铈基复合氧化物中晶格氧用于甲烷部分氧化制合成气

采用共沉淀法制备了Ce-M-O氧载体（M＝Fe、Mn、Cu）,并进行了XRD表征。研究了Ce-M-O中晶格氧部分氧化甲烷制合成气的反应。考察了再生时间、再生温度对氧载体部分氧化甲烷性能的影响。研究结果表明, Ce-Fe-O固溶体中的晶格氧适于部分氧化甲烷制合成气。在新鲜的Ce Fe O氧载体上存在少量的强氧化物种,导致开始阶段大部分甲烷被完全氧化,然后该氧载体能均匀地释放出具有高选择性的体相晶格氧将甲烷氧化为CO和H2。通过对氧载体再生条件的控制,可以有效提高目标产物的选择性,当再生温度为850℃,再生时间为7min时, 获得了最大的CO（96.68%）和H2（97.56%）选择性,同时H2与CO摩尔比达到2.02。在无气相氧存在下,用Ce-Fe-O中晶格氧实现甲烷部分氧化制合成气的方法是可行的。     

Ni基催化剂上CH~4部分氧化反应的研究

本文研究了NiO/SiO~2, NiO/Al~2O~3, NiO/La~2O~3催化剂的晶相组成及其还原性质。考察了催化剂的活性、选择性、稳定性。讨论了负载型催化剂稳定性较高的原因和发生部分氧化反应时CH~4的活化过程。     

Catalytic conversion of methane to methanol over Cu-mordenite

Methane can be converted to methanol over copper-exchanged mordenite at 200 °C. Methanol could be recovered at the end of the reactor. This multi-step reaction opens the possibility for methane to methanol conversion in a closed catalytic cyclic reaction system.     

Oxidative conversion of methane to syngas on metallic Ni monolith with Mg promotion

A MgO-promoted metallic nickel monolith was prepared from nickel sponge by sintering, acid treating and loading. The catalytic performances on the monolithic catalysts, unpromoted and promoted by MgO, were studied in the partial oxidation and oxidative steam and CO₂ reformings of methane to syngas.     

Ni-Mg-ZrO2催化剂上煤层甲烷三重整制合成气

采用共沉淀法制备Ni-ZrO₂和Ni-Mg-ZrO₂催化剂,用BET、XRD、H₂-TPR、CO₂-TPD等技术对催化剂进行了表征。采用固定床流动反应装置,研究了催化剂在煤层甲烷三重整制合成气反应中的催化性能;考察了反应温度和原料气体组成对反应的影响。实验结果表明,Ni-Mg-ZrO₂催化剂在反应温度800℃、常压、空速为30 000 mL/(g·h)、CH₄/CO₂/H₂O/O₂/N₂=1.0/0.45/0.45/0.1/0.4的条件下,CH₄转化率为99%,CO₂转化率为65%左右,生成合成气H₂/CO体积比为1.5,并在58 h的实验中催化剂活性和稳定性良好。这主要归因于催化剂中金属和载体之间的强相互作用、催化剂的高热稳定性和强碱性。此外,较高的反应温度有利于甲烷三重整反应的进行;通过调节原料气组成,可以获得不同H₂/CO体积比的合成气。     

Effect of the oxidizing capacity of ceria-based support on the conversion of methane to syngas

Ceria-based solid solutions have been proposed as catalytic supports for the conversion of methane to syngas. Control of oxygen vacancies in vacancy-rich oxides represents a promising way to stable catalysts with improved activity.     

Hydrogen and syngas production from two-step steam reforming of methane using CeO2 as oxygen carrier

CeO2 oxygen carrier was prepared by precipitation method and tested by two-step steam reforming of methane (SRM). Two-step SRM for hydrogen and syngas generation is investigated in a fixed-bed reactor. Methane is directly converted to syngas at a H2/CO ratio close to 2 : 1 at a high temperature (above 750 °C) by the lattice oxygen of CeO2; methane cracking is found when the reduction degree of CeO2 was above 5.0% at 850 °C in methane isothermal reaction. CeO2?δ obtained from methane isothermal reaction can split water to generate CO-free hydrogen and renew its lattice oxygen at 700 °C; simultaneously, deposited carbon is selectively oxidized to CO2 by steam following the reaction (C+2H2O→CO2+2H2). Slight deactivation in terms of amounts of desired products (syngas and hydrogen) is observed in ten repetitive two-step SRM process due to the carbon deposition on CeO2 surface as well as sintering of CeO2.     

甲烷部分氧化制合成气Pt-Ni/Al~2O~3催化剂的研究

研究了Ni/Al~2O~3,Pt/Al~2O~3和一系列Pt-Ni/Al~2O~3催化剂对甲烷部分氧化制合成气的催化作用,发现Pt-Ni/Al~2O~3催化剂显示了比Ni/Al~2O~3和Pt/Al~2O~3更高的活性和稳定性。H~2-TPR,CO-TPD,CO~2-TPD,SEM,XPS和XRD等结果证明:Pt和Ni之间存在较强的相互作用,Pt和部分Ni形成固溶体合金并且Pt在催化剂表面富集。Pt和Ni之间的相互作用提高了催化剂的活性和稳定性,甲烷在Pt-Ni/Al~2O~3上的催化部分氧化具有不同于在Pt/Al~2O~3和Ni/Al~2O~3上的反应性能。     

Highly selective conversion of methane to ethanol over CuFe2O4-carbon nanotube catalysts at low temperature

Conversion of methane into liquid alcohol such as ethanol at low temperature in a straight, selective and low energy consumption process remains a topic of intense scientific research but a great challenge. In this work, Cu Fe₂O₄/CNT composite is successfully synthesized via a facile co-reduction method and used as catalysts to selectively oxidize methane. At a low temperature of 150 °C, methane is directly converted to ethanol in a single process on the as-prepared CuFe     

Ce-Fe-Zr-O/MgO整体型氧载体用于化学链部分氧化甲烷制合成气

以MgO为载体,采用球磨法制备了Ce-Fe-Zr-O/MgO粉末状氧载体,进而采用挤压成型法制备了整体型氧载体。研究了两种氧载体化学链部分氧化甲烷制合成气的性能,并通过XRD、H₂-TPR对氧载体进行表征。结果表明,粉末状氧载体中的储氧组分以Ce-Fe-Zr-O固溶体形式存在,而整体型氧载体的制备过程会导致Zr、Fe游离氧化物的形成。粉末状氧载体和整体型氧载体上均存在表面晶格氧和体相晶格氧,其中,体相晶格氧具有高选择性氧化甲烷的性能,可以将甲烷转化成CO和H₂。粉末状氧载体与甲烷反应活性较高,但其存在高含量的表面氧,易导致甲烷的完全氧化。整体型氧载体上体相晶格氧占据优势,可将甲烷选择性氧化为CO和H₂。氧化还原循环实验表明,粉末状氧载体在还原反应发生短时间内容易引起甲烷裂解导致产物气中的H₂/CO物质的量比显著大于2.0,同时产生大量积炭,制约了其循环性能。而整体型氧载体经10次循环实验后,全程反应过程中合成气H₂/CO物质的量比一直维持在2.0附近,显示了较高的循环稳定性能。     

氧化锆催化合成气直接转化制芳烃

采用共沉淀法和水热法制备了三种不同粒径、不同结构的纳米氧化锆催化剂,借助XRD、TEM、Raman光谱、N_2物理吸附、XPS、NH_3-TPD表征了催化剂的物理化学性质,并研究了其合成气催化转化性能。在400℃、3 M Pa、空速500 m L/(gcat·h)、进料组成H_2/CO/Ar(体积比)为5∶5∶1时,氧化锆能够一步催化合成气转化为高辛烷值烃类产物,主要是异构烯烃、环状烯烃及芳烃。在烃类产物中,C_(5+)选择性高达48%,C_(5+)中芳烃含量为30%-53%。结果表明,单斜相氧化锆比四方相更有利于CO转化,其中,比表面积较大、酸量较大的小粒径氧化锆表现出最高的CO转化率及产物收率;而大晶粒单斜相氧化锆表现出最高的芳烃选择性,这与其较高的酸性位密度相对应。因此,CO转化在Zr O_2催化剂上是酸催化反应,酸量影响催化剂的活性,而酸性位密度是影响芳烃等较大分子量产物生成的主要因素。     

Kinetics of methane conversion over microspherically grained nickel-alumina catalysts

Kinetics of methane conversion in a fluidized bed of microspherically grained nickel-alumina catalyst has been studied at pressures from 0.3 to 3.1 MPa. The rate equation shows that the reaction is inhibited by H₂O.

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0,3 3,1 . , .

     

Microwave effect on partial oxidation of methane to syngas

In this paper the results of the partial oxidation of methane over Ni-based and Co-based catalysts activated by two different heating modes (conventional and microwaves) are reported. Compared with a conventional heating mode, the temperature of the catalytic bed is much lower and there is a higher selectivity of CO and H₂ with microwave irradiation.     

ZIF-8衍生ZnO耦合HZSM-5一步催化合成气制烃醚燃料

通过水热溶剂法合成有机骨架结构材料ZIF-8,以其为前驱体调变焙烧温度制备ZnO纳米粒子。采用XRD、TEM、XPS、Raman等表征研究ZnO的组成结构及晶粒粒径形态变化;将ZnO与HZSM-5耦合形成双功能催化剂,考察其在合成气转化中的催化活性。结果表明,焙烧温度对ZnO的颗粒粒径结构影响较大,温度影响晶粒的形成速率,提高温度会促进ZnO的聚集; ZIF-8衍生ZnO通过调变温度影响ZnO晶粒粒径,起到改变产物分布的作用。当焙烧温度≤450℃时,以碳包覆ZnO纳米粒子结构存在,ZnO晶粒粒径小于20 nm,含碳ZnO耦合HZSM-5催化剂的产物以二甲醚为主;当温度≥500℃,以纯相ZnO存在,ZnO晶粒粒径皆大于20 nm,ZnO耦合HZSM-5催化剂的产物以烃类为主。ZnO与HZSM-5的耦合方式对双功能催化剂的产物选择性有显著影响。     

镍基中空纤维催化剂实现甲烷高效电催化转化

随着天然气以及页岩气为代表的非常规天然气的大规模开采,甲烷作为化工原料的直接转化利用受到了越来越多的关注.然而,甲烷分子具有极其稳定的正四面体结构,其物理化学性质非常稳定,如具有高达439 kJ/mol的C-H键能、极弱的电子亲和力、相当大的离子化能量和低的极化率,这都使得甲烷分子C-H键的活化相当困难.如何实现甲烷直接高效催化转化被誉为催化领域的'皇冠式'课题.与经甲烷重整制合成气,然后通过F-T合成获取化学品的间接转化法相比,甲烷直接转化无论在物料、能量转换效率还是在设备成本、环境保护等方面都有着非常明显的优势.以甲烷氧化偶联以及非氧化偶联(如无氧芳构化等)为典型代表的甲烷直接转化研究不断取得突破,但其各自都存在一定的局限性.相比于热催化转化路径,电催化转化路径在许多方面存在着十分明显的优势:(1)反应条件温和,甚至在常温常压条件下也能实现甲烷电催化转化反应的发生;(2)可调控程度高,仅需调节关键实验参数如电压和电流等,就能实现对反应过程热力学以及动力学的调控;(3)能够利用可再生电能驱动甲烷转化反应的发生,可将低品阶的电能转化并存储为化学能.本文采用Ni中空纤维作为基底,在其表面构筑NiO活性层,将NiO@Ni中空纤维作为电极,实现了常温常压条件下的甲烷电催化转化.通过X射线衍射、扫描电镜、透射电镜等表征手段,确定了中空纤维特有的多孔三维结构、气体传输规律、NiO活性层分布状态等物化性质.通过电化学交流阻抗与循环伏安等测试手段,获得了电荷传递、电化学活性比表面积等电化学性质.恒电压电氧化甲烷研究发现,1%NiO@Ni中空纤维具有最优的催化活性,分别在1.44 V与1.46 V(vs.RHE)电势下获得54%的甲醇法拉第效率和85%的乙醇法拉第效率.     

Hydrogen production by conversion of methane over nickel-supported USY-type zeolite catalysts

Hydrogen production by conversion of methane over Ni-supported zeolite catalysts was investigated, and Ni-supported USY-type zeolite (Si/Al₂ = 14.0, 360) was found to have longer catalytic lifetime than Ni-supported silica (Cab-O-Sil) catalyst, which had been reported to have the longest catalytic lifetime for this reaction.     

核壳结构催化剂Cr-Zn@SiO2@SAPO-34催化合成气直接转化制低碳烃的性能

合成气直接转化高选择性制烃类产物仍是巨大的挑战.本文合成了以Cr-Zn氧化物为核, SiO2为中间过渡层,再通过原位水热合成覆盖一层SAPO-34分子筛为壳的核壳结构催化剂.合成气转化反应结果显示,与纯Cr-Zn金属氧化物相比,核壳结构催化剂将产物分布由甲醇和甲烷移动至C2–C4烃(所有烃类产物中占66.9%).这表明核壳结构催化剂用于合成气一步法直接转化制液化石油气的反应具有可行性,但是催化剂结构和组成有待于进一步优化,以提高其催化反应性能.     

Direct conversion of methane to methanol over Cu exchanged mordenite: Effect of counter ions

Direct conversion of methane(CH4)to methanol(DMTM)is a promising,but very challenging process for the utilization of abundant CH4 as a low carbon resource.In this context,Cu loaded zeolites,mordenite(MOR)in particular,were recognized as the most effective system to perform DMTM.In this work,different Cu salts were used to exchange with MOR,by which the effect of counter ions on the catalytic performance towards DMTM was investigated.The prepared catalysts were characterized and evaluated systematically.It was found that the counter ions affected the speciation of Cu sites,probably due to their capability in extraction of protons from MOR and the influence on the hydrolysis state of the Cu2+in aqueous solution.These behaviors adjusted the association between Cu2+and the exchangeable protons in MOR.As a result,varied DMTM performance was observed.Among the used Cu salts,Cu(CH3COO)2 exchanged MOR showed the highest performance,achieving stable CH3 OH yield of 117±28μmol/g in 5 consecutive cycles,these values are among the highest for Cu loaded MOR zeolites in open publications.     

Microbial conversion of high-rank coals to methane

Applied Biochemistry and Biotechnology - It has been demonstrated recently that certain bacteria and fungi are capable of directly or indirectly converting low-rank coals into liquid and gaseous...