Co3O4改性USY分子筛吸附和催化氧化甲苯特性研究

利用水热法合成Co₃O₄/USY复合材料,研究其对有机污染物甲苯的吸附和催化氧化特性,同时结合微波对Co₃O₄的精准加热特性,考察不同负载量Co₃O₄/USY在微波作用下的升温特性及催化甲苯氧化降解特性。结果表明,通过水热反应,Co₃O₄在USY表面形成多孔蜂窝状结构;负载Co₃O₄后的USY保持较高的吸附容量,Co₃O₄/USY-1.5m室温下的吸附容量为85 mg/g;Co₃O₄/USY在干、湿两种状态下均在325℃表现出优良的催化氧化特性、CO₂选择性和稳定性;Co₃O₄/USY能够与微波高效耦合,快速升温启动其催化作用,控制反应温度为250℃,发现微波诱导甲苯催化氧化过程的CO₂选择性优于常规催化,表明所制备Co₃O₄/USY复合材料具备吸附甲苯并进行微波快速再生协同有机污染物高效催化氧化降解的可行性。     

A pillared-layer metal-organic framework for efficient separation of C3H8/C2H6/CH4 in natural gas

Metal-organic frameworks (MOFs) have great potentials as adsorbents for natural gas purification. However, the trade-off between selectivity and adsorption capacity remains a challenge. Herein, we report a pillared-layer metal-organic framework Ni(HBTC)(bipy) for efficiently separating the C₃H₈/C₂H₆/CH₄ mixture. The experimental results show that the adsorption capacity of C₃H₈ and C₂H₆ on Ni(HBTC)(bipy) are as high as 6.18 and 5.85 mmol·g^-1, while only 0.93 mmol·g^-1 for CH₄ at 298 K and 100 kPa. Especially, the adsorption capacity of C₃H₈ at 5 kPa can reach an unprecedented 4.52 mmol·g^-1 and for C₂H₆ it is 1.48 mmol·g^-1 at 10 kPa. The ideal adsorbed solution theory predicted C₃H₈/CH₄ selectivity is as high as 1857.0, superior to most of the reported materials. Breakthrough experiment results indicated that material could completely separate the C₃H₈/C₂H₆/CH₄ mixture. Therefore, Ni(HBTC)(bipy) is a promising material for separation of natural gas.     

CO/N2/CO2在MOF-74(Ni)上吸附相平衡和选择性

主要研究了MOF-74(Ni)材料对CO/N₂/CO₂的吸附分离性能。应用水热法合成制备MOF-74(Ni),分别采用全自动表面积吸附仪、P-XRD、扫描电子显微镜对材料的孔隙结构和晶体形貌进行了表征,应用静态吸附法测定了CO、N₂和CO₂在MOF-74(Ni)上的吸附等温线,应用DSLF方程模拟了3种气体MOF-74(Ni)上的吸附等温线,依据IAST理论模型计算了MOF-74(Ni)对CO/N₂二元混合物和CO/CO₂二元混合物的吸附选择性。研究结果表明:在0.1 MPa和常温条件下,MOF-74(Ni)材料对CO吸附容量高达6.15 mmol·g^-1,而相同条件下N₂的吸附量只有0.86 mmol·g^-1。MOF-74(Ni)在低压下(0～40 kPa)对CO的吸附量明显高于其对CO₂的吸附量。应用IAST模型估算MOF-74(Ni)对二元混合物吸附选择性的结果表明:MOF-74(Ni)对CO/N₂混合物的吸附选择性在1000以上;MOF-74(Ni)对CO/CO₂的吸附选择性在4～9范围,在所研究的二元气体混合物吸附体系中,MOF-74(Ni)都能优先吸附CO。     

Ni/Al-LDH/MCNTs原位复合材料的制备与电化学性能

以Ni（NO₃）₂·6H₂O、Al（NO₃）₃·9H₂O、尿素和MCNTs为原料,采用原位均相沉淀法制备了MCNTs含量（质量分数）分别为1%、3%和5%的Ni/Al-LDH/MCNTs复合电极活性材料。采用X射线衍射（XRD）、傅里叶变换红外光谱（FTIR）和场发射扫描电子显微镜（FESEM）表征了材料的微观结构和形貌;采用循环伏安（CV）、电化学交流阻抗（EIS）和充放电测试研究了该复合材料作为镍氢电池正极材料的电化学性能。结果表明,在Ni/Al-LDH中复合MCNTs能够提高材料的电化学活性,降低电化学反应电阻,显著改善材料的大电流充放电性能。其中MCNTs含量为3%的Ni/Al-LDH/MCNTs复合材料具有最佳的电化学性能,在200、500、1000和2000 mA·g^-1电流密度下的放电比容量分别为330、321、307和288 mA·h·g^-1,而未复合MCNTs的Ni/Al-LDH在2000 mA·g^-1电流密度下放电比容量仅为205 mA·h·g^-1。     

Optimization of electrochemically synthesized Cu3(BTC)2 by Taguchi method for CO2/N2 separation and data validation through artificial neural network modeling

Cu₃(BTC)₂, a common type of metal organic framework (MOF), was synthesized through electrochemical route for CO₂ capture and its separation from N₂. Taguchi method was employed for optimization of key parameters affecting the synthesis of Cu₃(BTC)₂. The results indicated that the optimum synthesis conditions with the highest CO₂ selectivity can be obtained using 1 g of ligand, applied voltage of 25 V, synthesis time of 2 h, and electrode length of 3 cm. The single gas sorption capacity of the synthetized microstructure Cu₃(BTC)₂ for CO₂ (at 298 K and 1 bar) was a considerable value of 4.40 mmol·g⁻¹. The isosteric heat of adsorption of both gases was calculated by inserting temperature-dependent form of Langmuir isotherm model in the Clausius-Clapeyron equation. The adsorption of CO₂/N₂ binary mixture with a concentration ratio of 15/85 vol-% was also studied experimentally and the result was in a good agreement with the predicted value of IAST method. Moreover, Cu₃(BTC)₂ showed no considerable loss in CO₂ adsorption after six sequential cycles. In addition, artificial neural networks (ANNs) were also applied to predict the separation behavior of CO₂/N₂ mixture by MOFs and the results revealed that ANNs could serve as an appropriate tool to predict the adsorptive selectivity of the binary gas mixture in the absence of experimental data.     

氧化镍/碳纳米管构筑准固态不对称超级电容器及电化学性能

以Ni(NO₃)₂为原料、NaOH为沉淀剂和羟基化碳纳米管（CNT）为基质首先制备了Ni(OH)₂/CNT复合材料, 然后将其于一定温度下煅烧，使其转变为NiO/CNT复合材料。用X射线粉末衍射仪（XRD）、场发射电子显微镜（FESEM）和透射电子显微镜（TEM）表征了样品的晶相与形貌，结果表明NiO纳米粒子紧密锚附在碳纳米管表面。复合材料可能的形成机理被提出。采用循环伏安法（CV）、单电极充放电和电化学阻抗研究了反应条件对其电化学性能的影响，确定最佳制备条件。将复合材料正极、活性炭负极和PVA-KOH电解质膜组装成准固态不对称超级电容器，电化学性能测试结果表明，在充放电电流密度11.2mA/cm²下，其比电容达到868.0F/g并保持稳定循环3700圈。7500次循环后，其比电容值仍有564.2F/g，显示出高的比电容和长的循环稳定性。     

碱/碱土金属修饰Ni基催化剂的CO2吸附与甲烷化性能

采用分步浸渍法制备了碱/碱土金属修饰Ni基催化剂Ni-M/Al₂O₃ (M=K₂CO₃, Na₂CO₃, MgO, CaO)。探究了碱/碱土金属的添加对改性Ni基催化剂CO₂吸附和甲烷化性能的影响。研究发现,碱/碱土金属的添加提高了Ni/Al₂O₃催化剂表面的碱性活性位点密度,强化了其CO₂吸附性能。碱/碱土金属类型影响Ni-M/Al₂O₃催化剂碱性活性位点的分布、NiO物相的转化及Ni的分散度,进而影响其甲烷化性能。MgO添加使NiO物相转化为与载体呈强相互作用的β型和γ型NiO,降低了催化剂表面的强碱性活性位点比例,有利于CO₂吸附活化。Ni-MgO/Al₂O₃的CO₂吸附容量最高为0.68mmolCO₂/g,其CO₂转化率和CH₄选择性分别高达58.4%和95.4%,其在烟气CO₂捕集与原位甲烷化中极具应用前景。     

Efficient CO2 adsorption and mechanism on nitrogen-doped porous carbons

In this work, nitrogen-doped porous carbons (NACs) were fabricated as an adsorbent by urea modification and KOH activation. The CO₂ adsorption mechanism for the NACs was then explored. The NACs are found to present a large specific surface area (1920.72– 3078.99 m²·g⁻¹) and high micropore percentage (61.60%–76.23%). Under a pressure of 1 bar, sample NAC-650-650 shows the highest CO₂ adsorption capacity up to 5.96 and 3.92 mmol·g⁻¹ at 0 and 25 °C, respectively. In addition, the CO₂/N₂ selectivity of NAC-650-650 is 79.93, much higher than the value of 49.77 obtained for the nonnitrogen-doped carbon AC-650-650. The CO₂ adsorption capacity of the NAC-650-650 sample maintains over 97% after ten cycles. Analysis of the results show that the CO₂ capacity of the NACs has a linear correlation (R² = 0.9633) with the cumulative pore volume for a pore size less than 1.02 nm. The presence of nitrogen and oxygen enhances the CO₂/N₂ selectivity, and pyrrole-N and hydroxy groups contribute more to the CO₂ adsorption. In situ Fourier transform infrared spectra analysis indicates that CO₂ is adsorbed onto the NACs as a gas. Furthermore, the physical adsorption mechanism is confirmed by adsorption kinetic models and the isosteric heat, and it is found to be controlled by CO₂ diffusion. The CO₂ adsorption kinetics for NACs at room temperature and in pure CO₂ is in accordance with the pseudo-first-order model and Avramís fractional-order kinetic model.     

Fabrication of azobenzene-functionalized porous polymers for selective CO2 capture

Many solid adsorbents have been prepared for the CO₂ capture. In particular, the photoresponsive adsorbents have attracted extensive interests because of their tunable pore structure and variable responsive behaviors provoked by the external light. However, it is challenging to fabricate the photoresponsive adsorbents featured the big CO₂ capacity and high CO₂ selectivity. Herein, copolymerized between 4-phenylazobenzoyl chloride, 2,4,6-trichloro-1,3,5-triazine and melamine, a series of azobenzene-functionalized porous polymers (PTM-AZOs) are successfully synthesized. The PTM-AZOs are verified in possession of proper pore structures, large surface area and photoconductive properties through a series of characterization. The PTM-AZO-2 with the trans-isomerization exhibits the best CO₂ adsorption amount of 2.7 mmol·g^-1 (273 K and 0.1 MPa), while the CO₂/N₂ selectivity can reach 2459 and 607 on the trans- and cis-isomerization, respectively. The regulatable pore structures controlled by the photoresponsive azobenzene groups affect the CO₂ capture performance of the PTM-AZOs.     

Amine-immobilized HY zeolite for CO2 capture from hot flue gas

Solid amine-based adsorbents were widely studied as an alternative to liquid amine for post-combustion CO₂ capture (PCC). However, most of the amine adsorbents suffer from low thermal stability and poor cyclic regenerability at the temperature of hot flue gases. Here we present an amine loaded proton type Y zeolite (HY) where the amines namely monoethanolamine (MEA) and ethylenediamine (ED) are chemical immobilized via ionic bond to the zeolite framework to overcome the amine degradation problem. The MEA and ED of 5%, 10% and 20% (mass) concentration – immobilized zeolites were characterized by X-ray diffraction, Fourier-transform infrared spectroscopy, and N₂ -196 ℃ adsorption to confirm the structure integrity, amine functionalization, and surface area, respectively. The determination of the amine loading was given by C, H, N elemental analysis showing that ED has successfully grafted almost twice as many amino groups as MEA within the same solvent concentration. CO₂ adsorption capacity and thermal stability of these samples were measured using thermogravimetric analyser. The adsorption performance was tested at the adsorption temperature of 30, 60 and 90 ℃, respectively using pure CO₂ while the desorption was carried out with pure N₂ purge at the same temperature and then followed by elevated temperature at 150 ℃. It was found that all the amine@HY have a substantial high selectivity of CO₂ over N₂. The sample 20% ED@HY has the highest CO₂ adsorption capacity of 1.76 mmol·g^-1 at 90 ℃ higher than the capacity on parent NaY zeolite (1.45 mmol·g^-1 only). The amine@HY samples presented superior performance in cyclic thermal stability in the condition of the adsorption temperature of 90 ℃ and the desorption temperature of 150 ℃. These findings will foster the design of better adsorbents for CO₂ capture from flue gas in post-combustion power plants.     

氨基修饰微孔/介孔复合材料AM-5A-MCM-41对CO2吸附分离的分子模拟

构建了氨基修饰微孔/介孔复合材料AM-5A-MCM-41的全原子模型,采用巨正则Monte Carlo（GCMC）方法研究了它的CO₂吸附分离性能,采用加权混合规则来描述氨基和CO₂分子的弱化学作用。模拟结果表明,CO₂分子优先吸附在复合材料介孔表面的氨基附近,CO₂纯气体的吸附量和吸附热有了显著提高,而N₂的吸附量和吸附热则基本不受影响。对于CO₂和N₂的混合气分离,由于复合材料对CO₂的弱化学吸附作用,显著提高了CO₂吸附量和吸附选择性,在573 K和100 kPa时CO₂/N₂的选择性达到了87.0。通过分子模拟研究可以从微观角度了解CO₂在氨基修饰的微孔/介孔复合材料中的吸附分离的细节和机理,为实验设计和合成高效CO₂吸附剂提供指导。     

Multivariate optimization of high removal of lead(Ⅱ) using an efficient synthesized Ni-based metal–organic framework adsorbent

A new metal-organic framework(MOF) with the chemical formula of [Ni_2 F_2(4,4'-Bipy)_2(H_2 O)_2](VO_3)_2·8 H_2 O was introduced to adsorb Pb(Ⅱ) with the highest capacity.The sorbent was characterized by thermogravimetric analysis(TGA),infrared spectroscopy(FT-IR),field-emission scanning electron microscopy(FESEM),energy-dispersive Xray(EDX),and elemental analysis.The optimum conditions were obtained by a face-centered central composite design(FCCD) as follows:adsorbent dosage(m)=1.2 mg, initial concentration of Pb(Ⅱ)(C)=390 mg·L~(-1),and pH=5.According to the Langmuir model(R~2=0.9999),the maximum monolayer uptake capacity of lead(Ⅱ) is 2400.7 mg·g~(-1),which is the highe st observed amount for lead(Ⅱ) adsorption.Neither of the old adsorbents for lead(Ⅱ)has the uptake capacity over 2000 mg·g~(-1).The model of pseudo-second-order describes well the process kinetics.The adsorption process of lead(Ⅱ) is independent of temperature changes.This compound can adsorb lead(Ⅱ) from tap water.In addition to introducing a new MOF with the highest uptake capacity for removal of Pb(Ⅱ) that is the outright novelty of this study,the concurrent modeling of both the removal percent(R) and the uptake capacity(q) is another important advantage.Because it achieves the more economical and favorable optimum conditions in comparison with the single optimization of each response.     

Selective extraction of In(III), Ga(III) and Zn(II) using a novel extractant with phenylphosphinic acid

A new extractant, [N,N-di(2-ethylhexyl)amino]methylphenylphosphinic acid (DEAPP), was synthesized to de-velop the mutual separation techniques of In(III), Ga(III) and Zn(II). The extraction selectivity for In(III), Ga(I I) and Zn(II) with DEAPP was higher than that of the commercial phosphorus acid extractants such as D2EHPA and PC-88A. The extraction selectivity for metal ions in 1 mol·L?1 aqueous ammonium nitrate solution with DEAPP was in the following order:In(III) N Ga(III) N Zn(II). These selective extraction behaviors indicate that the amino moiety of DEAPP plays an important role in the mutual separation of In(III), Ga(III) and Zn(II). The extraction equilibria of In(I I), Ga(II ) and Zn(II) with DEAPP (=HR) were expressed by the following reactions:In3++2eHRT2?InR3eHRT+3H+, Ga3++1.5eHRT2+NO3??GaR2eHRTeNO3T+2H+, and Zn2++2eHRT2?ZnR2eHRT 2 + 2H+. The extraction equilibrium constants of In(III), Ga(III) and Zn(II) with DEAPP were determined to be Kex,M=1.7 × 104 [dm3·mol?1], 4.17 [(dm3·mol?1)0.5], and 1.55 x 10?2 [–], respectively.     

CO2加氢制甲醇Cu-Zn-Al水滑石催化剂的改性研究

CO₂加氢制甲醇既能有效缓解温室效应带来的全球气温升高问题,也能促进CO₂的资源化利用,成为研究热点之一。对Cu-Zn-Al水滑石(CZA-LDH)开展改性研究,以Cu(NO₃)₂·3H₂O、Zn(NO₃)₂·6H₂O和Al(NO₃)₃·9H₂O为原料,以NaOH和NaCO₃为沉淀剂,采用共沉淀法制备CZA-LDH,并在制备过程中引入聚乙二醇(PEG)、聚乙烯吡咯烷酮(PVP)和三乙醇胺(TEA),焙烧后得到4组催化剂。XRD、FT-IR、N₂吸附-脱附、SEM表征结果及催化性能测试数据表明,引入TEA的CZA-LDH焙烧后得到的复合金属氧化物催化剂(CZA-LDO-TEA)表现出最优的性能。这是因为TEA 能够破坏表面晶体结构,促进催化剂中CuO组分的还原,提高了 CO₂的化学吸附能力,从而提高了催化剂的CO₂转化率。     

Co改性活性炭吸附NO的实验研究

采用Co(NO_3)_2对活性炭进行改性,考察浸渍浓度和吸附温度等条件对活性炭吸附NO性能的影响,并对已吸附NO的0.3 mol·L~(-1)的Co(NO_3)_2改性活性炭进行再生。通过BET、SEM、吸附等温线和FT-IR表征样品的比表面积、颗粒形貌和表面官能团。结果表明,当浸渍溶液浓度为0.3 mol·L~(-1)时,吸附效果最佳,80 min时吸附效率达88.90%。活性炭的吸附效率随着温度升高而降低,用0.3 mol·L~(-1)Co(NO_3)_2改性的活性炭在200℃时的吸附效率大于90%,并可持续50 min。SEM和FT-IR表征结果表明,在Co(NO_3)_2改性的活性炭表面和孔隙生成了Co_3O_4,促进NO催化氧化为NO_2并进行吸附。加热再生后的0.3 mol·L~(-1)Co(NO_3)_2改性活性炭对NO的吸附效率在60 min内仍高于88.90%,再生效果较好,可持续再生利用。     

The effect of oxygen concentration on the reduction of NO with propylene over CuO/γ-Al2O3

The effect of oxygen concentration on the pulse and steady-state selective catalytic reduction (SCR) of NO with C₃H₆ over CuO/γ-Al₂O₃ has been studied by infrared spectroscopy (IR) coupled with mass spectroscopy studies. IR studies revealed that the pulse SCR occurred via (i) the oxidation of Cu⁰/Cu⁺ to Cu²⁺ by NO and O₂, (ii) the co-adsorption of NO/NO₂/O₂ to produce Cu²⁺(NO₃⁻)₂, and (iii) the reaction of Cu²⁺(NO₃⁻)₂ with C₃H₆ to produce N₂, CO₂, and H₂O. Increasing the O₂/NO ratio from 25.0 to 83.4 promotes the formation of NO₂ from gas phase oxidation of NO, resulting in a reactant mixture of NO/NO₂/O₂. This reactant mixture allows the formation of Cu²⁺(NO₃⁻)₂ and its reaction with the C₃H₆ to occur at a higher rate with a higher selectivity toward N₂ than the low O₂/NO flow. Both the high and low O₂/NO steady-state SCR reactions follow the same pathway, proceeding via adsorbed C₃H₇---NO₂, C₃H₇---ONO, CH₃COO⁻, Cu⁰---CN, and Cu⁺---NCO intermediates toward N₂, CO₂, and H₂O products. High O₂ concentration in the high O₂/NO SCR accelerates both the formation and destruction of adsorbates, resulting in their intensities similar to the low O₂/NO SCR at 523–698 K. High O₂ concentration in the reactant mixture resulted in a higher rate of destruction of the intermediates than low O₂ concentration at temperatures above 723 K.     

Spray-drying assisted layer-structured H2TiO3 ion sieve synthesis and lithium adsorption performance

A spray-drying assisted solid-state method to prepare spherical layer-structured H₂TiO₃ ion sieve (LSTIS) particles is reported herein. The effects of synthesis parameters (calcination temperature, calcination time, and the lithium-titanium molar ratio) on adsorption–desorption performance (the delithiation ratio, titanium dissolution loss, and the adsorption capacity) were investigated. The as-prepared LSTIS exhibited an equilibrium adsorption capacity of 30.08 mg·g^-1 (average of 25.85 mg·g^-1 over 5 cycles) and ultra-low titanium dissolution loss of less than 0.12% (average of 0.086% over 5 cycles). The LSTIS showed excellent selectivity toward Li⁺ in Na⁺, K⁺, Mg²⁺, and Ca²⁺ coexisting saline solutions where its adsorption capacity reached 27.45 mg·g^-1 and the separation factors of Li⁺ over the coexisting cations exceeded 100. The data suggests that the LSTIS is promising to competitively enrich Li⁺ from saline solutions.     

Preparation of Ni/bentonite catalyst and its applications in the catalytic hydrogenation of nitrobenzene to aniline

Ni supported on bentonite was prepared by the impregnation method with different nickel contents, applied to the hydrogenation of nitrobenzene to aniline in a fixed-bed reactor, and it was characterized by X-ray diffraction(XRD), H_2-temperature programmed reduction(H_2-TPR), and X-ray photoelectron spectrometry(XPS). The results showed that Ni/bentonite catalyst with 20 wt% nickel content provided a higher conversion of nitrobenzene and selectivity of aniline compared to other catalysts. Ni O was the precursor of the active component of the catalyst, and the small crystallite size as well as the highly dispersed Ni O on the Ni/bentonite-20 catalyst, contributed to the catalytic performance. The hydrogenation of nitrobenzene was carried out at 300 °C with a H_2 gaseous hourly space velocity of 4800 ml·(g cat)~(-1)·h~(-1)and a nitrobenzene liquid hourly space velocity of4.8 ml·(g cat)~(-1)·h~(-1)over Ni/bentonite-20. A 95.7% nitrobenzene conversion and 98.8% aniline selectivity were obtained. While the nitrobenzene liquid hourly space velocity was 4.8 ml·(g cat)~(-1)·h~(-1), the yield of aniline was more than 95.0% during a 10-hour reaction.     

蛇纹石与绿矾耦合提取富镁溶液矿化二氧化碳并回收镍

蛇纹石与绿矾耦合提取镁用于矿化二氧化碳,并富集回收蛇纹石中的镍,这为处理蛇纹石和绿矾提供了一条新的路径。为得到富镁溶液,同时从溶液中分离镍,以蛇纹石与绿矾混合焙烧-浸出后得到的溶液为研究对象,采用水解沉淀法除铁,二乙基二硫代氨基甲酸钠(DDTC)络合法分离镍镁,得到镍的产物和富镁溶液并将其用于二氧化碳矿化。结果表明,该方法能够高效地去除杂质、分离镍镁。在30℃、p H为5.0条件下,铁的去除率达97.36%,而镍、镁的损失率较低。在最佳络合条件下,镍的络合率达到99.50%,而镁的损失率仅为3.03%。此外,对络合机理进行了研究,DDTC中的特征官能团是—SH,络合之后镍和铁分别以Ni[(C₂H₅)₂NCS₂]₂,Fe[(C₂H₅)₂NCS₂]₃的形式存在,而镁不会被络合。富镁溶液在80℃下矿化率达92.63%。每1 000 kg蛇纹石可固定227.38 kg的二氧化碳...     

Adsorption behavior of carbon dioxide and methane in bituminous coal: A molecular simulation study

The adsorption behavior of CO₂, CH₄ and their mixtures in bituminous coal was investigated in this study. First, a bituminous coal model was built through molecular dynamic (MD) simulations, and it was confirmed to be reasonable by comparing the simulated results with the experimental data. Grand Canonical Monte Carlo (GCMC) simulations were then carried out to investigate the single and binary component adsorption of CO₂ and CH₄ with the built bituminous coal model. For the single component adsorption, the isosteric heat of CO₂ adsorption is greater than that of CH₄ adsorption. CO₂ also exhibits stronger electrostatic interactions with the heteroatom groups in the bituminous coal model compared with CH₄, which can account for the larger adsorption capacity of CO₂ in the bituminous coal model. In the case of binary adsorption of CO₂ and CH₄ mixtures, CO₂ exhibits the preferential adsorption compared with CH₄ under the studied conditions. The adsorption selectivity of CO₂ exhibited obvious change with increasing pressure. At lower pressure, the adsorption selectivity of CO₂ shows a rapid decrease with increasing the temperature, whereas it becomes insensitive to temperature at higher pressure. Additionally, the adsorption selectivity of CO₂ decreases gradually with the increase of the bulk CO₂ mole fraction and the depth of CO₂ injection site.