Hydrocondensation of CO2 (CO) over supported iron catalysts

Hydrogenation of CO₂ was investigated on iron-copper supported catalysts. Hydrocarbons, except methane, were formed through the CO intermediate, which is formed first in the water gas-shift reaction.

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CO₂ - . CO, , , .

     

CO2 hydrogenation on iron-containing mono- and bimetallic catalysts

The effect of chemical composition of supported, ironcontaining mono- and bimetallic catalysts on the mechanism of CO₂ adsorption and hydrogenation has been studied. It is shown that at 673 K the conversion degree of CO₂ decreases in the sequence Co/Al₂O₃> Co–Ni/Al₂O₃>Ni/Al₂O₃.

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CO₂. , 673 Co/Al₂O₃> Co–Ni/Al₂O₃>Ni/Al₂O₃ .

     

铁酸镍用于热化学循环反应CO2分解制CO的研究

采用共沉淀法制备了NiFe₂O₄和NiFe₂O₄/ZrO₂催化剂,用TGA考察了其热化学法,CO₂高温分解反应性能。通过对反应前后催化剂的表征发现,反应高温使两种催化剂都发生了明显的烧结,导致在热还原反应中形成的还原态氧化物不能完全被CO₂氧化从而降低了催化剂的反应性能;ZrO₂的加入对于提高催化剂的热稳定性以及循环反应稳定性具有重要的作用。在高温反应炉中考察了NiFe₂O₄/ZrO₂的CO₂分解实验,结果表明,提高热还原温度可以提高CO产量,然而,随着循环次数的增加CO的产量降低得更明显。     

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.     

CO/H2 and CO2/H2 reactions with amorphous carbon-metal catalysts

By metal impregnation of selected naturally occurring organic materials followed by controlled carbonization, metal semicoke catalysts can be readily prepared. These catalysts have been tested in the synthesis of hydrocarbons and alcohols from CO/H₂ and CO₂/H₂ mixtures. Fe and Co preparations have been used. Relatively high temperatures are required when using these catalysts, which are quite active for synthesis using CO₂ and H₂. The pressure (5150 kPa) is very favorable both for the synthesis of liquid hydrocarbons (C₅–C₃₀) and alcohols (C₁–C₅).

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. CO/H₂ CO₂/H₂. Fe Co. , CO₂ H₂. 5150 ) (C₅–C₃₀) (C₁–C₅).

     

CO2 fixation by hydrogenation over coprecipitated Co/Al2O3

CO₂ fixation by hydrogenation over coprecipitated 36 wt.% Co/Al₂O₃ has been studied under a range of reaction conditions to clarify the effects of reaction variables and to determine the kinetics and mechanism of the reaction. A comparison of the results with those reported for CO hydrogenation on the same catalyst indicates that, although product distributions of CO₂ and CO hydrogenation differ, the kinetics and mechanism are similar.     

Direct hydrogenation of CO2 on deposited iron-containing catalysts under supercritical conditions

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改性SiO2对铁基催化剂H2、CO吸附及加氢性能的影响

采用溶胶凝胶方法通过掺杂修饰剂M（M=Mn、Zn、Zr、Sr）制备出改性SiO₂载体,再用浸渍法将Fe元素负载于该载体上制成系列催化剂。采用X射线衍射（XRD）、氮气物理吸附-脱附、X射线光电子能谱（XPS）等手段表征了催化剂的织构性质、晶相组成和电子性质。利用程序升温手段研究了催化剂的H₂还原吸附性质和CO加氢性能。借助动力学分析方法研究了催化剂与H之间的相互作用。结果表明,少量掺杂的修饰剂对催化剂的Fe物相组成以及表面Fe物种电子状态基本没有影响,但降低了催化剂的比表面积以及活性相分散度,削弱了对H₂的吸附能力,降低催化剂的H₂脱附活化能。Zn、Zr的掺杂抑制了催化剂的还原,而Mn、Sr的掺杂却促进催化剂的还原。Mn、Zn、Zr的掺杂抑制催化剂表面CO的解离吸附,Sr则促进CO的解离吸附,Mn、Zn、Zr、Sr均促进低温区间C-C耦合和加氢反应,其中,Mn、Zr促进加氢的作用更显著。     

Simultaneous oxidation of CH4 and SO2 over vanadium and palladium containing catalysts

The kinetics of deep oxidation of CH₄ and SO₂ over complex vanadium catalysts with and without palladium additives and over silica-supported palladium has been studied. Sulfur dioxide increases the rate of CH₄ oxidation, not affecting the reaction mechanism, whereas CH₄ does not effect SO₂ oxidation on the catalysts studied.

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, , . , , .

     

Influence of CO2 and H2O on methane conversion over oxide catalysts

It has been established that the introduction of CO₂ and H₂O to the reaction mixture when using freshly prepared catalysts, increases the overall methane conversion and decreases the yield of hydrocarbons. On coked MgO their effect is insignificant.

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, CO₂ H₂O . MgO CO₂ H₂O .

     

Mg掺杂In2O3-x催化剂光热催化CO2加氢

为提高光热催化CO₂加氢In₂O₃催化剂的催化活性,采用均相水热法制备Mg (OH)₂-In (OH)₃前驱体,通过高温煅烧和H₂-还原处理得到了富含氧空位的Mg掺杂In₂O_3-x(Mg-In₂O_3-x)催化剂。在300℃、常压、可见光照射条件下,CO₂加氢转化为CO的CO₂转化率可达31.20%,CO产生速率为14.22 mmol·g_cat^-1·h^-1,CO选择性为100%。相比于单一In₂O_3-x催化剂,Mg-In₂O_3-x催化剂光热催化CO₂转化率及CO产生速率明显提高,这归因于Mg成功掺杂到In₂O₃晶格中,促进In₂O₃表面氧空位的形成,进而对可见光响应效率大幅提高,并有效减缓光生电子-空穴的复合。     

Mg掺杂In2O3-x催化剂光热催化CO2加氢

为提高光热催化CO₂加氢催化剂In₂O₃的催化活性,采用均相水热法制备Mg(OH)₂-In(OH)₃前驱体,通过高温煅烧和H₂-还原处理得到了富含氧空位的Mg掺杂In₂O_3-x(Mg-In₂O_3-x)催化剂。在300℃、常压、可见光照射条件下,CO₂加氢转化为CO的CO₂转化率可达31.20%,CO产生速率为14.22 mmol·gcat^-1·h^-1,CO选择性为100%。相比于单一In₂O_3-x催化剂,Mg-In₂O_3-x催化剂光热催化CO₂转化率及CO产生速率明显提高,这归因于Mg成功掺杂到In₂O₃形晶格中,促进In₂O₃表面氧空位的形成,进而对可见光响应效率大幅提高,并有效减缓光生电子-空穴的复合。     

CH4 oxidation over palladium and vanadium containing catalysts

The kinetics of total oxidation of CH₄ over a complex vanadium catalyst with and without Pd additives and over silica-supported palladium has been studied. The addition of palladium increases the initial reaction rate but as catalysis progresses, the activity decreases to the level of an unpromoted catalyst. Palladium additives do not affect the mechanism of CH₄ oxidation.

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, , . , . .

     

On the mechanism of auto-oscillations in CO hydrogenation on supported palladium catalysts

A mechanism accounting for the occurrence of auto-oscillations in the formation rates of CH₃Cl and (CH₃)₂O during CO hydrogenation on chlorine-containing supported palladium catalysts is proposed.

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, CH₃Cl (CH₃)₂O CO .

     

CO oxidation over CuCr/Al2O3 catalysts in presence of SO2

Poisoning of variously prepared CuCr/Al₂O₃ catalysts having different compositions by sulfur dioxide has been studied. Comparative values for a decrease in the catalyst activities have been obtained.

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CO .

     

纳米Ru-Mn/ZrO2催化剂上苯选择加氢制环己烯

采用共沉淀法制备了一系列不同Mn含量的纳米Ru-Mn催化剂,考察了纳米ZrO₂作分散剂时它们催化苯选择加氢制环己烯的反应性能,并采用X射线衍射、透射电镜、N₂物理吸附、X射线荧光、原子吸收光谱和俄歇电子能谱等手段对催化剂进行了表征.结果表明,Ru-Mn催化剂上Mn以Mn₃O₄存在于Ru的表面上.在加氢过程中,Mn₃O₄可以与浆液中ZnSO₄发生化学反应生成一种难溶性的(Zn(OH)₂)₃(ZnSO₄)(H₂O)₃盐.该盐易化学吸附在Ru催化剂表面上,从而在提高Ru催化剂上环己烯选择性起关键作用.当催化剂中Mn含量为5.4%时,环己烯收率为61.3%,同时具有良好的稳定性和重复使用性能.     

协同高效的铁催化剂构建及其在CO_2加氢制高碳烃中的应用

采用物理掺杂法制备了生物质灰分作为助剂的融铁催化剂,通过X射线衍射、透射电镜、穆斯堡尔谱等方法对催化剂进行了表征,并在固定床反应器中对其CO_2加氢制高碳烃的催化性能进行了评价。结果表明,与不含生物质灰分助剂的催化剂相比,添加助剂的融铁催化剂粒径较小且尺寸分布较窄,Fe_3O_4、Fe_5C_2、Fe_3C和α-Fe四相协同共存,进而促使逆水气变换反应与C-C偶联的串联反应高效进行,在有效抑制甲烷生成的同时,可明显提升高碳烃选择性。高碳烃产物以C_(4-18)的烃类为主,在300℃、1. 0 MPa、4800 h~(-1)、H~2/CO_2=3. 0、助剂添加量为5%(质量分数)的条件下,其在烃类产物中选择性最高可达73. 9%。     

Promotion effects of alkali metals on iron molybdate catalysts for CO2 catalytic hydrogenation

CO₂ hydrogenation is an attractive way to store and utilize carbon dioxide generated by industrial processes, as well as to produce valuable chemicals from renewable and abundant resources. Iron catalysts are commonly used for the hydrogenation of carbon oxides to hydrocarbons. Iron-molybdenum catalysts have found numerous applications in catalysis, but have been never evaluated in the CO₂ hydrogenation.In this work, the structural properties of iron-molybdenum catalysts wi...     

Liquid phase hydrogenation of citral and intermediaries over Ir/TiO2/SiO2 catalysts: Kinetic study

Kinetics of the hydrogenation of citral and its intermediates over Ir/TiO₂/SiO₂ catalysts has been studied. The effect of various parameters such as the initial concentration, H₂ pressure partial, temperature and weight of catalyst were examined. A high selectivity towards unsaturated alcohols using this catalyst was demonstrated. The initial rates increased linearly with the catalyst weight. The reaction rate obeys a kinetics represented by the Langmuir–Hinshelwood model. A single site model suggesting the surface reaction as the rate determining step provided the best fit of the experimental data for the hydrogenation of citral and alcohols (geraniol, nerol and citronellol), while a dual site represent the best kinetics for the hydrogenation of citronellal.