以Fe/活性炭为催化剂由甲烷和氮气合成氨

采用浸渍法制备了活性炭担载的Fe基催化剂.利用N2物理吸附、x射线粉末衍射、氢气程序升温还原等方法对载体和催化剂进行了表征.以甲烷和氮气为原料,在自制的常压连续流动式反应器中进行了直接合成氨实验.结果表明,在600～800℃之间有氨气产生,同时有乙烯、乙烷等物质生成,并且甲烷的转化速率和氨的生成速率随温度的升高而增大;...     

Development of Methane Decomposition Catalysts for CO<Subscript>x</Subscript> Free Hydrogen

Now-a-days, catalytic decomposition of methane (CDM) into hydrogen and carbon is a promising technique for production of fuel cell grade hydrogen. The Ni based catalysts seems promising particularly for the production of CO_x free H₂ by methane decomposition process. The CDM activity and longevity of the Ni based catalysts are mainly influenced by the amount of Ni and type of support material. In this paper the CDM activity results are correlated with NiO crystallite size, Ni metal surface area and acidity of the catalysts. In case of bimetallic catalysts addition of Cu to Ni catalysts lead to enhance the CDM activity at higher temperature thus resulting in the increased concentration of hydrogen in the outlet stream. Finally, some of the carbon-based catalysts are studied for methane decomposition activity at higher temperature. The surface changes over carbon catalysts with methane decomposition are studied using various characterization techniques.     

Co/Fe催化剂乙醇裂解和部分氧化制氢研究

采用共沉淀法制备的Co/Fe催化剂催化乙醇裂解和部分氧化制氢反应，考察了反应温度对两种途径反应的影响。结果发现，Co/Fe催化剂对乙醇部分氧化制氢显示出较高的氢选择性，且稳定性较好；该催化剂对乙醇裂解制氢也具有较高的氢选择性，但其稳定性很很差。XRD表征结果表明，在催化乙醇部分氧化反应后，Co70Fe30催化剂中存在CoFe合金和CoO相；而催化乙醇裂解反应后，Co70Fe30催化剂中仅存在CoFe合金，即CoFe合金可能是裂解反应的活性组分。     

气凝胶催化剂上甲烷裂解制备的碳纳米管结构特征

采用XRD、TGA、SEM、TEM、 Raman光谱等多种表征手段,考察了Al2O3气凝胶催化剂上甲烷裂解生长的碳纳米管的结构特征.制得的碳纳米管形态单一,为管径均匀、管壁光滑的中空纳米管,平均直径在10～20 nm.碳纳米管的比表面积较大,具有较强的抗氧化能力,其结构的长程有序度较石墨低.由碳纳米管的Raman光谱分析可知,碳纳米管存在碳层缺陷和无定形碳.当反应温度升高或甲烷浓度下降时,碳纳米管石墨化程度逐渐提高.     

Sm修饰的Ni-MgO催化剂制备碳纳米管的研究

Carbon nanotubes (CNTs) have been synthesized over Ni-MgO and Ni-Sm-MgO catalysts by decomposition of CH₄ at 650 ℃. The addition of Sm into Ni-MgO catalyst not only promotes the catalytic activity and lifetime of the catalyst, but also improves the graphitization and heat stability of carbon nanotubes. The yield of CNTs obtained over the Ni-10Sm-MgO catalyst reaches 33 g C·(g Ni)^-1, being more than 5 times higher than that of the Ni-MgO catalyst. XRD and TPR results of the catalysts indicate that there is a remarkable interaction of Ni with Sm species, which facilitates the reduction of nickel and restrains the Ni particles from agglomerating.     

An Ab Initio Study of N_2O Decomposition on MgO Catalyst

Nl0isalwaysusedasoxidantinalotofoxidativecatalyticprocesses,suchastheoxidativecouplingofmethane(0CM),oxidativedehydr0genationofalkanesands0on,becauseitdecomPosestoprovideOadspeciesonmetal0xidecatalystsandleadstothespecificoxidativeselectivity.Forexample,itwasf0undthatf0rOCMreacti0nonMgOandLougOcatalystS,thereactiontemPeraturerequiredislowerwhenoneusesN20asoxidantthanusing0,'.TheunderstandingofN20dec0mposihon0nmetal0xidecatalystsandthepropertiesofthereIevant0adspeciesshouldbeagoodstarting…     

甲烷在Ni/TiO_2催化剂表面的活化

考察了Ｎｉ／ＴｉＯ２催化剂甲烷部分氧化和二氧化碳重整制合成气的反应活性,实验表明,以ＴｉＯ２为载体的镍系催化剂对于甲烷部分氧化制合成气反应具有较好的活性,尤其对Ｈ２的选择性较高,对二氧化碳重整制合成气反应具有较好的低温反应活性．采用脉冲－质谱在线分析等技术,在无气相氧条件下向Ｎｉ／ＴｉＯ２催化剂脉冲ＣＨ４,发现甲烷在催化剂表面的活化（转化）及其氧化产物的选择性与金属催化剂表面氧的浓度密切相关．ＣＨ４与Ｎｉ／ＴｉＯ２催化剂作用过程中存在明显的氢溢流和氧溢流现象,可能是这种溢流效应使得Ｎ／ＴｉＯ２催化剂具有良好的反应活性和抗积碳性能．     

Ni/Al2 O3 催化剂上甲烷的分解温度和时间对积炭的影响

用在线质谱法研究了Ni/Al2O3催化剂上甲烷分解温度和时间对积炭的影响。实验结果表明：在600～800℃内甲烷在还原的Ni/Al2O3催化剂上可分解为表面碳物种（即NiXC）和氢气,这种表面碳物种在较低的温度下可扩散进入体相,在高温下可逐步转化为低活性的碳物种。在800℃下由于表面碳物种不能扩散进入体相,金属镍中心迅速被表面碳物种覆盖,导致甲烷分解反应失活。     

Iron Oxide Supported on Al2O3 Catalyst for Methane Decomposition Reaction: Effect of MgO Additive and Calcination Temperature

Production of hydrogen is a challenging task and have significant impact in the recent scenario. The alumina supported iron oxide nanoparticle synthesized using non‐ionic surfactant Triton‐X was found very effective for steady production of hydrogen through methane decomposition reaction. The high surface area, easily reducible catalyst calcined at 500 °C and 800 °C temperature showed steady activity towards methane decomposition reaction. At a higher reaction temperature there was catalyst deactivation. The doping of MgO facilitated particle growth rendering the poor catalytic activity. The TPR study showed that reducibility of TPR was difficult in presence of MgO additive. The formation of Fe? Mg? Al solid solution confirmed by XRD study was found mainly responsible for the lower catalytic activity. The bamboo‐shaped carbon nanotube formed from 20 % Fe/Al₂O₃ catalyst which is mainly because of the poor wetting property of quasi‐liquid metal and carbon nanotube.     

催化裂解甲烷制备氢气和碳纳米纤维

采用浸渍法制备了Ni/MgO与Ni/O-D(氧化金刚石)催化剂,分别研究了反应温度和空速对甲烷催化裂解转化率的影响,并利用XPS、SEM、EDS等测试技术对催化剂进行了表征. 结果表明,33Ni/O-D和41Ni/MgO分别在500与650 ℃能长时间维持其催化活性,前者在150 min内的甲烷转化率＞8%,后者则在120 min内的甲烷转化率＞25%;甲烷初始转化率随裂解反应温度升高而增大,但温度过高导致催化剂迅速失活;降低空速有利于提高甲烷的转化率,但却会降低氢气产量;甲烷裂解生成的碳产物形貌取决于载体和催化反应条件,较低温度(500和550 ℃)下,Ni/O-D表面的裂解碳呈现出纤维状,在650 ℃以上则表现为板结颗粒堆积并将Ni完全覆盖,但该温度下的Ni/MgO表面仍能形成碳纤维,并随空速降低存在直径增加的趋势.     

Ni-Co双金属催化剂上沼气重整制氢机理

用传统湿式浸渍法制备了La₂O₃掺杂的商业γ-Al₂O₃负载的沼气重整催化剂Ni-Co/La₂O₃-γ-Al₂O₃, 并用程序升温加氢(TPH)、程序升温氧化(TPO)、程序升温表面反应(TPSR)、程序升温脱附(TPD)及脉冲实验对催化剂进行了表征. 结果表明, 沼气重整过程中Ni-Co/La₂O₃-γ-Al₂O₃催化剂上的表面碳物种主要来源于CH₄的裂解, CO₂的贡献很小. CH₄裂解能够产生三种活性不同的碳物种, 即C_α、C_β与C_γ. 随着反应的进行, C_α物种减小而C_β与C_γ物种增加, 且C_γ物种能够转变为惰性的石墨碳. 重整反应过程中CH₄与CO₂的活化能相互促进. 催化剂表面的O物种与C反应生成CO或与CH_x反应生成CH_xO再分解为CO与吸附态的H物种, 可能是Ni-Co/La₂O₃-γ-Al₂O₃催化剂上沼气重整的速率控制步骤.     

Paper-like Microfibrous Nickel Catalyst for Hydrogen Production via NH3 Decomposition in Fuel Cell Applications

Recently, miniature H2 generator to power fuel cells for portable/micro electronic devices and passenger propulsion has been the focus of intense research activities1-3. One of the strategies is to find simple CO-free H2 production with novel microreactor…     

添加碱金属对甲烷与空气制合成气的催化剂性能的影响

考察了添加在镍基催化剂中的碱金属助剂 ,对甲烷与空气制合成气的催化反应性能的影响 ;并用 TPO、TPR、CO2 程序升温脱附 (TPD)、XPS及 CO脉冲色谱技术 ,对催化剂进行了表征 .实验表明 ,碱金属助剂对降低催化剂结炭有一定的作用 ,催化剂的抗积炭性能为 Ni- K2 O/Ca O- Al2 O3>Ni- L i2 O/Ca O- Al2 O3>Ni- Na2 O/Ca O-Al2 O3>Ni/Ca O- Al2 O3.在实验中发现 ,碱金属的添加 ,可使催化剂的 Ni比表面积变小、吸附 CO2 的能力增强 ,且结合能可发生不同程度的改变 .从而解释了碱土金属助剂对催化剂活性和抗积炭性的影响 .实验显示 ,Ni-L i2 O/Ca O- Al2 O3具有较好的活性和抗积炭性能     

AuPd和AgPd枝晶纳米催化剂催化甲酸分解制氢

由枝晶构成的AuPd和AgPd三维多孔泡沫薄膜在室温下分解甲酸制氢具有高催化活性。该高催化活性是由于纳米枝晶中存在大量的活性位点,如台阶、角、扭结、边缘以及合金间的电子效应。多孔泡沫膜除了具有较高的活性外,还具有其他优良的性能：在不需要有机添加剂的情况下,利用氢气泡模板法在Ti基板上可在5 min内快速沉积多孔泡沫催化剂,无需后处理便可用于催化甲酸分解制氢;通过将电沉积泡沫膜浸入或者拉出HCOOH+HCOONa溶液,可控制氢气的产生或停止;该泡沫催化剂通过去离子水清洗或者在H₂SO₄溶液中进行循环伏安扫描、干燥后就可活化重新使用。     

高Co含量的Co-Mo系列催化剂甲烷裂解制备单壁纳米碳管

制备了高Co含量的Co-Mo／γ-A12O3系列催化剂，发现此类催化剂可以在温和的反应温度下制备高质量的单壁纳米碳管．讨论了Mo组分的作用．认为Mo分散、稳定金属颗粒，促进了SWNTs的生长．同时，Mo组分的升华决定了单壁纳米碳管的生长和管径分布．这为可控地制备单壁纳米碳管提供了依据．     

阶跃升温分解法对非负载型镍催化甲烷分解活性的影响

 以乙醇为洗涤溶剂采用沉淀法制备了非负载型 Ni 催化剂, 考察了预处理过程对催化剂上 CH4 分解活性的影响. X 射线衍射及 CH4 程序升温表面反应结果表明, 降低还原温度可减小 Ni 粒子尺寸, 从而提高催化剂活性. 同时, 采用 CH4 多温度逐步分解 (多点阶跃升温分解) 法可形成较稳定的 Ni 粒子, 有效提高催化剂的活性及稳定性, 500 oC 下 CH4 初始转化率可达 8.40%, 反应 120 min 时升至 11.20%; 而在 350 和 500 oC 两点阶跃升温分解的 CH4 最高转化率只有 1.61%.     

Enhanced methane decomposition over transition metal-based tri-metallic catalysts for the production of COx free hydrogen

In this study, COx-free hydrogen production via methane decomposition was studied over Cu–Zn-promoted tri-metallic Ni–Co–Al catalysts. The catalysts have been prepared by the constant pH co-precipitation method, and the nominal Ni metal loading was fixed at 50 wt % along with other metals at 10 wt% each. The catalyst activity for methane decomposition reaction was examined in a reactor between 400 °C and 700 °C and at atmospheric pressure. Different techniques such as N₂-physisorption, X-ray diffraction, H₂-TPR SEM, TEM, ICP-MS, TGA, and Raman spectroscopy were applied to characterize the catalysts. The relation between the catalyst composition and their catalytic activity has been investigated. The controlled synthesis has resulted in a series of catalysts with a high surface area. Ni–Co–Cu–Zn–Al was the most active and productive catalyst. Various characterizations indicate that the promotional effects of Cu–Zn interaction were the critical factor in catalysts' activity and stability. Ni–Co–Cu–Zn catalyst gave the highest methane conversion of 85% at 700 °C. Zn addition improves the stability of the catalyst by retaining the active metal size during the decomposition reaction. The catalyst was active for 80 h of stability study. The rapid deactivation of the Ni–Co catalyst was due to the sintering of the catalyst at 650 °C. Moreover, carbon species accumulated during the methane decomposition reaction depend on the catalysts' composition. Zn promotes the growth of reasonably long and thin carbon nanotubes, whereas the diameter of carbon nanotubes on unpromoted catalysts was large.     

Oxidative Methylation of Toluene with Methane over K-exchanged Y Type Zeolite Catalyst Promoted with Alkali Metal Bromide and Alkali Metal Oxide

IntroductionManyresearchgroupsareconductingextensiveresearchtoreplacecrudeoil-basedchemicalswithnaturalgasandcoal-basedchemicals.Itisknownthatstyreneisoneofthemostimportantindustrialmonomers.Currently,styreneisproducedbycatalyticalkylationofbenzenewithethyleneoverA1Cl,-HClcata-lyst,followedbyoxidativedehydrogenationoftheresultantethylbenzeneoverpotassium-promotedironoxidecatalystsL'l.However,thisprocessinvolvestheutilizationofbenzeneandethylene,obtainedfromcrudeoilandpetroleumgas,whichareexp…     

Production of COx-Free Hydrogen and Few-Layer Graphene Nanoplatelets by Catalytic Decomposition of Methane over Ni-Lignin-Derived Nanoparticles

Nickel (Ni)-lignin nanocomposites were synthesized from nickel nitrate and kraft lignin then catalytically graphitized to few-layer graphene-encapsulated nickel nanoparticles (Ni@G). Ni@G nanoparticles were used for catalytic decomposition of methane (CDM) to produce COx-free hydrogen and graphene nanoplatelets. Ni@G showed high catalytic activity for methane decomposition at temperatures of 800 to 900 °C and exhibited long-term stability of 600 min time-on-stream (TOS) without apparent deactivation. The catalytic stability may be attributed to the nickel dispersion in the Ni@G sample. During the CDM reaction process, graphene shells over Ni@G nanoparticles were cracked and peeled off the nickel cores at high temperature. Both the exposed nickel nanoparticles and the cracked graphene shells may participate the CDM reaction, making Ni@G samples highly active for CDM reaction. The vacancy defects and edges in the cracked graphene shells serve as the active sites for methane decomposition. The edges are continuously regenerated by methane molecules through CDM reaction.     

Growth of Aligned Carbon Nanotubes on Large Scale by Methane Decomposition with Deactivation Inhibitor

The effects of additives containing iron or nickel during chemical vapor deposition(CVD)on the growth of carbon nanotubes(CNTs)by methane decomposition on Mo/MgO catalyst were investigated. Ferrocene and nickel nitrate were introduced as deactivation inhibitors by in-situ evaporation during CVD. The precisely controlled in-situ introduction of these inhibitors increased the surface renewal of catalyst, and therefore prevented the catalyst from deactivation.Using this method,aligned multi-walled CNTs with parallel mesopores can be produced on a large scale.