担载Ru_3（CO）_（12）－Fe_2（CO）_9混合簇的脱羰基作用和表面加氢反应

担载于ＺｒＯ２上的Ｒｕ３（ＣＯ）１２－Ｆｅ（ＣＯ）９混合簇的红外光谱表明，Ｒｕ３（ＣＯ）１２以Ｒｕ（ＣＯ）２Ｏ２表面络合物存在．混合族在真空中随温度升高而发生脱羰基作用，５００℃左右羰基完全脱掉；以Ａｌ２Ｏ３为载体者其羰基不易脱除，升高温度出现多种羰基带．混合簇中的Ｆｅ２－（ＣＯ）９极易脱羰基．担载混合簇在Ａｒ气中进行ＴＰＤＥ时，低温时以脱羰基为主，高于１５０℃时发生表面歧化反应而生成ＣＯ２；在Ｈ２气中，低温时仍以脱羰基为主，高于１５０℃时发生表面加氢反应而生成ＣＨ４．混合簇的脱羰基和表面反应能力与Ｒｕ／Ｆｅ比及载体有关．担载混合簇在ＣＯ加氢反应中以Ｒｕ（ＣＯ）２Ｏ２和分散Ｆｅ存在，还出现－ＣＨｘ多种表面物种．     

CO在负载型Ru,Co和Ru—Co金属簇催化剂上的脱附及表面加H2反应

担载于Ａｌ２Ｏ３和ＺｒＯ２上的三种金属羰基络合物在Ｈｅ气中进行程序升温分解（ＴＰＤＥ）时，其羰基发生表面岐化反应生成ＣＯ２能力的次序为ＮａＲｕＣｏ３（ＣＯ）１２＞＞Ｒｕ３（ＣＯ）１２＞＞ＣＣｏ３（ＣＯ）９。吸附于担载Ｒｕ３和Ｃｏ３上的ＣＯ在Ｈｅ气中进行程序升温脱附（ＴＰＤ）时发生表面岐化反应生成ＣＯ２。在Ｈ２气中，吸附于担载Ｒｕ３上的ＣＯ加Ｈ２生成ＣＨ４，吸附于担载Ｃｏ３上的ＣＯ却生成ＣＯ２，在担     

CO在负载型Ru、Co和Ru－Co金属簇催化剂上的脱附及表面加H_2反应

担载于Ａｌ＿２Ｏ＿３和ＺｒＯ＿２上的三种金属羰基络合物在Ｈｅ气中进行程序升温分解（ＴＰＤＥ）时，其羰基发生表面歧化反应生成ＣＯ＿２能力的次序为ＮａＲｕＣｏ＿３（ＣＯ）＿（１２）＞＞Ｒｕ＿３（ＣＯ）＿（１２）＞＞Ｃ＿３Ｈ＿７ＣＣｏ＿３（ＣＯ）＿９。吸附于担载Ｒｕ＿３和Ｃｏ＿３上的ＣＯ在Ｈｅ气中进行程序升温脱附（ＴＰＤ）时发生表面歧化反应生成ＣＯ＿２。在Ｈ＿２气中，吸附于担载Ｒｕ＿３上的ＣＯ力Ｈ＿２生成ＣＨ＿４，吸附于担载Ｃｏ＿３上的ＣＯ却生成Ｃｏ＿２，在担载ＲｕＣｏ＿３上的ＣＯ几乎完全力Ｈ＿２生成ＣＨ＿４。以ＺｒＯ＿２为载体的Ｒｕ＿３、Ｃｏ＿３和ＲｕＣｏ＿３催化剂上的ＣＯ吸附和反应能力均大于以Ａｌ＿２Ｏ＿３为载体者。吸附于以ＺｒＯ＿２为载体的ＲｕＣｏ＿３催化剂上的ＣＯ在ＴＰＤ和ＩＲ谱上并不显示ＣＯ物种的存在，分析了Ｃ＿（ａｄｓ）和Ｏ＿（ａｄｓ）物种存在的原因。根据实验结果还讨论了金属、载体对催化性能的影响和表面反应机理。     

Ni／Al2O3催化剂上CH4／CO2重整的脉冲反应研究

报道了用脉冲反应研究Ｎｉ／Ａｌ２Ｏ３催化剂上ＣＨ４／ＣＯ２重整反应的结果。脉冲反应显示，在还原的Ｎｉ／Ａｌ２Ｏ３催化剂上，ＣＨ４在６７３Ｋ就开始发生分解，并有Ｃ２Ｈ６、Ｃ２Ｈ４生成，１０２３Ｋ下，ＣＨ４几乎完全分解，单纯的ＣＯ２则很难在还原的催化剂上发生反应，在９７３Ｋ以上的高温下才会有少量Ｃ胜成ＣＯ．ＣＨＣＯ２的脉冲反应表明，当ＣＨ４在较低温度下开始分解时，ＣＯ２也会发生分解，并生成ＣＯ。脉冲反     

Kam insky型催化剂催化乙烯齐聚──二酚基二茂锆的催化作用

通过改变 Ａｌ／ Ｚｒ 比、反应温度及反应时间, 分别考察了 Ｃｐ２ Ｚｒ（ Ｏ Ａｒ）２／ Ｅ Ａ Ｏ （ Ａｒ＝ Ｃ６ Ｈ５、ｐ  Ｃ６ Ｈ４ Ｍ ｅ、ｍ  Ｃ６ Ｈ４ Ｎ Ｏ２、ｐ  Ｃ６ Ｈ４ Ｎ Ｏ２） ４ 种体系对乙烯齐聚的催化作用． 发现用 Ｃｐ２ Ｚｒ（ Ｏ Ａｒ）２ 代替 Ｃｐ２ Ｚｒ Ｃｌ２ 作为主催化剂, 对于 Ｋａｍ ｉｎｓｋｙ 型体系 Ｃｐ２ Ｚｒ Ｌ２／ Ｅ Ａ Ｏ 催化乙烯齐聚, 具有调变作用,在提高催化活性的同时, 可使低碳烯烃的选择性明显改善． 在 Ｃｐ２ Ｚｒ（ Ｏ Ａｒ）２／ Ｅ Ａ Ｏ 的４ 种催化体系中, 当酚基对位带有强吸电子基团时（ Ａｒ＝ ｐ  Ｃ６ Ｈ４ Ｎ Ｏ２）, 对乙烯齐聚的催化性能最佳．     

担体对Fe-MnO催化剂CO加氢合成烯烃性能影响的TPSR表征

考察了不同担体担载的Ｆｅ－ＭｎＯ催化剂上ＣＯ加氢合成烯烃的反应。结果表明担体直接影响低碳烯烃选择性。通过对催化剂的ＣＯ，ＣＯ／Ｈ２，Ｃ２Ｈ４等吸附的ＴＰＳＲ表征及催化剂表面ＣＯ加氢微观反应的研究，证明以碱性担体为基质的ＰＢＣ催化剂具有强吸附ＣＯ能力，且生成的烯烃不易发生二次反应，因而ＰＢＣ催化剂具有较高的烯烃选择性；以酸性担体为基质的ＰＡＣ催化剂对ＣＯ为弱吸附，对Ｈ２为较强吸附，且烯烃会发生强烈的     

不同元素对Fe/AlPO_4-5催化剂CO加氢反应性能的影响(英文)

本文考察了稀土氧化物，合金和氧化锆对ＡｌＰＯ４５载体和Ｆｅ／ＡｌＰＯ４５催化剂的影响。结果表明，Ｌａ、Ｃｅ和Ｙ稀士氧化物的引入可有效地促进硝酸铁丙酮溶液中制备的Ｆｅ／ＡｌＰＯ４５催化剂在ＣＯ加氢反应中的催化活性；负载不同合金的ＡｌＰＯ４５催化剂具有明显不同的催化反应结果；ＺｒＯ可调变ＡｌＰＯ５载体的表面性能，削弱活性组份和载体间的相互作用，使在硝酸铁水溶液中制备的催化剂在合成气转化中具有一定的催化活性。     

铑基CO加氢制乙醇催化剂的FTIR研究

用ＦＴＩＲ的Ｒｈ／ＣｅＯ２／ＳｉＯ２系列ＣＯ加氢制乙醇催经剂进行了研究，在Ｈ２流中升温处理时，吸附ＣＯ的脱附温度低于Ｎ２气流中ＣＯ的脱附温度，ＣｅＯ２的加入进一步降低了Ｎ２和Ｈ２气流中ＣＯ的脱附温度，在Ｈ２气流中升温处理时，相邻双羰基峰的低波数峰迅速消失，而高波数峰变得不对称，ＦＴＩＲ结果表明，在ＣＯ加氢反应中，催化剂表面上生成了Ｒｈ（Ｈ）ＣＯ物种，反应的速度决定步骤很可能是这一物种的进一步反应，     

H2,CO和H2/CO在ZrO2催化剂上吸附行为研究

用ｉｎ ｓｉｔｕＦＴＩＲ法研究了Ｈ２、ＣＯ及ＣＯ／Ｈ２在ＺｒＯ２表面的吸附行为。结果表明,Ｈ２在ＺｒＯ２表面吸附存在两种形态的羟基（即ＺｒＯＨ和ＺｒＯＨＺｒ）,吸附温度增加,羟基数量增加。ＣＯ在２００℃易与ＺｒＯ２表面羟基作用形成甲酸盐物种,吸附温度升高时,该物种逐渐分解生成ＣＯ和ＺｒＯＨ。当ＣＯ和Ｈ２共存时,表面甲酸盐的量明显增加,并随温度增加,逐渐加氢形成甲氧基,最后生成甲烷。甲氧基的加氢过程     

Fe—Silicalite—2催化剂表面CO2加氢反应性能的研究

研究了Ｆｅ／Ｓｉｌｉｃａｌｉｔｅ－２催化剂ＣＯ２加氢低碳烯烃反应性能，利用ＣＯ２－ＴＰＤ，ＣＯ２／Ｈ２－ＴＰＳＲ和ＣＯ／Ｈ２－ＴＰＳＲ表征手段，考察了铁含量及ＭｎＯ助剂对Ｆｅ／Ｓｉｌｉｃａｌｉｔｅ－２催化剂ＣＯ２吸附脱附及加氢反应性能的影响，表明随铁含量增加可提高催化剂对ＣＯ２的吸附能力，有利于提高ＣＯ２加氢反应的转化率。     

聚甲基丙烯酸甲酯的燃烧特性以及CO和CO2的生成机理

采用质谱，色谱和锥形量热仪研究了自由基聚合的聚甲基丙烯酸甲酯（PMMA）燃烧过程中CO和CO2的生成机理及恒温条件下的燃烧情况，结果表明，在有氧条件下，自由基聚合的PMMA的解聚方式有三种，除了链末端的双键断裂和主链上的无规则C－C键的断裂外，还存在侧链酯基的断裂，其主要产物为CO2和CH3OH；在燃烧过程中，单体MMA的氧化主要的耗氧反应，其产物为CO2和少量的CO，并且CO2和CO的产率与反应温度以及样品的厚度基本无关，通过耗氧量估算得出，PMMA在空气中燃烧反应的热效应大约为22．9MJ/kg。     

色谱法同时测定羰化反应尾气中的O2、CO、CO2

提出用特制活性炭填充柱分离,热导检测器检测,以外标法定量,同时测定O2、CO、CO2。探讨了该方法的校正因子、各组分的线性相关性及微量氧气的分离和定量等。在选定的色谱条件下,O2与CO的分离度达1．7,各组分的相对标准偏差＜O．18％,绝对误差＜0．04％。     

CO oxidation over supported Pt clusters at different CO coverage

CO adsorption and oxidation over supported Pt₁₄ with different CO coverage on TiO₂(110) surface were investigated using density functional theory (DFT) calculations and thermodynamic analysis. According to the phase diagram, Pt₁₄/TiO₂(110) and 11CO@Pt₁₄/TiO₂(110) were chosen to represent the low and high CO coverage of Pt clusters, respectively. Our study shows that the high coverage of CO can induce the structural change of supported Pt clusters and weaken the interaction between Pt clusters and TiO₂ support. The CO adsorption and oxidation mechanism depends on the CO coverage, which is determined by the experimental reactant composition, pressure, and temperature. At low CO coverage, the dissociated oxygen is active specie to form CO₂ by reacting with CO. At high coverage, the molecular oxygen can directly react with CO via the formation of OOCO intermediate. Our proposed mechanisms provide useful information for understanding the CO oxidation over Pt clusters with different CO coverage. © 2016 Wiley Periodicals, Inc.     

Effect of CO2 adsorbents on the Ni-based dual-function materials for CO2 capturing and in situ methanation

The present work studied the effect of different carbon dioxide (CO₂) adsorbents on Ni-based dual-function materials (DFMs) for the development of carbon capture and on-site utilization in a reactor at isothermal condition. The DFMs containing Ni functioning as a methanation catalyst with various CO₂ adsorbents (i.e., CaO, MgO, K₂CO₃, or Na₂CO₃) were prepared on γ-Al₂O₃ through sequential impregnation. The result indicated that Ni-Na₂CO₃/γ-Al₂O₃ had the highest methanation capacity (i.e., 0.1783 mmol/g) and efficiency (i.e., 71.09%) in the CO₂ adsorption–methanation test. The CO₂ uptake and the subsequent methanation capacity of the Ni-Na₂CO₃/γ-Al₂O₃ increased to more than 24 times and more than 17 times, respectively, compared to Ni/γ-Al₂O₃. The high methanation capacity was correlated to its highest amount of weak basic sites, substantial CO₂ capture capacity and capture/release efficiency, and reactivity to H₂ at a lower temperature, supported by CO₂-TPD, TGA analyses for adsorption or adsorption–desorption at the isothermal condition, and H₂-TPRea, respectively. A continuous cyclic CO₂ adsorption–methanation was performed by using the Ni-Na₂CO₃/γ-Al₂O₃ and Ni-CaO/γ-Al₂O₃, showing that the CO₂ adsorption capacity was stabilized from third cycle onward, whereas the methanation capacity was stabilized at all cycles, indicating the high stability of the DFMs for both CO₂ adsorption and subsequent methanation. This work demonstrated successful synthesis of the Ni-based, low-cost, and stable DFMs with the ability to produce methane via the direct capture of CO₂.     

CO在CeO2(111)表面的吸附与氧化

采用密度泛函理论计算了CO在CeO2(111)表面的吸附与氧化反应行为. 结果表明, O2在洁净的CeO2(111)表面为弱物理吸附, 而在氧空位表面是强化学吸附, 且O2分子活化程度较大, O—O键长为0.143 nm. CO在CeO2(111)表面吸附行为的研究表明, CO在洁净表面及氧空位表面上为物理吸附, 吸附能均小于0.42 eV; 当表面氧空位吸附O2后, CO可吸附生成二齿碳酸盐中间体或直接生成CO2, 与原位红外光谱结果相一致. 表面碳酸盐物种脱附生成CO2的能垒仅为0.28 eV. 计算结果表明, 当CeO2表面存在氧空位时, Hubbard参数U对CO吸附能有一定的影响. CeO2载体在氧化反应中可能的催化作用为, 在氧气氛下, CeO2表面氧空位吸附O2分子, 形成活性氧物种, 参与CO催化氧化反应.     

Efficient CO2 Removal for Ultra‐Pure CO Production by Two Hybrid Ultramicroporous Materials

Removal of CO₂ from CO gas mixtures is a necessary but challenging step during production of ultra‐pure CO as processed from either steam reforming of hydrocarbons or CO₂ reduction. Herein, two hybrid ultramicroporous materials (HUMs), SIFSIX‐3‐Ni and TIFSIX‐2‐Cu‐i , which are known to exhibit strong affinity for CO₂, were examined with respect to their performance for this separation. The single‐gas CO sorption isotherms of these HUMs were measured for the first time and are indicative of weak affinity for CO and benchmark CO₂/CO selectivity (>4000 for SIFSIX‐3‐Ni ). This prompted us to conduct dynamic breakthrough experiments and compare performance with other porous materials. Ultra‐pure CO (99.99 %) was thereby obtained from CO gas mixtures containing both trace (1 %) and bulk (50 %) levels of CO₂ in a one‐step physisorption‐based separation process.     

Computational Exploration of Mechanistic Avenues in Metal-Free CO2 Reduction to CO by Disilyne Bisphosphine Adduct and Phosphonium Silaylide

Recent years have seen a growing interest in metal-free CO₂ activation by silylenes, silylones, and silanones. However, compared to mononuclear silicon species, CO₂ reduction mediated by dinuclear silicon compounds, especially disilynes, has been less explored. We have carried out extensive computational investigations to explore the mechanistic avenues in CO₂ reduction to CO by donor-stabilized disilyne bisphosphine adduct ( R1^M ) and phosphonium silaylide ( R2 ) using density functional theory calculations. Theoretical calculations suggest that R1^M exhibits donor-stabilized bis(silylene) bonding features with unusual Si−Si multiple bonding. Various modes of CO₂ coordination to R1^M have been investigated and the coordination of CO₂ by the carbon center to R1^M is found to be kinetically more facile than that by oxygen involving only one or both the silicon centers. Both the theoretically predicted reaction mechanisms of R1^M and R2 -mediated CO₂ reduction reveal the crucial role of silicon-centered lone pairs in CO₂ activations and generation of key intermediates possessing enormous strain in the Si−C−O ring, which plays the pivotal role in CO extrusion.     

Origin of Thermal and Hyperthermal CO2 from CO Oxidation on Pt Surfaces: The Role of Post‐Transition‐State Dynamics,Active Sites,and Chemisorbed CO2

The post‐transition‐state dynamics in CO oxidation on Pt surfaces are investigated using DFT‐based ab initio molecular dynamics simulations. While the initial CO₂ formed on a terrace site on Pt(111) desorbs directly, it is temporarily trapped in a chemisorption well on a Pt(332) step site. These two reaction channels thus produce CO₂ with hyperthermal and thermal velocities with drastically different angular distributions, in agreement with recent experiments (Nature, 2018 , 558, 280–283). The chemisorbed CO₂ is formed by electron transfer from the metal to the adsorbate, resulting in a bent geometry. While chemisorbed CO₂ on Pt(111) is unstable, it is stable by 0.2 eV on a Pt(332) step site. This helps explain why newly formed CO₂ produced at step sites desorbs with far lower translational energies than those formed at terraces. This work shows that steps and other defects could be potentially important in finding optimal conditions for the chemical activation and dissociation of CO₂.     

Electrocatalytic CO2 Reduction with a Half‐Sandwich Cobalt Catalyst: Selectivity towards CO

We present herein a Cp*Co(III)‐half‐sandwich catalyst system for electrocatalytic CO₂ reduction in aqueous acetonitrile solution. In addition to an electron‐donating Cp* ligand (Cp*=pentamethylcyclopentadienyl), the catalyst featured a proton‐responsive pyridyl‐benzimidazole‐based N,N‐bidentate ligand. Owing to the presence of a relatively electron‐rich Co center, the reduced Co(I)‐state was made prone to activate the electrophilic carbon center of CO₂. At the same time, the proton‐responsive benzimidazole scaffold was susceptible to facilitate proton‐transfer during the subsequent reduction of CO₂. The above factors rendered the present catalyst active toward producing CO as the major product over the other potential 2e/2H⁺ reduced product HCOOH, in contrast to the only known similar half‐sandwich CpCo(III)‐based CO₂‐reduction catalysts which produced HCOOH selectively. The system exhibited a Faradaic efficiency (FE) of about 70% while the overpotential for CO production was found to be 0.78 V, as determined by controlled‐potential electrolysis.