Hydrogenation of CO2

The hydrogenation of CO₂ has been studied on three different series of catalysts: Fe/MgO, Ni/Ti, Cr/Zn doped with potassium. Reaction was carried out in a conventional flow microreactor system at 15 bar at 250–350°C. Three independent competing reactions: Reverse gas-water shift (RGWS), Fischer-Tropsch (FT) and methanol synthesis were observed.

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CO₂ : Fe/MgO, Ni/Ti, Cr/Zn . 15 250–350°C. : RGWS, F.T. .

     

Hydrogenation of CO2 on Fe/carbon catalysts

The hydrogenation of CO₂ on activated carbon-supported iron catalysts has been carried out at atmospheric pressure and using a H₂/CO₂ ratio of 4. The specific activities for this reaction are lower than those obtained for the Fischer-Tropsch synthesis using the same catalysts. CO and CH₄ are the only products obtained in the hydrogenation of CO₂ under the experimental conditions used. The apparent activation energies determined for the production of CO are lower than those for the production of CH₄.

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CO₂ , , H₂/CO₂=4. , - . CO CH₄ , CO₂ . - CO , CH₄.

     

负载型CuO/TiO2催化剂催化CO2加氢制甲醇

采用浸渍法制备了CuO/TiO₂负载型催化剂,并将其用于CO₂加氢制甲醇反应。重点考察了铜的负载量对催化剂性能的影响,并对其物化性能和催化性能之间的关系进行了讨论。结果发现,随着铜负载量的增加,催化剂中金属铜的比表面先增加后减小,当铜的负载量为10%（质量百分数）时达到最大值。催化剂的表面碱性位数量随铜含量的增加持续减小,中等碱位和强碱位的强度下降。当铜的负载量不高于10%时,CO₂的转化率与铜的比表面积呈线性关系。甲醇选择性与催化剂的表面碱位性质有关,过强的碱性位会降低甲醇选择性。     

负载型CuO/TiO2催化剂催化CO2加氢制甲醇

采用浸渍法制备了CuO/TiO_2负载型催化剂,并将其用于CO2加氢制甲醇反应。重点考察了铜的负载量对催化剂性能的影响,并对其物化性能和催化性能之间的关系进行了讨论。结果发现,随着铜负载量的增加,催化剂中金属铜的比表面先增加后减小,当铜的负载量为10%(质量百分数)时达到最大值。催化剂的表面碱性位数量随铜含量的增加持续减小,中等碱位和强碱位的强度下降。当铜的负载量不高于10%时,CO2的转化率与铜的比表面积呈线性关系。甲醇选择性与催化剂的表面碱位性质有关,过强的碱性位会降低甲醇选择性。     

Fe—Zn—M／HZSM—5复合催化剂上CO2加氢性能的研究

研究了380℃、5.0MPa条件下,在Fe-Zn-M/HZSM-5(M=Cr、Al）复合催化剂上进行的CO2催化加氢的反应,考察了Fe-Zn-M中Fe含量、分子筛的硅铝比及Fe-Zn-M/HZSM-5的比率对CO2转化率和产物选择性的影响。结果表明,随着Fe含量的增加,复合催化剂的活性增强、目的产物选择性降低;Fe-Zn-M与HZSM－5间有适宜的配比;分子筛的硅铝比影响到复合催化剂的活性和选择性,随着分子筛硅铝比的降低,复合催化剂的活性增强,目的产物选择性提高。     

Ti-Si composite oxide-supported cobalt catalysts for CO2 hydrogenation

In the present work, different silica-based supported cobalt (Co) catalysts were synthesized and used for CO2 hydrogenation for methanation. Different supports, such as SSP, MCM-41, TiSSP and TiMCM were used to prepare Co catalysts with 20 wt% Co loading. The supports and catalysts were characterized by means of N2 physisorption, XRD, SEM/EDX, XPS, TPR and CO chemisorption. It is found that after calcination of catalysts, Ti is present in the form of anatase. The introduction of Ti plays important roles in the properties of Co catalysts by:(i) facilitating the reduction of Co oxides species which are strongly interacted with support, (ii) preventing the formation of silicate compounds, and (iii) inhibiting the RWGS reaction. Based on CO2 hydrogenation, the CoTiMCM catalyst exhibites the highest activity and stability.     

纳米催化剂在CO_(2)加氢制甲醇中的研究进展北大核心CSCD

为减缓温室效应,将CO_(2)转换成高附加值的甲醇是减少CO_(2)排放的有效途径,而高效催化剂是CO_(2)加氢制甲醇反应规模化的关键.可调控合成的具有量子尺寸效应的纳米催化剂在该反应上具有独特的优势.因此我们深入探讨了反应机理,综述了纳米材料在CO_(2)加氢制甲醇中的研究进展,最后给出了高效催化剂可能的发展方向.     

Deactivation of preoxidized cobalt foil studied by CO2 pulse hydrogenation

Evolution of catalytic activity on preoxidized Co-foil in CO₂ pulse hydrogenation has been characterized. The changes in catalytic activity were not fully reversible. Possible conversion of the experimental results into one general deactivation curve was shown.     

Effect of CO2 on O2 photo-adsorption on anatase

The presence of CO₂ on TiO₂ affects the process of oxygen photo-adsorption depending on the hydroxylation state of the surface. In dehydroxylated samples CO₂ blocks the formation of O ₃ ^– and O ₂ ^– . On H₂O₂/TiO₂ samples pretreated in the range of 150–200°C it leads to CO₂–O ₂ ^– species.

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, Cu(II). . .

     

CO2 reforming of methane over nickel catalysts supported on nanocrystalline MgAl2O4 with high surface area

In this paper dry reforming of methane (DRM) was carried out over nanocrystalline MgAl2O4-supported Ni catalysts with various Ni loadings. Nanocrystalline MgAl2O4 spinel with high specific surface area was synthesized by a co-precipitation method with the addition of pluronic P123 triblock copolymer as surfactant, and employed as catalyst support. The prepared samples were characterized by X-ray diffraction (XRD), N2 adsorption, H2 chemisorption, temperature-programmed reduction (TPR), temperature-programmed oxidation (TPO), temperature- programmed desorption (TPD) and transmission and scanning electron microscopies (TEM, SEM) techniques. The obtained results showed that the catalyst support has a nanocrystalline structure (crystal size: about 5 nm) with a high specific surface area (175 m2 g-1) and a mesoporous structure. Increasing in nickel content decreased the specific surface area and nickel dispersion. The prepared catalysts showed high catalytic activity and stability during the reaction. SEM analysis revealed that whisker type carbon deposited over the spent catalysts and increasing in nickel loading increased the amount of deposited carbon. The nickel catalyst with 7 wt% of nickel showed the highest catalytic activity.     

Hydrocondensation of CO2: Reaction of CO2(CO)/H2 on CuO/ZnO contact masses

The hydrocondensation of CO₂ and CO with and without added MeOH, HCHO and (CH₃)₂CHOH has been studied on CuO/ZnO contact masses in a static reactor at different pressures and reaction times.

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CO₂ CO MeOH, HCHO (CH₃)₂CHOH CuO/ZnO .

     

Study of CO2 Hydrogenation to Methanol over Cu-V/γ-Al2O3 Catalyst

The effect of vanadium addition to CU/γ-Al2O3 catalyst used in the hydrogenation of CO2 to produce methanol was studied. It was found that the catalytic performance of the Cu-based catalyst improved after V addition. The influence of reaction temperature, space velocity and the molar ratio of H2 to CO2 on the performance of 12%Cu-6%V/γ-Al2O3 catalyst were also studied. The results indicated that the best conditions for reaction were as follows: 240℃, 3600 h-1 and a molar ratio of H2 to CO2 of 3:1. The results of XRD and TPR characterization demonstrated that the addition of V enhanced the dispersion of the supported CuO species, which resulted in the enhanced catalytic performance of CU-V/γ-Al2O3 binary catalyst.     

Pd/Zn/C-N催化CO2加氢合成甲醇性能研究

利用Zn2+和2-甲基咪唑自组装形成的ZIF-8, 800℃N2氮气气氛下焙烧得到Zn/C-N载体.采用NaBH4还原法将不同含量Pd负载于Zn/C-N上焙烧后得到Pd/Zn/C-N催化剂, ICP测得Pd实际负载量为0.02%、0.05%、0.1%、0.3%.负载Pd后,由于Pd氢溢流作用, ZnO表面还原温度降低,氧空穴增加,更有利于CO2解离吸附,因此Pd负载量越高,催化剂CO2转化率越高.甲醇选择性受Pd纳米颗粒大小显著影响,小颗粒Pd与ZnO相互作用更强,更有利于甲醇生成,其中0.02%Pd/Zn/C-N催化剂在275℃, 2 MPa反应条件下, Pd/g上甲醇时空收率最高, STYMeOH值为11.0 mol/(g Pd·h).     

Intermolecular forces for D2, N2, O2, F2 and CO2

The intermolecular potentials for D₂, N₂, O₂, F₂ and CO₂ are determined on the basis of the second virial coeffincients, the polarizabilities parallel and perpendicular to the molecular axes, and the electric quadrupole moment. The repulsive parts of the potentials are taken from the corresponding Kihara core-potentials. Effects of the octopolar induction are taken into consideration in a unique way. The potential depends on relative orientations of the two molecules as well as the distance r between the molecular centers. This dependence is shown in graphs. A measure of the anisotropy of the potential depth is 0.72 for CO₂ 0.36 for D₂, and smaller than 0.27 for N₂ O₂ and F₂. The remarkable anisotropy for CO₂ and D₂ is due to strong electrostatic quadrupole interactions.     

TiO_2纳米带光催化二氧化碳甲烷化

研究了在常温常压下TiO2纳米带光催化CO2催化加氢气反应。在紫外光照射下,二氧化碳的加氢还原产物为甲烷。利用高分辨TEM,XRD,UV-Vis DRS,低温氮吸附-脱附,TG等考察了催化剂与甲烷产率的构效关系。结果表明,在600℃焙烧时得到的双晶材料具有最佳的光催化活性。优异的光催化活性主要得益于TiO2双晶脱水纳米带(DNR Bicrystalline dehydratednanoribbon)。上面形成的纳米晶界能够提高催化剂在紫外区的光吸收能力,TiO2(B)和锐钛矿独特的双晶间隔结构也提高了界面电荷分离的效率。担载贵金属Pt显著地提高了反应速率。     

PLASMA POLYMERIZATION OF ACETYLENE/CO_2/H_2

A study has been made on the plasma polymerization of acetylene/CO_2/H_2 in a capacitively coupled RF plasma. The monomer mixture yielded a crosslinked film with light brown color. A kinetic study is reported for the plasma polymer ization of acetylene/CO_2/H_2. The effects of discharge power level and reactor geometry on the rate of polymer formation are reported. The structure of the plasma polymer is investigated by IR study.     

Metastable anions of CO2

Long-lived metastable negative ions of CO₂ have been observed in the gas phase as direct products of electron and cesium collisions with organic molecules which contain “bent” CO₂ as a basic unit. The long autodetachment life-times are attributed to two related factors - first, the potential energy curve of CO⁻₂(²A₁) lies below that of CO₂(¹A₁) at 134°, and, second, an unfavorable Franck-Condon overlap exists between the bent ion (134°) and the linear neutral parent.     

CO2的光电催化还原

CO2为温室气体的主要成分,同时也是潜在的碳能源。本文主要介绍了近年来利用光催化、电催化以及光电催化3种不同催化方法还原CO2的研究现状。文章综述了催化剂材料和催化反应体系对CO2还原效果的影响。从催化效率,光、电转化效率,选择性和能耗等不同角度进行了比较和评价。细致地讨论分析了各种催化还原方法的反应机理,并对催化还原CO2研究的发展方向和应用前景进行了展望。     

CO2吸附活化的研究进展

本文分析讨论了CO₂ 在金属催化剂和金属氧化物催化剂上吸附活化的机理及活化吸附态的反应性能, 提出了CO₂ 作为一种温和氧化剂在化工生产中加以综合利用的有效途径。     

Collision-induced absorption of infrared radiation by N2, O2 and CO2

The collision-induced absorption of the symmetric vibration of CO₂ has been observed in the pure gas at densities from 20.0 to 40.0 amagat and at temperatures of 273, 298, and 323 K using infrared techniques. From the integrated intensities of the bands and using the (exp ?4) model of van Kranendonk, it is possible to deduce a value for the first derivative of the quadrupole moment with respect to the vibrational coordinate. For CO₂ the contribution from quadrupole distortion to the binary absorption coefficient is reported for several temperatures. The (exp ?4) model of van Kranendonk is used to calculate the binary absorption coefficients for the fundamental vibrational bands of N₂ and O₂ at temperatures from 70 to 340 K. The parameters λ and p/σ describing the magnitude and range of the short-range collision-induced dipole moments were determined using the known experimental absorption coefficients. The contributions from atomic distortion and quadrupole distortion to the binary absorption coefficient are calculated for N₂ and O₂.