设计思路和当前研究进展。

同时,综合比较了不同多相催化体系的催化条件、催化活性及循环使用性等催化参数的优缺点。

最后,基于上述分析,本文总结了不同多相催化体系的应用前景并建议其后续发展应与均相催化体系相结合,利用两者的优势高效活化CO 2与环氧化物,以实现温和条件下催化耦合反应。

关键词:二氧化碳;催化剂;环氧化物;催化作用;耦合反应;环状碳酸酯中图分类号:TQ203.2 文献标志码:A 文章编号:1000-6613(2024)03-1252-14Research advance of heterogeneous catalytic system for the couplingbetween CO 2 and epoxide into propylene carbonateLIU Fangwang 1,HAN Yi 1,ZHANG Jiajia 1,BU Honghong 1,WANG Xingpeng 1,YU Chuanfeng 1,LIU Mengshuai 2(1 College of Chemical Engineering, Weifang Vocational College, Weifang 262737, Shandong, China; 2 College of ChemicalEngineering, Qingdao University of Science and Technology, Qingdao 266042, Shandong, China)Abstract: As the most important greenhouse gas, carbon dioxide (CO 2) has caused serious environmentalproblems by excessive emission. On the other hand, CO 2 is an abundant, cheap, safe and renewable C 1 resource, and thus is considered as an ideal carbon material in organic synthesis. Efficient and green chemical fixing CO 2 to prepare cyclic carbonate with high boiling, high polarity, low volatility and biological degradability is an effective way of CO 2 resource utilization, which has attracted wide attention. In this paper, the existing reaction pathways for the synthesis of cyclic carbonate are briefly described. Then, staring with the coupling reaction of CO 2 with epoxides, we emphatically analyze the reaction mechanism, and the design ideas and current research advance of the heterogeneous catalytic system. Meanwhile, the advantages and disadvantages of the catalytic parameters such as catalytic conditions,catalytic activity and recyclability, of different heterogeneous catalytic systems are comprehensively compared. Finally, the application and development prospects of different heterogeneous catalytic systems综述与专论DOI :10.16085/j.issn.1000-6613.2023-0351收稿日期:2023-03-08;修改稿日期:2023-06-13。

二氧化碳吸附材料

二氧化碳吸附材料

二氧化碳吸附材料二氧化碳(CO2)是一种重要的温室气体,其排放对全球气候变化产生了重大影响。

因此,寻找高效的二氧化碳吸附材料成为了当前研究的热点之一。

二氧化碳吸附材料是指能够吸附并储存二氧化碳的材料,其主要应用于二氧化碳捕获、气体分离和储存等领域。

目前,有许多种类的二氧化碳吸附材料被广泛研究和开发,包括金属有机框架(MOFs)、多孔有机聚合物(POPs)、氧化物、金属化合物等。

这些材料具有不同的结构和吸附性能,可以根据具体的应用需求进行选择和设计。

金属有机框架(MOFs)是一类由金属离子和有机配体组成的晶体材料,具有高度可调的孔隙结构和表面化学性质。

由于其高比表面积和可控的孔径大小,MOFs被认为是一种潜在的二氧化碳吸附材料。

通过调控MOFs的结构和功能化修饰,可以实现对二氧化碳的高效吸附和选择性分离。

另一类重要的二氧化碳吸附材料是多孔有机聚合物(POPs),它们由有机单体通过化学键连接而成,具有均匀的孔隙结构和可调的化学性质。

POPs具有良好的化学稳定性和可控的孔径大小,能够实现对二氧化碳的高效吸附和再生。

因此,POPs被广泛应用于二氧化碳捕获和气体分离领域。

除了MOFs和POPs,氧化物和金属化合物也被认为是潜在的二氧化碳吸附材料。

氧化物具有丰富的化学成分和结构多样性,可以通过合成和调控实现对二氧化碳的高效吸附和转化。

金属化合物具有良好的热稳定性和化学活性,能够实现对二氧化碳的高效吸附和储存。

综上所述,二氧化碳吸附材料是一类具有重要应用价值的功能材料,其研究和开发对于减缓气候变化和实现清洁能源具有重要意义。

随着对二氧化碳捕获和利用技术的不断深入,相信二氧化碳吸附材料将会迎来更广阔的发展前景。

钙钛矿—金属有机框架材料光催化还原CO2的超快动力学

钙钛矿—金属有机框架材料光催化还原CO2的超快动力学

钙钛矿—金属有机框架材料光催化还原CO2的超快动力学钙钛矿是一种具有特殊结构和性质的材料,已经被广泛应用于太阳能电池、光触媒和光电化学催化等领域。

钙钛矿材料主要由离子型晶格和有机分子框架组成,这种特殊的结构使其具有优异的光电转换和催化性能,特别是在CO2光催化还原方面显示出了巨大的潜力。

钙钛矿材料的光催化还原CO2反应机制是利用光能激发材料表面上的电荷转移过程,将CO2分子中的碳原子还原为有机化合物。

这个过程主要涉及光吸收、电荷分离、电子传输、还原反应和产物释放等步骤。

首先,当光能照射到钙钛矿材料上时,光子被吸收并产生激子(电子-空穴对),其中电子会被激发到较高的能级,而空穴则停留在价带中。

随后,在材料表面或界面附近,电子和空穴会发生分离,形成电流,进而引发光生电子传导。

这些光生电子可以通过导电材料传输到电极上,为催化反应提供电子。

接下来,导电材料表面的光生电子会与CO2分子中的碳原子发生电子转移反应,将CO2还原为有机物(如甲醇)。

这个过程需要光生电子具有足够的能量和合适的位置,以及合适的反应位点。

钙钛矿材料通常具有宽禁带和较高的电子迁移率,因此有利于光生电子的形成和传输。

此外,钙钛矿材料的光催化还原CO2的超快动力学也与光吸收性能有关。

钙钛矿材料对光子的吸收能力通常取决于其光学性质、吸收系数和光照强度等因素。

光子的吸收能力越强,光生电子的数量就越多,从而催化反应的速度也越快。

钙钛矿材料通常具有高的吸光度和良好的光吸收性能,因此能够有效利用可见光和红外光等大部分光谱范围内的能量。

总之,钙钛矿材料作为一种具有特殊结构和性质的金属有机框架材料,展现出了优异的光催化还原CO2性能。

其超快动力学与光吸收、电荷分离、电子传输和反应机制密切相关。

这种材料未来有望在环境保护和能源转化等领域发挥重要作用,为实现CO2的高效转化和利用提供有力支撑。

Adsorption of CO2, CH4, and N2 on Gas Diameter Grade Ion-Exchange Small Pore Zeolites

Adsorption of CO2, CH4, and N2 on Gas Diameter Grade Ion-Exchange Small Pore Zeolites

Adsorption of CO 2,CH 4,and N 2on Gas Diameter Grade Ion-Exchange Small Pore ZeolitesJiangfeng Yang,Qiang Zhao,Hong Xu,Libo Li,Jinxiang Dong,and Jinping Li *Research Institute of Special Chemicals,Taiyuan University of Technology,Taiyuan 030024,Shanxi,P.R.Chinastructure like CO 2.From the viewpoint of the equilibrium selectivity for CO 2and N 2or CO 2andof CO 2;K-zeolites with high S CO 2/N 2and S CH 4/N 2,adsorption potential order was K-zeolites >Na-zeolites >The removal of CO 2from gaseous mixtures is important for CO 2capture from flue gas,biogas,or land fill gases.These sources of natural gas mainly contain CH 4,CO 2,and N 2.Therefore,the separation of CO 2,CH 4and N 2mixtures canupgrade low quality natural energy gas and also mitigate the problem of excess CO 2emissions.1Of the available adsorption-based separation processes,energy (CH 4)and CO2capture isconsidered to be an energy-and cost-e fficient alternative.Thus,adsorption is an important solution for separation,CO 2capture,CH 4storage,and transportation.2−4This approach uses various types of sorbents or adsorption materials such as carbon materials (activated carbon and carbon molecular sieves),5,6molecular sieves (zeolites),7−10and the popular new metal −organic frameworks (MOFs).11−14Sorbents are considered to be the most important factors a ffecting adsorption techniques.A comparison of di fferent adsorption materials showed that carbon materials are di fficult to have a balance of small pores and large pores,for optimum balance between capacity and dynamics,and MOFs had lower thermal stability,but zeolites produced very homogeneous structures with high surface area and good thermal stability,and the size of the pore volume could be modulated.15,16Thus,zeolites are the most commonly used adsorbents in the field,such as LTA structures (4A,5A,and 13X).17The question is how do we choose appropriate zeolites for a speci fic application such as CO 2,CH 4,and N 2adsorption and First,an analysis of gases showed that nonpolar gases have very similar diameters and gas dynamics:CO 2=0.33nm,CH 4=0.38nm,and N 2=0.36nm,18while the adsorptionstrength of the sorbents was CO2>CH4>N2.19,20Therefore,the adsorption and separation of most gases by zeolites isreliant on their surface potential or the balance of ions in surface channels,particularly the low silicon Li-X zeolite usedfor O 2and N 2separation.21The pore diameters of zeolites areusually bigger than the gas molecules,so gases can di ffusethrough these pores.But what would happen if the pores had a similar size to or smaller than the molecular diameter of the three gases during zeolite adsorption?Titanium silicalite ETS-4had a pore size that is similar to the molecular diameter,and it can be modulated by temperature changes for the aperture separation of various gases,such as CO 2and CH 4,N 2,and CH 4,although its lower adsorptioncapacity limits theapplication of this approach.22−24The ori fice diameters of the zeolites,KFI,CHA,and LEV,are very close to the kinetic diameters of CO 2,CH 4,and N2(Figure 1).These three small-pore zeolites have cage-like structures,and the larger cavity in the hole is ideal for gas uptake.This type of small-pore size microporous zeolite is a hot research area in the field of catalysis and adsorption.25−27Received:August 28,2012Accepted:October 31,2012Published:November 7,2012Krishna and van Baten found frequent correlation e ffects with cage-type zeolites,such as LTA,CHA,and DDR,where narrow windows separated the cages.26Webley et al.studied the gas adsorption selectivity of M(Ca,K)-CHA and concluded that the high O 2/Ar selectivity was possibly due to partial pore blockage by a large K +located near the 8-member ring,producing a 20-hedron cage.28The small pore size and the metal cation balance probably plays an important role in the gas diameter grade structure of zeolites where it determines the adsorption capacity and shape-selective catalysis.It is less common to focus on these types of small pore size cage-like structures and the adsorption of gas molecules close to the aperture.In this study,we synthesized three types of zeolites,Na-LEV,K-CHA,and K-KFI,using the hydrothermal method,whereas Na-KFI,Li-KFI,Ca-KFI,Na-CHA,Li-CHA,and Ca-CHA were obtained by ion exchange.The aims of this study were to evaluate the pore size e ffect and the metal cation e ffect on the adsorption of CO 2,CH 4,and N 2.We also discuss the most suitable method for the separation of CO 2,CH 4,and N 2based on calculations of the adsorption equilibrium.■MATERIALS AND METHODSThe chemicals used in this study are described in more detail in Table 1.Partial Aluminum Potassium.[50.00g of water +29.76g of potassium hydroxide +15.80g of alumina]were heated to boiling until clear,cooled to room temperature,and corrected for any weight loss due to boiling.30,31K-KFI.The synthesis following the procedure reported by Johannes et al.30−32The batch composition was:7.2partial aluminum potassium/0.1strontium nitrate/7.5silicon dioxide/130water,and the typical procedure involved mixing the required amounts of partial aluminum potassium and water,followed by the addition of silica sol,and mixing until smooth (approximately 10min),before strontium nitrate was added to the mixture and stirred for 10min.The resulting mixture was transferred into a 23mL Te flon-lined autoclave and heated in an oven for 5days at 423K.After cooling to ambient temperature,the product was filtered,washed with water,and dried at 373K.The crystal structure of KFI and the degree of crystallinity were con firmed by powder X-ray di ffraction(XRD).Figure 1.Structures of zeolites KFI (a),CHA (b),and LEV (c).29Table 1.Purity of Chemicals Used in This Study and Their Detailschemical name source initial mass fraction purityalumina Aladdin,China >0.99silica sol QingdaoHaiyang Chemical Co.,Ltd.0.401,1-dimethylpiperidinium chloride Shanghai Bangcheng Chemical Co.,Ltd.0.98strontium nitrate Aladdin,China >0.99potassium hydroxide TianjinKemiou Chemical Reagent Co.,Ltd.0.82sodium hydroxide TianjinKemiou Chemical Reagent Co.,Ltd.0.96sodium chloride TianjinKemiou Chemical Reagent Co.,Ltd.0.99lithium hydroxide Tianjin Kemiou Chemical Reagent Co.,Ltd.0.98lithium chloride TianjinKemiou Chemical Reagent Co.,Ltd.0.97calcium hydroxide TianjinKemiou Chemical Reagent Co.,Ltd.0.95calcium chloride Tianjin Kemiou Chemical Reagent Co.,Ltd.0.96K-CHA.The synthesis method was similar to that for K-KFI,but the batch composition was:7.2partial aluminum potassium:0.1strontium nitrate:6silicon dioxide/130water,so there were lower levels of Si/Al.The crystal structure of CHA and the degree of crystallinity were con firmed by powder XRD.Na-LEV.This was prepared from:6partial aluminum sodium/10silicon dioxide/31,1-dimethylpiperidinium chlor-ide/200H 2O,which was made according to our previously reported method.33Ion Exchange.The Na-KFI described above was converted from its potassium form (K-KFI)via three consecutive ion exchanges.In general,300mL of 1M sodium chloride at pH =9(adjusted with 0.01M sodium hydroxide)was added to 5g of zeolite,and the solution was heated to 363K and stirred for 12h.The solution was decanted,and fresh solution was added.After successive washes with the requisite solution,the resulting zeolite was vacuum-filtered and washed with 500mL of deionized water.The zeolite was dried at 373K for 24h.Li-KFI was prepared from Na-KFI by five consecutive ion exchanges of Na-KFI with 2M lithium chloride (5g of zeolite:300mL of lithium chloride)at pH =9(adjusted with 0.01M lithium hydroxide).Ca-KFI was prepared from Na-KFI by five consecutive ion exchanges of Na-KFI with 1M calcium chloride (1g of zeolite:300mL of calcium chloride).The solution was heated at 353K for 12h and decanted,and fresh solution was added.This procedure was repeated five times.Finally,the Ca-KFI was filtered and washed with copious amounts of deionized water and dried at 373K overnight.Na-CHA,Li-CHA,and Ca-CHA,were prepared using the same procedure.34Characterization.The crystallinity and phase purity of the molecular sieves were measured by powder XRD using a Rigaku Mini Flex II X-ray di ffractometer with Cu K αradiation operated at 30kV and 15mA.The scanning range was from 5to 40°(2theta)at 1°/min.Morphological data were acquired by scanning electron microscopy (SEM)using a JEOL JSM-6700F scanning electron microscope operated at 15.0kV.The samples were coated with gold to increase their conductivity before scanning.The Si/Al ratio and the metal ion content of the zeolites were determined by elemental analysis using a spectrophotometer-723P.High-Pressure Gas Adsorption Measurements.The purity of the carbon dioxide was 99.999%,methane was 99.95%,and nitrogen was 99.99%.The adsorption isotherms were measured under high pressure using an Intelligent Gravimetric Analyzer (IGA 001,Hiden,UK).Before measuring the isotherm,a 50mg sample was predried under reduced pressure and then outgassed overnight at 673K under a high vacuum until no further weight loss was observed.Each adsorption/desorption step was allowed to approach equilibrium over a period of 20−30min,and all of the isotherms for each gas were measuredusing a single sample.■RESULTS AND DISCUSSION Synthesis,Ion Exchange,and Characterization.The zeolite K-KFI was synthesized according to a published method.32Figure 2a shows the XRD pattern of the synthesized molecular sieve K-KFI compared with the standard XRD data for the molecular sieve KFI.The peak positions and relative di ffraction intensity were similar to the reported values,which demonstrated that the molecular sieve K-KFI had been synthesized.Figure 2a also shows the XRD pattern of the molecular sieve K-KFI,which was calcined from (573to 1073)K.Its peak positions and relative di ffraction intensity were the same as a sample synthesized below 973K,while the skeleton collapse temperature was 1073K.The method used for the synthesis of K-CHA was similar to that used for K-KFI.Figure 2b shows the XRD pattern of the synthesized molecular sieve K-CHA compared with the standard XRD data for the molecular sieve CHA.The peak positions and relative di ffraction intensity were similar to the reported values,which demonstrated that the molecular sieve K-CHA had been synthesized.The samples had similar behavior at below 973K,while the skeleton collapse temperature was 1073K.The data showed that the structures of KFI and CHA had good thermal stability.The Si/Al values in K-KFI and K-CHA were 4.59and 2.63,respectively.The low Si/Al value indicated that K +occupied more channels in the zeolites,where the large space allowed access to small metal ions or divalent ion exchange.In addition,K-CHA with a lower Si/Al value indicated that more ions could be exchanged,while the size of the pore space could change greatly.However,the higher Si/Al value of K-KFI indicated lower ion exchange,so the size of the pore space could be regulated at a finer level.Table 2shows the experimental K-zeolites,which were changed to Na-zeolites via ion exchange,and the uncertainty is within ±0.005.This shows that the ion exchange degree was increased with temperature and frequency.K-CHA with a lower Si/Al value was produced more completely and easier than K-KFI with a higher Si/Al value from Na +exchanged with K +.The ion exchange degree of Na-CHA from K-CHA wasveryFigure 2.XRD patterns of KFI (a)and CHA (b).high in the first cycle,because the higher temperature is helpful to ion exchange in low Si/Al zeolites.35We selected the highest exchange degree for K +(Na-KFI with 0.91and Na-CHA with 0.99)and the Na-zeolites were used to obtain Li-zeolites and Ca-zeolites.Table 3shows that Li-KFI and Ca-KFI were 0.96and 0.83,respectively,based on Li +and Ca 2+exchange for Na +,while Li-CHA and Ca-CHA were 0.92and 0.96,respectively.The XRD patterns of the Na-,Li-,and Ca-zeolites showed that the zeolite structures were highly stable throughout ion exchange (Figure 3).The samples that changed in appearance are shown in Figure 4.The morphologies of the zeolites with KFI and CHA structures were observed by SEM.For K-KFI to Na-KFI,Li-KFI,and Ca-KFI,the morphologies of the crystals changed from regular cubic accumulations until they completely lost their regular structures.We also showed that there was a slight change in their appearance after a single exchange of materials,followed by a more obvious change after the secondary exchange of materials,particularly M 2+exchange with M +based on the morphologies of M-CHA (M-metal).The pore diameter of some of the samples was too small to be measured or analyzed using a liquid nitrogen adsorption isotherm,for LEV with the ori fice very close to the nitrogen-diameter,so the surfaces of all samples were measured andanalyzed using a CO 2adsorption isotherm at 273K (Figure 5).The microporous surface area and microporous volumes werecalculated using the Dubinin −Radushkevitch (D-R)equation(Table 4):β=−··⎡⎣⎢⎤⎦⎥V V B T PP log()log()log0202(1)where V was volume adsorbed at equilibrium pressure;V 0was the micropore capacity;P 0was saturation vapor pressure of gas attemperature T ;P was equilibrium pressure;B was a constant,βwasthe a ffinity coe fficient of analysis gas relative to P 0gas (for this application βis taken to be 1);T was the analysis bath temperature.36−38All of the samples with a high surface area could be used foradsorption;the surfaces and the pore volumes of the zeoliteswere changed very obvious by ion exchange.Table 4shows thesurface of the samples where the greatest changes were in theappearance of the M-CHAs with the lowest surface areas (K-CHA with 278.5m 2·g −1)and the highest (Li-CHA with 638m 2·g −1,the same situation also appear in the pore volumechange (K-CHA with 0.07cm 3·g −1and Li-KFI with 0.17cm 3·g −1).because they had lower Si/Al values and morebalanced metal ions could be exchanged,so with the smallersize of Li +instead of K +(Table 3),more space can be obtained.However,M-KFI had a higher Si/Al value than M-CHA,so the area of its surface and microporous volume that could be regulated by ion exchange was smaller;that is,the surface area ranges from 333.5m 2·g −1(Ca-KFI)to 566.2m 2·g −1(Na-KFI),and the pore volume ranges from 0.07cm 3·g −1(Ca-KFI)to 0.15cm 3·g −1(Na-KFI).We also found that the surfaces and pore volumes of Ca-zeolites were smaller than Li-or Na-zeolites,which showed that the introduction of Ca 2+reduced the number of balanced ions,while the plug was very strong because the size of Ca 2+larger than Li +and Na +.Li-KFI and Na-KFI had similar surfaces,so it was inferred from Li +that there was no hole in Na-KFI to produce major changes.The systematic errors of surface areas and pore volume have been estimated to be less than 5m 2·g −1and 0.01cm 3·g −1.Table 2.Ion Exchange Degree from K-Zeolite to Na-Zeolite at Di fferent Exchange Times and Temperatures of (323and 363)K a 0.5870.7570.8800.910363Na-CHA 0.7500.7640.9240.9343230.9240.9710.9740.991363a Uncertainties are:U (exchange degree)=0.005;U (T )=0.1K.Table 3.Ion Exchange Degree of Li and Ca-Zeolite from Na-Zeolite a zeolites cation ionic radius (nm)Na +per unit cell (wt %)exchange degree for Na +K-KFI 0.133Na-KFI 0.095 5.29Li-KFI 0.0680.200.96Ca-KFI 0.0990.900.83K-CHA 0.133Na-CHA 0.0957.94Li-CHA 0.0680.640.92Ca-CHA 0.0990.290.96a Uncertainties are:U (Na +contents)=0.02wt %;U (exchange degree)=0.005.Figure 3.XRD patterns of Na,Li,and Ca-KFI (a)and Na,Li,and Ca-CHA (b).Gas Sorption Isotherm Measurements.The CO 2,CH 4,and N 2adsorption and desorption isotherms of the samples are shown in Figure 6,where all of the isotherms have a Langmuir I form and the relative uncertainties of adsorption volumes are estimated to be 0.05V .Most of the samples exhibited rapid desorption,and this correlated with their adsorption curve.Only sample K-CHA exhibited desorption hysteresis during CH 4adsorption.We inferred that the pore size of K-CHA was too close to the kinetics of the di ffusion diameter of CH 4,so it had a very strong CH 4adsorption potential,whereas desorption was hindered by the steric e ffect of the micropores.Table 5also shows the orders of the volumes for CO 2,CH 4,and N 2adsorption of the samples at 0.1MPa.The order of CO 2adsorption at 298K corresponded to the surfaces of the samples.Based on the CO2adsorption,we can also determine the zeolites with Li +and Na +exchange with bigger surfaces and greater adsorption volumes.Based on the high levels (>100cm 3·g −1)of CO 2adsorption with Li,Na-KFI,and Li,Na-CHA at high pressurea,we conclude that micropore Li-zeolites and Na-zeolites could be used for CO 2capture and storage (CCS).The smallest CH 4adsorption volume was found with Na-LEV,so we inferred that CH4adsorption would not occur in itsmicropores because the levels were far less than with othersamples.We conclude that CH4could not di ffuse through theholes in Na-LEV because the ori fice diameter (0.36×0.48nm)was too small.The CH 4adsorption results showed thatM-Figure 4.SEM of the samples:(a)K-KFI,(b)Na-KFI,(c)Li-KFI,(d)Ca-KFI,(e)K-CHA,(f)Na-CHA,(g)Li-CHA,(h)Ca-CHA.CHA was better than M-KFI,so CH 4adsorption or storage was based on the surface features and the ori fice diameter (CHA with 0.38×0.38nm,KFI with 0.39×0.39nm),which indicated a higher adsorption potential.39The low N 2adsorption with Na-LEV shows that molecules could not di ffuse through its pores.N 2adsorption was not a ffected by the metal ion or the structure,so the pore size or surfaces of porous materials were always su fficient for liquid nitrogen adsorption.In the other samples,the N 2adsorption results showed that the pores were expanded by small metal ions or divalent ion exchange,that is,twice then once,because the order was Li,Ca-zeolite >Na-zeolite >K-zeolite (Table 5).Adsorption Equilibrium Selectivity.To evaluate the adsorption equilibrium selectivity and predict the adsorption of the gas mixture from the pure component isotherms,the adsorbent selection parameter S i /j is de fined in the following equation:=ΔΔS qq a i j i j /12/(2)where Δq 1and Δq 2are the adsorption equilibrium capacity di fferences at the adsorption pressure and desorption pressure for components 1and 2.The adsorption equilibrium selectivity a i /j between components i and j is de fined as follows:==a K K q b q b i j i j mi imj j /(3)Henry ’s law:=q Kp (4)Langmuir isotherm model:=+q q bpbp 1m (5)where q m and b are Langmuir isotherm equation parameters,which can be determined from the slope and intercept of a linear Langmuir plot of (1/q )versus (1/p )where q m i and q m jand b i and b j are the Langmuir equation constants for components i and j ,respectively.The equilibrium selectivity de fined in the above equation is basically the ratio of Henry ’s constants for the two components.40Based on the results for S CO 2/CH 4and S CO 2/N 2(in Table 6andthe relative uncertainties of S i /j are estimated to be 0.05S ),all ofthe micropore zeolites produced excellent results in the evaluations,because of the high adsorption of CO 2in the gas diameter grade micropore structures.Na-LEV was the bestmicroporous sieve for gas materials with the highest S CO 2/CH 4=137and S CO 2/N 2=934due to the almost total nonadsorption ofCH 4and N 2but high adsorption of CO 2,which is rare among sorbents.41The second best was Na-KFI (S CO 2/CH 4=92andS CO 2/N 2=374),which had produced better results than otherM-KFIs.In addition,Na-CHA had a higher SCO 2/CH 4than K andLi-CHA,and at the same time Na-CHA also had a higher S CO 2/N 2than Li,Ca-CHA,so we can conclude that Na-zeoliteshad higher CO 2adsorption.A reanalysis of the data showed that Li-zeolites were followed by Na-zeolite,so the e ffects of the smaller Li +were lower than the e ffects of the bigger Na +,and we inferred that the size of the metal ions was an important impact in zeolites.The aerodynamic diameter and physicochemical propertiesof CH 4and N 2were very similar,so separating CH4and N 2wasmuch more di fficult than CO 2and CH4or CO 2and N 2separation which used an adsorption technique.The exper-imental data for S CH 4/N 2in Table 6also con firmed this point.K-CHA had the highest S CH 4/N 2=14.5,while the second was K-KFI (S CH 4/N 2=8.5),which indicated that the introduction of alarge K +increased the potential adsorption of CH4.The Na-zeolites and Li-zeolites have very low data for S CH 4/N 2.Based on the relatively good K-zeolite data for S CO 2/N 2and the smallersurface pores,we can conclude that K +had a signi ficant role in the adsorption of CH4and CO 2,although a smaller hole did not allow greater nitrogen di ffusion.From the perspective of the adsorption potential,we conclude that the large K +was better than Na +and the small Li +;the order was K-zeolites >Na-zeolites >Li-zeolites,indicating that bigger ions had a stronger a ffinity.While the introduction of divalent ions could halve the total number of ions,thus,Ca 2+formed fewer of these small pore type zeolites,and it did not produce very good resultsfor adsorption separation.■CONCLUSION We prepared nine di fferent surfaces of gas diameter grade small pore zeolites,which were characterized by XRD,SEM,and elemental analysis.We synthesized K-CHA with a lower Si/Al value,and more balanced metal ions could be exchanged,so the surfaces and microporous volumes were changedgreatly.Figure 5.CO 2adsorption of the samples on 273K.Table 4.Microporous Surface (MS)and Microporous Volume (MV)of the Samples Obtained from CO 2Adsorption Isotherms at 273K a K-KFI 430.40.10Na-KFI 566.20.15Li-KFI 550.60.14Ca-KFI 333.50.07K-CHA 278.50.07Na-CHA 594.80.16Li-CHA 638.00.17Ca-CHA 487.20.12a Uncertainties are:U (MS)=5m 2·g −1;U (MV)=0.01cm 3·g −1.However,K-KFI had a higher Si/Al value,and the area of its surface and microporous volumes could be modulated to make it smaller.We focused on the CO 2,CH 4,and N 2adsorption isotherms of the samples under high pressure (1MPa)at room temperature (298K),and we found that the smaller Li +and Na +exchanged more with the surface and they had higher adsorption volumes,whereas the larger K +led to severe channel congestion.We calculated and evaluated the adsorption equilibrium selectivity of CO 2/CH 4/N 2,which showed that the ori fice diameter had a very important role in the sieving of CO 2and N 2or CO 2and CH 4,where Na-LEV produced the best sieving e ffect.From the viewpoint of the adsorption equilibria,the Na-zeolites produced the best results for adsorption equilibrium selectivity with CO 2and N 2or CO 2and CH 4,followed by Li-zeolites,whereasK-zeolites withhigh Figure 6.CO 2(▲),CH 4(■),and N 2(●)adsorption (solid)and desorption (hollow)isotherm of the samples at 298K and 1MPa:(a)K-KFI,(b)K-CHA,(C)Na-LEV,(d)Na-KFI,(e)Li-KFI,(f)Ca-KFI,(g)Na-CHA,(h)Li-CHA,(i)Ca-CHA.Table 5.Volumes of CO 2,CH 4,and N 2Adsorption on the Samples at 0.1MPa a K-KFI 67.317.57.1Na-KFI 93.617.79.5Li-KFI 88.315.99.3Ca-KFI 54.816.29.5K-CHA 47.119.1 5.5Na-CHA 104.330.316.7Li-CHA 106.633.016.9Ca-CHA 83.221.418.7a The relative uncertainties of adsorption volumes are estimated to be 0.05V .Table 6.Separation Factor of CH 4/N 2,CO 2/CH 4,and CO 2/N 2Calculated from Pure Component Adsorption Isothermsof the Samplesa zeolite S CO 2/CH 4S CO 2/N 2S CH 4/N 2Na-LEV 137934 6.8K-KFI 353038.5Na-KFI 92374 4.1Li-KFI 80237 3.0Ca-KFI 1959 3.0K-CHA 2435214.5Na-CHA 42187 4.3Li-CHA 32154 4.7Ca-CHA 51127 1.6a The relative uncertainties of Si /j are estimated to be 0.05S .S CH 4/N 2and S CO 2/N 2.Based on the adsorption equilibrium selectivity results,we can conclude that the adsorption potential order was K-zeolites >Na-zeolites >Li-zeolites,so the bigger ions had a stronger a ffinity.Divalent ions were less likely to be captured in the structures than univalent ions,so their separation was somewhat poorer.■AUTHOR INFORMATION Corresponding Author *E-mail:Jpli211@.Tel.:86-3516010908.Fax:86-3516010908.Funding We gratefully acknowledge financial support from the National Natural Science Foundation of China (Nos.21136007,51002103)and Research Fund for the Doctoral Program of Higher Education of China (No.20091402110006).This work was financially supported by the program for the Top Science and Technology Innovation Teams of Higher Learning Institutions of Shanxi.Notes The authors declare no competing financial interest.■REFERENCES (1)Kikkinides,E.S.;Yang,R.T.;Cho,S.H.Concentration and recovery of CO 2from flue gas by pressure swing adsorption.Ind.Eng.Chem.Res.1993,32,2714−2720.(2)Hao,G.P.;Li,W.C.;Qian,D.;Wang,G.H.;Zhang,W.P.;Zhang,T.;Wang,A.Q.;Schu t h,F.;Bongard,H.J.;Lu,A.H.Structurally Designed Synthesis of Mechanically Stable Poly-(benzoxazine-co-resol)-Based Porous Carbon Monoliths and TheirApplication as High-Performance CO 2Capture Sorbents.J.Am.Chem.Soc.2011,133,11378−11388.(3)Matranga,K.R.;Myers,A.I.;Glandt,E.D.Storage of natural gas by adsorption on activated carbon.Chem.Eng.Sci.1992,47,1569−1579.(4)Matranga,K.R.;Stella,A.;Myers,A.L.;Glandt,E.D.Molecular simulation of adsorbed natural gas.Sep.Sci.Technol.1992,27,1825−1836.(5)Liu,Y.;Wilcox,J.Effects of Surface Heterogeneity on the Adsorption ofCO 2in Microporous Carbons.Environ.Sci.Technol.2012,46,1940−1947.(6)Chen,J.;Loo,L.S.;Wang,K.An Ideal Absorbed Solution Theory (IAST)Study of Adsorption Equilibria of Binary Mixtures ofMethane and Ethane on a Templated Carbon.J.Chem.Eng.Data 2011,56,1209−1212.(7)Ducrot-Boisgontier,C.;Parmentier,J.;Faour,A.;Patarin,J.;Pirngruber,G.D.FAU-Type Zeolite Nanocasted Carbon Replicas for CO 2Adsorption and Hydrogen Purification.Energy Fuels 2010,24,3595−3602.(8)Jayaraman,A.;Hernandez-Maldonado,A.J.;Yang,R.T.;Chinn,D.;Munson,C.L.;Mohr,D.H.;Donald,H.Clinoptilolites for nitrogen/methane separation.Chem.Eng.Sci.2004,59,2407−2417.(9)Wang,Y.;LeVan,M.D.Adsorption Equilibrium of BinaryMixtures of Carbon Dioxide and Water Vapor on Zeolites 5A and 13X.J.Chem.Eng.Data 2010,55,3189−3195.(10)Bao,Z.;Yu,L.;Dou,T.;Gong,Y.;Zhang,Q.;Ren,Q.;Lu,X.;Deng,S.Adsorption Equilibria of CO 2,CH 4,N 2,O 2,and Ar on High Silica Zeolites.J.Chem.Eng.Data 2011,56,4017−4023.(11)Coudert,F.O.-X.;Mellot-Draznieks,C.;Fuchs,A.H.;Boutin,A.Prediction of Breathing and Gate Opening Transitions Upon Binary Mixture Adsorptionin Metal −Organic Frameworks.J.Am.Chem.Soc.2009,131,11329−11331.(12)Zheng,S.T.;Bu,J.T.;Li,Y.;Wu,T.;Zuo,F.;Feng,P.;Bu,X.Pore Space Partition and Charge Separation in Cage-within-Cage Indium −Organic Frameworks with High CO 2Uptake.J.Am.Chem.Soc.2010,132,17062−17064.(13)He,Y.;Xiang,S.;Chen,B.A Microporous Hydrogen-BondedOrganic Framework for Highly Selective C 2H 2/C 2H 4Separation at Ambient Temperature.J.Am.Chem.Soc.2011,133,14570−14573.(14)Sumida,K.;Rogow,D.L.;Mason,J.A.;McDonald,T.M.;Bloch,E.D.;Herm,Z.R.;Bae,T.H.;Long,J.R.Carbon Dioxide Capture in Metal −Organic Frameworks.Chem.Rev.2012,112,724−781.(15)Gemma,L.H.;Edward,B.;Martin,C.S.;Neil,C.H.;Ewan,M.M.;Paul,F.M.;Joseph,A.H.High-Pressure and Temperature IonExchange of Aluminosilicate and Gallosilicate Natrolite.J.Am.Chem.Soc.2011,133,13883−13885.(16)Aguilar-Armenta,G.;Hernandez-Ramirez,G.;Flores-Loyola,E.;Ugarte-Castaneda, A.;Silva-Gonzalez,R.;Tabares-Munoz, C.;Jimenez-Lopez,A.;Rodriguez-Castellon,E.Adsorption Kinetics of CO 2,O 2,N 2,and CH 4in Cation-Exchanged Clinoptilolite.J.Phys.Chem.B 2001,105,1313−1319.(17)Walton,K.S.;Abney,M.B.;LeVan,D.M.CO 2adsorption in Yand X zeolites modified by alkali metal cation exchange.Microporous Mesoporous Mater.2006,91,78−84.(18)Yang,R.T.Adsorbents:Fundamentals and Applications ;Wiley-Interscience:New York,2003.(19)Van den Bergh,J.;Mittelmeijer-Hazeleger,M.;Kapteijn,F.Modeling Permeation of CO 2/CH 4,N 2/CH 4,and CO 2/Air Mixturesacross a DD3R Zeolite Membrane.J.Phys.Chem.C 2010,114,9379−9389.(20)Dunne,J.A.;Mariwala,R.;Rao,M.;Sircar,S.;Gorte,R.J.;Myers, A.L.Calorimetric Heats of Adsorption and Adsorption Isotherms.1.O 2,N 2,Ar,CO 2,CH 4,C 2H 6,and SF6on Silicalite.Langmuir 1996,12,5888−5895.(21)Baksh,M.S.A.;Kikkinde,E.S.;Yang,R.T.Lithium Type XZeolite as a Superior for Air Separation.Sep.Sci.Technol.1992,27,277−294.(22)Kuznicki,S.M.;Bell,V.A.;Nair,S.;Hillhouse,H.W.;Jacubinas,R.M.;Braunbarth,C.M.;Toby,B.H.;Tsapatsis,M.A titanosilicatemolecular sieve with adjustable pores for size-selective adsorption ofmolecules.Nature 2001,412,720−724.(23)Marathe,R.P.;Farooq,S.;Srinivasan,M.P.Modeling GasAdsorption and Transport in Small-Pore Titanium ngmuir2005,21,4532−4546.(24)Pillai,R.S.;Peter,S.A.;Jasra,R.V.Adsorption of carbondioxide,methane,nitrogen,oxygen and argon in NaETS-4.Micro-porous Mesoporous Mater.2008,113,268−276.(25)Altwasser,S.;Welker,C.;Traa,Y.;Weitkamp,J.Catalyticcracking of n-octane on small-pore zeolites.Microporous MesoporousMater.2005,83,345−356.(26)Krishna,R.;van Baten,J.M.Onsager coefficients for binary mixture diffusion in nanopores.Chem.Eng.Sci.2008,63,3120−3140.(27)Saxton,C.G.;Kruth,A.;Castro,M.;Wright,P.A.;Howe,R.F.Xenon adsorption in synthetic chabazite zeolites.Microporous Mesoporous Mater.2010,129,68−73.(28)Singh,R.K.Adsorption of N 2,O 2,and Ar in PotassiumChabazite.Adsorption 2005,11,173−177.(29)Baerlocher,Ch.;McCusker,L.B.;Olson,D.H.Atlas of Zeolite Framework Types ,6th revised ed.;Elsevier:New York,2007.(30)Johannes,V.Zeolite ZK-5.U.S.Patent US4994249,1991(31)Robson,H.How to read a patent.Microporous Mesoporous Mater.1998,22,551−662.(32)Schwarz,S.;Corbin,D.R.;Sonnichsen,G.C.The effect ofcrystal size on the methylamines synthesis performance of ZK-5zeolites.Microporous Mesoporous Mater.1998,22,409−418.(33)Dong,J.;Wang,X.;Xu,H.;Zhao,Q.;Li,J.Hydrogen storage inseveral microporous zeolites.Int.J.Hydrogen Energy 2007,32,4998−5004.(34)Zhang,J.;Singh,R.;Webley,P.A.Alkali and alkaline-earthcation exchanged chabazite zeolites for adsorption based CO2capture.Microporous Mesoporous Mater.2008,111,478−487.(35)Xu,R.;Pang,W.Chemistry-Zeolites and Porous Materials(Chinese);Science Press:Beijing,2004.。

金属有机骨架材料吸附去除环境污染物的进展

金属有机骨架材料吸附去除环境污染物的进展

CHEMICAL INDUSTRY AND ENGINEERING PROGRESS 2016年第35卷第2期·586·化 工 进 展金属有机骨架材料吸附去除环境污染物的进展李小娟1,2,何长发1,黄斌1,林振宇2,刘以凡1,2,林春香1,2(1福州大学环境与资源学院,福建 福州 350116;2福州大学化学学院能源与环境光催化国家重点实验室,福建 福州 350002)摘要:金属有机骨架材料(MOFs )具有超高的比表面积、较高且可调的孔隙率、结构组成多样性、开放的金属位点和化学可修饰等优点,近年来在选择性吸附领域中的应用受到人们的广泛关注。

本文综述了MOFs 在液相吸附去除各种环境污染物方面的应用进展,包括吸附去除水中的有机污染物、重金属离子以及吸附去除燃油中的有机含硫化合物和有机含氮化合物;讨论了不同MOFs 及改性MOFs 对环境污染物的吸附性能及吸附机理,指出MOFs 的孔结构、开放的金属位点、静电吸附作用、π-π键合作用、氢键作用、酸碱吸附作用等是影响MOFs 吸附过程的重要参数或机理,而通过对MOFs 进行有目的的功能化改性可以提升MOFs 对目标污染物的吸附性能;最后展望了MOFs 吸附去除环境污染物今后的研究热点。

关键词:金属有机骨架材料;环境污染物;吸附中图分类号:TB 383 文献标志码:A 文章编号:1000–6613(2016)02–0586–09 DOI :10.16085/j.issn.1000-6613.2016.02.039Progress in the applications of metal-organic frameworks in adsorptionremoval of hazardous materialsLI Xiaojuan1,2,HE Changfa 1,HUANG Bin 1,LIN Zhenyu 2,LIU Yifan 1,LIN Chunxiang1(1College of Environment and Resources ,Fuzhou University ,Fuzhou 350116,Fujian ,China ;2State Key Laboratoryof Photocatalysis on Energy and Environment ,College of Chemistry ,Fuzhou University ,Fuzhou 350002,Fujian ,China )Abstract :Due to the high specific surface area ,high/tunable porosity ,controllable structure ,open metal sites and the possibility to functionalize ,metal organic frameworks (MOFs) as promising adsorption materials have attracted considerable attention in recent decade. This critical review focuses on the progress in the applications of MOFs in adsorption removal of organic pollutants/heavy metal ion from wastewater and sulfur-containing compounds (SCCs)/nitrogen-containing compounds (NCCs) from fuel. The adsorption properties of MOFs for different hazardous materials and adsorption mechanism were discussed. It was demonstrated that the porosity ,pore size and the central metal ions was important for the adsorption ,which was found to proceed through a number of different mechanisms such as electrostatic interactions ,π-π stacking/interactions ,acid-base interactions and hydrogen bonding. The adsorption properties can be promoted by the functional modification of MOFs. The research trend in the future was also prospected.Key words :metal-organic frameworks; hazardous materials; adsorption收稿日期:2015-06-12;修改稿日期:2015-07-06。

应用于CO2捕获的MOFS材料

应用于CO2捕获的MOFS材料
IRMOF 系列材料
IRMOFs 由[Zn4O]6+无机基团与一系列芳香酸配体,以八面体形式桥 连自组装而成的微孔晶体材料
UiO 系列材料
UiO(University of Oslo) 系列的 MOF 材料通常含有金属锆,结构 分为八面体、锥形四面体两种。
ZIF 系列材料
ZIF主要由金属离子(Zn 2+、 Co2+ )和咪唑类配体组成。
功能性强
可以选择不同的有机
配体与金属离子结合, 3
合成出不同功能的 MOFs 材料,还可以 经过改性引入功能基 团调控性能
MOFs材料的特点
2 稳定性高
1
有着良好的热稳
定性和化学稳定

种类繁多
有大量可以作为 配体的有机物, 例如羧酸酯,酚, 吡啶等。
孔隙率高
比表面积大,密度小, 孔隙率高。
孔尺寸可调整
综上所述,材料的比表面积越大,CO2吸附量就越大;氨负载量越大,CO2吸附 量亦越大。但是,氨水浸溃改性后的材料NH3-Mg-MOF-74对CO2吸附性能的大小, 既不取决于材料比表面积也不取决于所使用浸溃氨水的浓度,而是二者因素共
同作用。当使用氨水溶液浸溃原材料Mg-MOF-74时,使用高浓度的氨水有
构建超微孔结构
当客体分子大小与孔径尺寸相近 时,其对吸附性能的影响尤为明 显,且孔径越接近分子实际尺寸, 吸附作用越强。
Mg-MOF-74的氨改性
说明用不同浓度氨水 溶液浸渍负载MgMOF-74并未改变材料 的结构特征,改性后 的材料仍具有良好的 晶体结构。
Mg-MOF-74与NH3-Mg-MOF-74材料的XRD衍射图谱
或金属簇)与桥连的有机配体通过
自组装相互连接,形成的一类具有

Amine-Functionalized Metal Organic Framework as a Highly Selective Adsorbent for CO2 over CO

Amine-Functionalized Metal Organic Framework as a Highly Selective Adsorbent for CO2 over CO
0 1 0 2 1 0n K1n1 p1 1 1 0n K 2n2 p2 2

1
(8)
For y1:y2=1:m mixed gases,
y1
y2
1 1 m
m 1 m
(9) (10)
Combining equation (2), (9), (10), equation (11) is obtained.
RT A pi0
P 0
i0 ( pi0 )

qi ( p) dp p
(1)
pt yi pi0 xi
(2) (3) (4) (5) (6)
i0 0 j
x 1 y 1
i
i
S
xi xj
In these equations, qi(p) is the adsorption capacity of pure gas experimentally measured as a function of p. A is the surface area of the adsorbent (For a specific adsorbent, A is the same for different gases).pt is the total pressure of mixed gases and xi, yi is the adsorbed and gas phase mole fractions for component i. pi0 is the equilibrium gas phase pressure of the pure component I corresponding to the so-called spreading pressure πi0 (pi0). The selectivity of component i over component j, S, is derived from the ratio of adsorbed phase mole fraction xi and xj. The specific calculation process is shown as follows. Equation (7) is derived from the combination of equation (1) and Freundlich equation.

《2024年SBA-16及沸石改性的HKUST-1用于CO2吸附性能研究》范文

《2024年SBA-16及沸石改性的HKUST-1用于CO2吸附性能研究》范文

《SBA-16及沸石改性的HKUST-1用于CO2吸附性能研究》篇一SBA-16及沸石改性HKUST-1在CO2吸附性能研究中的应用一、引言随着全球气候变化和环境污染问题日益严重,碳捕集和储存(CCS)技术的研究逐渐受到关注。

在众多的CCS技术中,吸附法因其在捕获二氧化碳(CO2)方面的高效性、经济性和环保性,而受到广泛关注。

在众多的吸附材料中,SBA-16及沸石改性的HKUST-1因其独特的结构和良好的吸附性能,成为研究的热点。

本文旨在探讨这两种材料在CO2吸附性能方面的应用及研究进展。

二、SBA-16的CO2吸附性能研究SBA-16是一种具有高比表面积和有序介孔结构的材料,其独特的结构特性使其在CO2吸附方面具有潜在的应用价值。

研究表明,SBA-16的孔径和表面化学性质对CO2的吸附性能具有重要影响。

首先,SBA-16的孔径大小对CO2的吸附能力有显著影响。

较大的孔径有利于CO2分子的扩散和传输,从而提高吸附速率和容量。

其次,SBA-16的表面化学性质也是影响CO2吸附的重要因素。

通过引入含氮、氧等极性基团,可以增强SBA-16与CO2分子之间的相互作用,从而提高其吸附性能。

三、沸石改性的HKUST-1的CO2吸附性能研究HKUST-1是一种具有高比表面积和良好稳定性的金属有机骨架(MOF)材料,其三维开放骨架结构有利于CO2分子的传输和吸附。

然而,HKUST-1的CO2吸附性能仍需进一步提高以满足实际应用的需求。

通过沸石改性可以优化HKUST-1的结构和性能。

沸石作为一种具有多级孔结构和丰富表面化学性质的天然材料,其引入可以增加HKUST-1的比表面积和孔容,提高其CO2吸附能力。

同时,沸石中的硅、铝等元素与HKUST-1中的金属离子发生相互作用,形成更强的CO2分子亲和力,进一步提高其吸附性能。

四、SBA-16及沸石改性的HKUST-1在CO2吸附中的应用对比在CO2吸附性能方面,SBA-16和沸石改性的HKUST-1均具有良好的表现。

光电催化co2还原的文献综述

光电催化co2还原的文献综述

光电催化co2还原的文献综述摘要:1.引言2.二氧化碳的光电催化还原概述3.光电催化CO2 还原的关键参数4.光电催化CO2 还原的催化剂研究5.光电催化CO2 还原的挑战与展望6.结论正文:1.引言随着全球气候变暖和环境污染问题日益严重,开发可持续的清洁能源和环境友好型技术已成为当务之急。

二氧化碳(CO2)作为温室气体的主要成分,对其进行有效转化以减少温室效应具有重要意义。

光电催化CO2 还原技术可以将太阳能直接转化为化学能,实现二氧化碳的转化,因此备受关注。

本文旨在对光电催化CO2 还原的研究进行综述,以期为相关领域的研究者提供参考。

2.二氧化碳的光电催化还原概述光电催化CO2 还原是指在光照条件下,利用光电催化材料将CO2 转化为低碳烃或氧气等有用物质的过程。

这一过程需要在光催化材料表面产生光生电子- 空穴对,并利用这些活性载体进行还原反应。

根据反应的类型,光电催化CO2 还原可分为光催化还原和光电催化氧化两种。

3.光电催化CO2 还原的关键参数影响光电催化CO2 还原效率的关键参数包括光催化材料的选择、光催化剂的形貌和结构、以及反应条件等。

光催化材料的选择主要取决于其光吸收性能、电子结构和催化活性。

光催化剂的形貌和结构对光生电子- 空穴对的产生和传输具有重要影响。

反应条件包括光照强度、反应温度、气氛和反应时间等,这些条件会影响到光催化CO2 还原的速率和选择性。

4.光电催化CO2 还原的催化剂研究目前,已经发现的光电催化CO2 还原催化剂包括金属氧化物、金属硫属化合物、金属有机框架(MOFs)和共价有机框架(COFs)等。

这些催化剂具有不同的优点,如高光吸收性能、良好的电子结构和丰富的活性位点等,能够在不同程度上促进CO2 的还原。

5.光电催化CO2 还原的挑战与展望尽管光电催化CO2 还原取得了一定的研究进展,但仍面临许多挑战,如低转化效率、高成本和稳定性差等。

为了克服这些挑战,研究者们需要在催化剂设计、反应条件优化和器件结构改进等方面进行深入研究。

CO2矿物封存技术研究进展

CO2矿物封存技术研究进展

化工进展Chemical Industry and Engineering Progress2022年第41卷第4期CO 2矿物封存技术研究进展何民宇1,刘维燥1,刘清才1,秦治峰2(1重庆大学材料科学与工程学院,四川重庆400044;2四川大学化学工程学院,四川成都610065)摘要:CO 2捕集与封存技术是目前实现碳减排最有效的方法。

其中,CO 2矿物封存(又称CO 2矿化)是利用CO 2与含钙镁硅酸盐矿物进行反应使CO 2以稳定的碳酸盐形式永久储存起来。

本文首先介绍了CO 2矿化的基本原理和技术路线,其中间接矿化反应条件较温和、矿化效率更高、得到的产物也更纯,因此对于CO 2间接矿化的研究也更广泛。

本文综述并对比了天然矿物及工业固废矿化CO 2的研究进展,指出工业固废更有利于CO 2矿化过程。

工业固废矿化CO 2过程矿化CO 2的同时处理了工业固废,实现以废治废,因此它在经济上也是具有一定优势。

在此基础上,本文以高炉渣为代表,介绍了其矿化CO 2的详细研究进展,指出采用可循环的助剂、回收高炉渣中有价元素可提升矿化过程经济性。

对于CO 2矿化过程的放大试验、生命周期的评估及低能耗的新工艺开发将是CO 2矿物封存实现工业化的关键。

关键词:CO 2矿物封存;工业固废;碳酸化;硫酸铵;高炉渣中图分类号:TQ53文献标志码:A文章编号:1000-6613(2022)04-1825-09Research progress in CO 2mineral sequestration technologyHE Minyu 1,LIU Weizao 1,LIU Qingcai 1,QIN Zhifeng 2(1College of Materials Science and Engineering,Chongqing University,Chongqing 400044,Sichuan,China;2School ofChemical Engineering,Sichuan University,Chengdu 610065,Sichuan,China)Abstract:At present,CO 2capture and storage technology is the most effective way to achieve CO 2emission reduction.Wherein,CO 2mineral sequestration mainly utilizes the reactions of carbon dioxide with calcium and magnesium silicate minerals to form stable carbonates,and thus can permanently store CO 2.The principles and pathways for CO 2mineral carbonation are briefly introduced in this paper.Indirect carbonation receives more attentions due to the moderate reaction condition,higher mineralization efficiency and possibility for recovering valuable byproducts.This paper reviews and compares the carbonation process by using natural minerals and industrial solid wastes as feedstock.It is found that the latter is more conducive to the CO 2mineralization process.This process realizes the disposal of industrial solid wastes while storing CO 2,realizing the treatment of waste with waste,which had certain advantages in economy.Based on above,this paper takes blast furnace slag as representative and summarized its research progress in CO 2mineral carbonation.It is pointed out that using recyclable reagents and recovering valuable elements from blast furnace slag can improve the economy of CO 2mineralization.To realize the industrial application of the CO 2mineralization technology,the scale-up综述与专论DOI :10.16085/j.issn.1000-6613.2021-0845收稿日期:2021-04-21;修改稿日期:2021-06-09。

吸附二氧化碳的mof晶体结构

吸附二氧化碳的mof晶体结构

吸附二氧化碳的mof晶体结构英文回答:Metal-organic frameworks (MOFs) are a class of crystalline materials with a porous structure that can be used for a variety of applications, including gas storage, catalysis, and drug delivery. MOFs are typically composed of metal ions or clusters that are connected by organic ligands. The resulting structure has a high surface area and a large number of pores, which allows it to adsorb a variety of molecules.One of the most promising applications of MOFs is for the adsorption of carbon dioxide. Carbon dioxide is a greenhouse gas that contributes to climate change. MOFs can be used to capture carbon dioxide from the atmosphere or from industrial processes. The carbon dioxide can then be stored underground or used to produce fuels and other products.A number of different MOFs have been developed for the adsorption of carbon dioxide. Some of the most promising MOFs include:MIL-101: MIL-101 is a MOF that is composed of chromium(III) ions and terephthalate ligands. MIL-101 has a high surface area and a large number of pores, which allows it to adsorb a large amount of carbon dioxide.MOF-5: MOF-5 is a MOF that is composed of zinc ions and terephthalate ligands. MOF-5 has a high surface area and a large number of pores, which allows it to adsorb a large amount of carbon dioxide.HKUST-1: HKUST-1 is a MOF that is composed ofcopper(II) ions and trimesate ligands. HKUST-1 has a high surface area and a large number of pores, which allows it to adsorb a large amount of carbon dioxide.These are just a few of the many different MOFs that have been developed for the adsorption of carbon dioxide. MOFs are a promising new technology for the capture andstorage of carbon dioxide. They have the potential to make a significant contribution to the fight against climate change.中文回答:金属有机骨架(MOF)是一类具有多孔结构的晶体材料,可用于多种应用,包括储气、催化和药物输送。

低氧化态的过渡金属co2吸附能力 -回复

低氧化态的过渡金属co2吸附能力 -回复

低氧化态的过渡金属co2吸附能力-回复低氧化态过渡金属的CO2吸附能力随着全球气候变化和能源需求的增长,减缓二氧化碳(CO2)的排放成为一项迫切的任务。

过渡金属催化剂在CO2吸附与转化方面展示了巨大的潜力。

其中,低氧化态的过渡金属表现出了极高的CO2吸附能力。

本文将从介绍低氧化态过渡金属的定义与性质开始,然后探讨其CO2吸附能力的原理与影响因素,最后总结未来的研究方向。

首先,低氧化态过渡金属是指其氧化态低于它们通常的氧化态。

在过渡金属的周期表中,位于左侧的元素,如镍(Ni)、铁(Fe)和钴(Co),在低氧化态下能够更有效地与CO2发生相互作用。

这是因为CO2是一个电负性较高的分子,能够向电负性较低的过渡金属中心提供电子。

此外,低氧化态的过渡金属还表现出更高的表面活性,使其能够更好地与CO2分子接触。

其次,低氧化态过渡金属的CO2吸附能力受多种因素的影响。

第一个因素是过渡金属的氧化还原能力。

较低氧化态的过渡金属能够容易地与CO2发生还原反应,形成CO和其他有机物。

因此,具有较强还原能力的过渡金属,如铁、镍和钴,通常表现出更高的CO2吸附能力。

其次,过渡金属的晶体结构也会影响其CO2吸附性能。

一些过渡金属具有较大的孔隙结构,提供了更多的吸附位点,因此具有更高的CO2吸附能力。

此外,催化剂的载体也对CO2吸附能力起着重要作用。

通常情况下,催化剂需要被支撑在活性载体上,以提高其表面积和稳定性。

常见的载体材料包括二氧化硅(SiO2)、氧化铝(Al2O3)和氧化锆(ZrO2)等。

这些载体具有较高的比表面积和良好的热稳定性,能够提供更多的吸附位点和保护过渡金属离子不受氧化的环境。

在解释低氧化态过渡金属CO2吸附能力的原理时,有两个主要的机制被提出:配位催化和氧化还原催化。

配位催化是指CO2通过与低氧化态过渡金属形成配位键而被吸附。

催化剂表面的活性位点能够与CO2分子中的带正电的中心(如碳原子)形成配位键,并吸引CO2分子吸附在催化剂表面上。

co2-tpo表征

co2-tpo表征

co2-tpo表征
CO2-TPD (Carbon Dioxide Temperature Programmed Desorption) 是一种用于表征催化剂表面上活性氧化物种的技术。

它通常用于研究固体表面上的氧化物,例如氧化铜、氧化锌等。

在CO2-TPD实验中,首先在催化剂表面吸附二氧化碳(CO2),然后通
过升温来驱使CO2从表面脱附。

通过监测脱附过程中释放的CO2量,可以得到关于催化剂表面上活性氧化物种的信息。

CO2-TPD技术的原理是基于不同氧化物种与CO2的吸附特性不同。

通过在不同温度下对催化剂表面进行程序升温,可以定量地测
量不同温度下CO2的脱附量,从而得到活性氧化物种的脱附特性曲线。

这些曲线可以提供有关催化剂表面上活性氧化物种的信息,例
如其种类、浓度、分布等。

CO2-TPD技术在催化剂研究中具有重要意义。

通过了解催化剂
表面上活性氧化物种的特性,可以优化催化剂的设计和制备,提高
催化剂的活性和选择性。

此外,CO2-TPD还可以用于研究催化剂的
稳定性和寿命,以及催化剂在反应过程中活性氧化物种的变化情况。

总之,CO2-TPD是一种重要的表征技术,可以帮助科研人员深
入了解催化剂表面上活性氧化物种的特性,为催化剂设计和应用提供重要参考。

钙钛矿瞬态吸收science

钙钛矿瞬态吸收science

钙钛矿瞬态吸收science
钙钛矿在科学领域中是一个备受关注的研究课题,特别是其在光电子器件和太阳能电池方面的应用。

钙钛矿材料因其优良的光电性能而备受瞩目,其中瞬态吸收是研究中的一个重要方面。

首先,让我们来了解一下什么是钙钛矿。

钙钛矿是一类晶体结构具有ABX3式结构的材料,其中A通常是较大的有机阳离子,B是较小的金属阳离子,X则是卤素阴离子。

这种结构使得钙钛矿材料具有优异的光电特性,因此被广泛研究和应用。

瞬态吸收是一种用于研究材料在极短时间尺度下光学响应的技术。

在钙钛矿研究中,瞬态吸收技术被广泛应用于研究材料的载流子动力学、光生电荷分离和传输等过程。

通过瞬态吸收技术,研究人员可以了解钙钛矿材料在光照条件下的电子和空穴的行为,从而为提高太阳能电池的效率和稳定性提供重要信息。

钙钛矿瞬态吸收的研究不仅有助于深入理解钙钛矿材料的光电特性,还为钙钛矿太阳能电池等器件的设计和优化提供了重要的理论基础。

通过对钙钛矿瞬态吸收特性的深入研究,科学家们可以不断改进钙钛矿材料的性能,推动钙钛矿在光电子器件领域的应用。

总的来说,钙钛矿瞬态吸收在科学研究中具有重要意义,它为我们揭示了钙钛矿材料在极短时间尺度下的光学行为,为钙钛矿材料的应用和改进提供了重要的理论支持。

希望这些信息能够对你有所帮助。

在不同温度下含铜的MOFs材料Cu-BTC对CO2的吸附研究

在不同温度下含铜的MOFs材料Cu-BTC对CO2的吸附研究

在不同温度下含铜的MOFs材料Cu-BTC对CO2的吸附研究摘要:利用溶剂热法,均苯三甲酸(H3btc)用做有机配体与硝酸铜进行溶剂热反应合成了金属有机骨架(MOFs,Metal Organic Framworks)材料Cu-BTC。

通过BET比表面分析、X-射线衍射(XRD)、扫描电镜(SEM)、热重分析(TG)、差热分析(DSC)等分析技术对其结构进行了表征。

重点考察了在不同温度条件下Cu-BTC对CO2的变压吸附(PSA)性能,发现Cu-BTC对CO2具有较高的吸附容量,且在不同压力对应CO2吸附量的吸附等温线上出现了一个特定的拐点;有趣的是首次发现该吸附曲线拐点所对应的CO2吸附量随温度升高呈现很好的线性变化趋势,有助于MOFs微孔结构材料Cu-BTC在气体的吸附与分离领域的应用。

关键词:金属-有机骨架;气体吸附;二氧化碳;变压吸附Abstract: using solvent hot method, all three were acid (H3btc) used as Organic ligands and nitric acid copper for the synthesis of Organic solvent flavoring substances Metal skeleton (MOFs, Metal Organic Framworks) material Cu-BTC. Through the BET surface analysis, than the X-ray diffraction (XRD), scanning electron microscopy (SEM), thermogravimetric analysis (TG), differential thermal analysis (DSC) analysis technology to the structures were characterized. The author in different temperature condition of Cu-BTC CO2 pressure swing adsorption (PSA) change performance, find that the Cu-BTC to CO2 has high adsorption capacity, and the corresponding with different pressure CO2 adsorption DengWenXian adsorption of appeared on a specific inflection point; Interesting is the first found that the adsorption curve inflection point of the corresponding CO2 adsorption increased with temperature present good linear change trend, help MOFs microporous structure material Cu-BTC in gas adsorption and separating fields.Keywords: metal-organic skeleton; Gas adsorption; Carbon dioxide; Variable pressure adsorption*通讯联系人. 黎维彬教授.本项目得到国家科技支撑计划(2008BADC4B12)的资助。

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CO2 Adsorption of Metal Organic Framework Material Cu-BTC via Different Preparation RoutesMei Mei Peng, Dae Kyung Kim, Abidov Aziz, Kyung Ran Back, Ung Jin Jeon, and Hyun Tae Jang*Chemical Engineering Department, Hanseo University, Seosan 356-706, South Korea htjang@hanseo.ac.krAbstract. In this work, Cu3(BTC)2 (Cu-BTC) metal organic framework (MOF), also known as HKUST-1, was prepared by 3 different synthetic route. The synthesized Cu-BTC materials were characterized by powder X-ray diffraction (XRD) for phase structure, scanning electron microscopy (SEM) for crystal structure, thermogravimetric analysis (TGA) for thermal stability, and nitrogen adsorption-desorption for pore textural structure. The results showed that the sample synthesized by microwave method has the high surface area and pore volume of 1721 m2g-1 and 0.7424 cm3g-1, respectively. Among the three synthetic methods, the sample synthesized by microwave method exhibited a CO2 uptake of 23.3% at 25 °C and ambient pressure. Keywords: MOFs, Cu-BTC, CO2 adsorption, porous material.1IntroductionMetal-organic frameworks (MOFs) have been of considerable interest in recent years because of their novel three dimensional porous architectures. As a new class of nanoporous materials MOF have many potential advantages over the traditional adsorbents, such as well-defined structures, controlled pore size, high thermal and chemical stability, high surface area, low density, desired chemical functional groups [1-5]. Applications of MOFs in gas storage, gas/vapor separation, size-, shape-, and enantio-selective catalysis, luminescent and fluorescent materials, and drug storage and delivery have been explored [6]. The attractive properties of MOFs make them promising materials for gas separation and storage [7-12]. MOF-210 synthesized by Yaghi et al. currently holds the record breaking CO2 storage of 2400 mg/g of MOF at room temperature and at ca. 50 bar [13], the surface area and pore volume of this MOF is 6240 m2g-1 and 3.6 cm3g-1, this is the highest surface area reported for any crystalline material. Like this MOF-177 also have highest CO2 adsorption capacity of about 33.5 mmol g-1 at 32 bar [14]. Cu3(BTC)2, (Cu-BTC) also known as HKUST-1 is a widely studied MOF, which was first reported by Chui et al. [15]. Cu-BTC is a typical coordination framework*Corresponding author.T.-h. Kim et al. (Eds.): MAS/ASNT 2012, CCIS 341, pp. 244–251, 2012. © Springer-Verlag Berlin Heidelberg 2012CO2 Adsorption of Metal Organic Framework Material Cu-BTC245with open metal sites, this unsaturated metal centers exhibits a high CO2 adsorption capacity, this open metal sites can participate in the binding of CO2 directly. Bordiga et al. investigated the CO2 adsorption in Cu-BTC by IR spectroscopy [16]. Their results showed that the coordinatively unsaturated Cu2+ centers in this MOF act as specific interaction sites and play an important role in CO2 adsorption. The mechanism of adsorption can be described by CO2 coordination to the metal center in an end-on fashion, i.e., O=C=O···Cu2+. CO2 adsorption of Cu-BTC has been reported by several groups [9, 14, 17], among which the highest CO2 uptake capacity has been reported as 12.7 mmol g-1 at 15 bar and ambient temperature [17]. Based on the previous reports, in the present study, Cu-BTC was synthesized in 3 different methods and studied for its CO2 adsorption performance at ambient temperature and pressure.22.1ExperimentalChemicalsCopper (II) nitrate trihydrate [Cu(NO3)2·3H2O, Daejung chemicals & metals, 99%], benzene-1,3,5-tricarboxylic acid (BTC, Sigma Aldrich, C9H6O6, 95%). The solvents, ethyl alcohol anhydrous (C2H5OH, Daejung chemicals & metals 99.9%), N,Ndimethylformamide [DMF, HCON(CH3)2, Daejung chemicals & metals 99.5%], chloroform [CHCl3, Daejung chemicals & metals 99.5%], deionized (DI) water were used in the synthesis. 2.2 Synthesis Procedures for Cu-BTC with Different Methods2.2.1 Solvothermal Method (Cu-BTC-ST1) Cu(NO3)2·3H2O (1.75 g, 7.2 mmol) was dissolved into 24 ml DI water, and BTC (0.84 g, 4 mmol) was dissolved into 24 ml ethanol under stirring at room temperature. Then the copper solution was added to the BTC solution and stirred for 1 h. The mixture was transferred to a Teflon lined stainless steel autoclave and kept at 120 °C for 12 h. The reaction vessel was cooled to ambient temperature, centrifuged and the solid product was vacuum dried at room temperature to yield sample, CuBTC-ST1 [18]. 2.2.2 Solvothermal Method (Cu-BTC-ST2) Cu-BTC-ST2 was synthesized following the procedure reported by Xiang et al. [19]. BTC (2.5 g, 12 mmol) and Cu(NO3)2·3H2O (5 g, 20.7 mmol) were added in a 250 ml bottle in 125 ml solvent consisting of DMF, ethanol, and DI water with a ratio of 1:1:1, after sonication for 15 min, the bottle was placed in an oven at 85 °C for 20 h. The product was isolated by filtration and rinsed with 3x10 ml DMF, and then immersed in CHCl3 for 3 days, during which the activation solvent was decanted and replaced freshly thrice. The product was dried at 200 °C in vacuum to yield Cu-BTCST2.246M.M. Peng et al.2.2.3 Microwave Method (Cu-BTC-MW) Cu-BTC-MW was synthesized following the procedure reported by Xiang et al. [19]. BTC (2.5 g, 12 mmol) and Cu(NO3)2·3H2O (5 g, 20.7 mmol) were added in a 500 ml beaker in 125 ml solvent containing DMF, ethanol, and DI water with a ratio of 1:1:1. After sonication for 15 min, the beaker was then placed inside household microwave oven (Goldstar, MH-700H) and heated at 700 W for 4 min, during which the beaker was put out from microwave oven for a little while with slight stir every 30 s to avoid explosion. A blue suspension was obtained. The product was isolated and then rinsed with 3x10 ml DMF. After exchanging with CHCl3 for three days, the product was dried at 200 °C in vacuum to yield Cu-BTC-MW. 2.3 CharacterizationPowder X-ray diffraction (XRD) patterns were recorded using a Rigaku D/Max 2200+Ultima diffractometer with Cu-Kα radiation (λ=0.154 nm). The diffraction data were recorded in the 2θ range 5-50° with a step of 0.02 °/s. Thermogravimetric analysis (TGA) was performed by Scinco TGA N-1000 thermo gravimetric (TG) analyzer, the sample was heated from room temperature to 800 °C under N2 at a temperature ramp of 10 °C/min. The nitrogen adsorption-desorption isotherms were measured at 77 K on a Belsorp mini II volumetric adsorption analyzer. Prior to each adsorption measurement the samples were evacuated at 200 °C under vacuum (p<10-5 mbar) for 6 h in the degassing port. The surface area (SBET) was determined from the linear part of the Brunauer-Emmett-Teller (BET) equation, and the pore volume was calculated using a BET plot based on the amount of nitrogen gas adsorbed at the last adsorption point (p/p0 = 0.99) and the pore size distribution using the Barrett-JoynerHalenda (BJH) method. SEM images were captured on JEOL JSM 5600 scanning electron microscope. 2.4 CO2 AdsorptionCO2 adsorption-desorption measurements for Cu-BTC MOFs were performed using Scinco TGA N-1000 thermo gravimetric (TG) analyzer. A sample weight of approximately 10 mg was loaded into an alumina sample pan in a TG unit and tested for CO2 adsorption-desorption performance. The initial activation of the samples was carried out at 150 °C for 1 h in a nitrogen atmosphere. Then adsorption run was conducted using CO2 gas (99.99%), and the desorption run was conducted in N2 flow. The adsorption runs were conducted at 25, 50, 75 °C under atmospheric pressure, and desorption was determined at 150 °C.33.1Results and DiscussionsCharacterizationFig.1 A. shows the XRD patterns of Cu-BTC sample prepared by solvothermal and microwave methods. The XRD patterns of the Cu-BTC obtained by the three methodsCO2 Ads sorption of Metal Organic Framework Material Cu-BTC247were almost similar with ea other, and coincided closely with the Cu-BTC repor ach rted in literature [18]. It indicate that the three samples synthesized by different meth ed hods have the same crystal stru ucture. The SEM images of the synthesized samples are presented in Fig. 1 B. Th showed octahedral morphology [20]. The crystals of hey s samples synthesized by th solvothermal method were almost similar while the he sample synthesized by m microwave method was smaller in size which was in e accordance with the previou report [19]. Smaller dimensions of the latter were due to us homogeneous effect. More seeds were formed in a short time, leading to a li e ittle chance for the seeds to grow up while using microwave. wFig. 1. A. XRD patterns of Cu u-BTC prepared with different methods.(a) Cu-BTC-ST1, (b) CuBTC-ST2 and (c) Cu-BTC-MW B. SEM images of Cu-BTC prepared with different meth W. hods. (a) Cu-BTC-ST1, (b) Cu-BT TC-ST2, (c) Cu-BTC-MW and (d) Cu-BTC-MW at 10, ,000 magnification.The nitrogen adsorption n-desorption isotherms of Cu-BTC samples prepared by different methods are show in Fig. 2. All of them displayed Type I isotherm a wn m, signature characteristic of m microporous materials. The surface area and pore volu ume Cu-BTC-MW was found to be 1721 m2g-1 and 0.7424 cm3g-1 respectively, which w o was higher than Cu-BTC-ST1 a Cu-BTC-ST2 (Table 1). The results are in line with the and previous reports [19]. The s surface area and pore volume of Cu-BTC-MW was alm most nearer to value reported by Millward and Yaghi [14]. The thermograms of the synthesized samples are presented in Fig. 3. Prior to e r ater analysis, the samples were preheated in a vacuum oven remove the physisorbed wa and gases. Initial weight loss below 150 °C is attributed to desorption of the coordinated water. A weigh loss of about 5.2 and 3.4 % was observed for Cu-BT ht TCST 1 and 2 while a loss of about 7.6% was noted for Cu-BTC-MW, hence the la f atter retains more amount of water. The second weight loss around above 300 °C was due to the decomposition of th organic network. Cu-BTC-MW was found to be sta he able upto 350 °C.248M.M. Peng et al.Fig. 2. N2 adsorption-desorption isotherms of Cu-BTC prepared with different methods Table 1. Porosity properties of Cu-BTC prepared with different methodsSample Cu-BTC-ST1 Cu-BTC-ST2 Cu-BTC-MW 3.2 CO2 AdsorptionSBET (m2g-1)1465.0 1656.8 1721.0Total pore volume (cm3g-1)0.6079 0.7130 0.7424Average pore diameter (nm)1.6600 1.6571 1.7924The CO2 adsorption and desorption profiles of Cu-BTC samples are presented in Fig. 4, the CO2 adsorption capacity of the three samples decreased with increase in temperature, which reveals that the CO2 adsorption in Cu-BTC was mainly by physical adsorption. High CO2 uptake was exhibited by Cu-BTC-MW of about 23.3 wt% while for Cu-BTC-ST 1 and 2 exhibited 16.7 and 22.3 wt% respectively, at 25 °C. Hence, Cu-BTC-MW is better than other as it showed high adsorption at room temperature (25 °C) and atmospheric pressure The repeatability of Cu-BTC-MW was verified by carrying four consecutive CO2 adsorption-desorption runs at 25 °C (adsorption) and 150 °C (desorption) with pure CO2 (99.99%) feed gas. No apparent change in CO2 uptake was observed (Fig. 5). This result suggests that the Cu-BTC-MW is reusable.CO2 Ads sorption of Metal Organic Framework Material Cu-BTC249Fig. 3. TGA cu urves of Cu-BTC prepared with different methodsFig. 4. CO2 adsorption-deso orption profiles of Cu-BTC prepared with different methods. (a) Cu-BTC-ST1, (b) Cu-BTC-ST2 and (c) Cu-BTC-MW.250M.M. Peng et al.Fig. 5. Recycla ability of CO2 adsorption at 25 °C of Cu-BTC-MW4ConclusionCu-BTC crystals were sy ynthesized under solvothermal and microwave assis sted solvothermal conditions. Compared to the 2 solvothermal methods, Cu-B BTC ave ume synthesized under microwa condition possessed high surface area and pore volu of 1721 m2g-1 and 0.7424 c 3g-1. The CO2 uptake of Cu-BTC-MW was found to be cm o about 23.3 wt% at 25 °C a ambient pressure. So from this study, it is concluded and that, for the synthesis of C Cu-BTC, microwave method is a better than others a it as requires short crystallizati ion time and also exhibit high CO2 uptake at ro oom temperature and pressure. Acknowledgements. We a acknowledge the financial support by grants from Ko orea CCS R&D center, founded by the Ministry of Education, Science and Technology of y the Korean Government.References1. Banerjee, R., Furukawa, H Britt, D., Knobler, C., O’Keeffe, Y.O.M.: Control of Pore S H., Size and Functionality in Isore eticular Zeolitic Imidazol M. ate Frameworks and Their Car rbon Dioxide Selective Capture Properties. J. Am.Chem. Soc. 131, 3875–3877 (2009) e 2. Ferey, G.: Hybrid Porou Solids: Past, Present, Future. Chem. Soc. Rev. 37, 191– us –214 (2008)CO2 Adsorption of Metal Organic Framework Material Cu-BTC2513. Yaghi, O.M., O’Keeffe, M., Ockwig, N.W., Chae, H.K., Eddaoudi, M., Kim, J.: Reticular Synthesis and the Design of New Materials. Nature 423, 705–714 (2003) 4. Rowsell, J.L.C., Yaghi, O.M.: Metal-Organic Frameworks: A New Class of Porous Materials. Micropor. Mesopor. Mater. 73, 3–14 (2004) 5. Snurr, R.Q., Hupp, J.T., Nguyen, S.T.: Prospects for Nanoporous Metal-Organic Materials in Advanced Separations Processes. AIChE J. 50, 1090–1095 (2004) 6. Kuppler, R.J., Timmons, D.J., Fang, Q.R., Makal, J.R., Li, T.A., Young, M.D., Yuan, D.Q., Zhao, D., Zhuang, W.J., Zhou, H.C.: Potential Applications of Metal-Organic Frameworks. Coordination Chemistry Reviews 253, 3042–3066 (2009) 7. Li, J.R., Kuppler, R.J., Zhou, H.C.: Selective Gas Adsorption and Separation in MetalOrganic Frameworks. Chem. Soc. Rev. 38, 1477–1504 (2009) 8. Ma, S.Q., Zhou, H.C.: Gas Storage in Porous Metal-Organic Frameworks for Clean Energy Applications Chem. Commun. 46, 44–53 (2010) 9. Wang, Q.M., Shen, D., Bulow, M., Lau, M., Deng, S., Fitch, F.R., Lemcoff, N.O., Semanscin, J.: Metallo-Organic Molecular Sieve for Gas Separation and Purification. J. Micro. Meso. Mater. 55, 217–230 (2002) 10. Saha, D., Wei, Z., Deng, S.: Equilibrium, Kinetics and Enthalpy of Hydrogen Adsorption in MOF-177. Int. J. Hydrogen Energy 33, 7479–7488 (2008) 11. Saha, D., Deng, S.: Adsorption Equilibria and Kinetics of Carbon Monoxide on Zeolite 5A, 13X, MOF-5, and MOF-177J. Chem. Eng. Data 54, 2245–2250 (2009) 12. Saha, D., Wei, Z., Deng, S.: Hydrogen Adsorption Equilibrium and Kinetics on MetalOrganic Framework (MOF)-5 Synthesized with DEF ApproachSep. Purif. Technol. 64, 280–287 (2009) 13. Furukawa, H., Ko, N., Go, Y.B., Aratani, N., Choi, S.B., Choi, E., Yazaydin, A.O., Snurr, R.Q., O’Keeffe, M., Kim, J., Yaghi, O.M.: Ultrahigh Porosity in Metal-Organic Frameworks. Science 329, 424–427 (2010) 14. Millward, A.R., Yaghi, O.M.: Metal-Organic Frameworks with Exceptionally High Capacity for Storage of Carbon Dioxide at Room Temperature. J. Am. Chem. Soc. 127, 17998–17999 (2005) 15. Chui, S.S.-Y., Lo, S.M.-F., Charmant, J.P.H., Orpen, A.G., Williams, I.D.: A Chemically Functionalizable Nanoporous Material [Cu3(TMA)2(H2O)3]n. Science 19, 1148–1150 (1999) 16. Bordiga, S., Regli, L., Bonino, F., Groppo, E., Lamberti, C., Xiao, B., Wheatley, P.S., Morris, R.E., Zecchina, A.: Adsorption Properties of HKUST-1 Toward Hydrogen and Other Small Molecules Monitored by IR. Phys. Chem. Chem. Phys. 9, 2676–2685 (2007) 17. Liang, Z., Marshall, M., Chaffee, A.L.: CO2 Adsorption-Based Separation by Metal Organic Framework (Cu-BTC) versus Zeolite (13X). Energy Fuels 23, 2785–2789 (2009) 18. Schlichte, K., Kratzke, T., Kaskel, S.: Improved Synthesis, Thermal Stability and Catalytic Properties of the Metal-Organic Framework Compound Cu3(BTC)2 Micropor. Mesopor. Mater. 73, 81–88 (2004) 19. Xiang, Z.H., Cao, D.P., Shao, X.H., Wang, W.C., Zhang, J.W., Wu, W.Z.: Facile Preparation of High-Capacity Hydrogen Storage Metal-Organic Frameworks: A Combination of Microwave-Assisted Solvothermal Synthesis and Supercritical Activation. Chemical Engineering Science 65, 3140–3146 (2010) 20. Xiang, S.C., Zhou, W., Gallegos, J.M., Liu, Y., Chen, B.L.: Exceptionally High Acetylene Uptake in a Microporous Metal-Organic Framework with Open Metal Sites. J. Am. Chem. Soc. 131, 12415–12419 (2009)。

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