共压直接成型法制备单腔体固体氧化物燃料电池

采用共压直接成型法制备单腔体固体氧化物燃料电池(SC-SOFC),单电池结构为Ni-YSZ/YSZ/LSM,YSZ为8%(x)Y2O3稳定的ZrO2,LSM为锰酸镧锶(La0.7Sr0.3MnO3).应用扫描电子显微镜(SEM)研究了电池微观结构,结果表明:阴极和电解质之间结合紧密,LSM在阴极YSZ三维骨架上负载性能良好;YSZ电解质薄膜厚约50μm,阳极厚约600μm,阴极层厚约100μm.研究了单电池反应温度T,阴极催化剂负载层数n,甲烷和氧气混合体积比Rmix对电池输出性能的影响规律.在T=800℃、n=2、Rmix=2时,电池性能达到最佳,开路电压为0.95V,最大电流密度为130mA·cm-2,最大功率密度为30mW·cm-2.     

乙醇在Ni-ZnO-ZrO_2-YSZ阳极SOFC上的发电性能

为考察乙醇用于固体氧化物燃料电池的可行性,用柠檬酸溶胶-凝胶制备阳极催化材料Ni-ZnO-ZrO2,利用机械混合法制备Ni-ZnO-ZrO2-YSZ(Y2O3稳定的ZrO2)阳极。用涂覆法,在YSZ电解质上,制备了Ni-ZnO-ZrO2-YSZ/YSZ/LSM(La0.85Sr0.15MnO3)与Ni-YSZ/YSZ/LSM的单体电池。在不同蒸发器操作温度、电池操作温度和乙醇蒸气流量下,以乙醇为燃料进行发电实验,对两种阳极的电池发电性能进行比较。实验结束后,用SEM检测了两种电池阳极的表面。结果表明,Ni-ZnO-ZrO2-YSZ阳极SOFC的电池输出性能明显高于Ni-YSZ阳极,且Ni-ZnO-ZrO2-YSZ阳极具有较好的抗积炭能力。     

乙醇在Ni-ZnO-ZrO2-YSZ阳极SOFC上的发电性能

为考察乙醇用于固体氧化物燃料电池的可行性,用柠檬酸溶胶 凝胶制备阳极催化材料Ni-ZnO-ZrO₂,利用机械混合法制备Ni-ZnO-ZrO₂-YSZ(Y₂O₃稳定的ZrO₂)阳极。用涂覆法,在YSZ电解质上,制备了Ni-ZnO-ZrO₂-YSZ/YSZ/LSM（La_0.85Sr_0.15MnO₃）与Ni-YSZ/YSZ/LSM的单体电池。在不同蒸发器操作温度、电池操作温度和乙醇蒸气流量下,以乙醇为燃料进行发电实验,对两种阳极的电池发电性能进行比较。实验结束后,用SEM检测了两种电池阳极的表面。结果表明,Ni-ZnO-ZrO₂-YSZ阳极SOFC的电池输出性能明显高于Ni-YSZ阳极,且Ni-ZnO-ZrO₂-YSZ阳极具有较好的抗积炭能力。     

SOFC中干甲烷浓度对Ni-YSZ阳极上反应的影响

为探讨固体氧化物燃料电池(solid oxide fuel cell, SOFC)中干甲烷浓度对反应的影响,采用色谱在线测量阳极尾气,总结阳极尾气的变化规律。在此基础上,分析干甲烷在固体氧化物燃料电池Ni-YSZ阳极上的反应,寻找干甲烷浓度与电流对电池阳极反应影响的数学关系。结果表明,随着电流密度的增加,低浓度甲烷按顺序发生CH₄+O^2- → CO+2H₂+2e^-、CH₄+2O^2- → CO+H₂O+H₂ +4e^-、CH₄+3O^2- → CO+2H₂O + 6e^-、CH₄+4O^2- → CO₂+2H₂O+8e^-反应,高浓度甲烷只发生甲烷的第一个氧化反应,中浓度甲烷发生前两个或前三个反应。依据法拉第第一定律及反应物之间的关系,确定甲烷的低、中、高浓度的判定依据分别为:q_v(CH₄)≤I/(4F)、I/(4F)≤q_v(CH₄)≤I/(2F)、q_v(CH₄)≥I/(2F)。     

梯度Cu-CeO2-Ni-YSZ复合阳极直接甲烷SOFC的制备与性能

采用三层共压-共烧结法, 并涂覆La_0.8Sr_0.2MnO₃ (LSM)阴极, 制备了梯度Ni-YSZ阳极结构的固体氧化物燃料电池(SOFC)(大孔Ni-YSZ|微孔Ni-YSZ|YSZ|LSM) (YSZ: Y₂O₃稳定的ZrO₂; LSM: Sr 掺杂的LaMnO₃).通过浸渍法在大孔Ni-YSZ 基底中沉积占总重量约1%的Cu-CeO₂抗积碳催化剂, 形成梯度Cu-CeO₂-Ni-YSZ复合阳极. 分别以CH₄和H₂为燃料, 空气为氧化剂, 测定了构造的SOFC输出电性能和长期稳定性. 结果表明,三层共压-共烧结法制备的梯度阳极SOFC, 层间结合紧密无缺陷, 阳极梯度孔结构明显, YSZ膜致密无缺陷.在850℃下操作, 以梯度Ni-YSZ 阳极制备的SOFC, 燃料由H₂切换为甲烷时, 最大功率密度由284 mW·cm^-2下降到143 mW·cm^-2; 而以Cu-CeO₂-Ni-YSZ 复合阳极构造的SOFC出现相反趋势, H₂切换为甲烷后最大输出由176 mW·cm^-2增加到196 mW·cm^-2. 在250 mA·cm^-2负荷下, 梯度Ni-YSZ阳极支撑的直接甲烷SOFC仅稳定运转10 h 便出现明显衰减, 阳极中积碳严重; 但Cu-CeO₂-Ni-YSZ 复合阳极支撑SOFC连续运转50 h, 输出电压与输出功率密度基本不变, 电镜观察不到积碳.     

双过渡层阴极对流延法制备的阳极支撑直接碳固体氧化物燃料电池性能的改善作用

采用流延法制备了阳极支撑的固体氧化物燃料电池(SOFC),电解质材料为钇稳定化氧化锆(YSZ),阳极为镍和YSZ构成的金属陶瓷(Ni-YSZ),阴极为LSCF-GDC/LSCF复合材料,同时在阴极与电解质之间制备了YSZ-GDC/GDC双过渡层。分别采用含3%的加湿H_2和活性炭为燃料,对此电池的输出性能及阻抗谱进行测试。采用加湿H_2测试的结果表明:在800℃下,采用双过渡层电池的开路电压达到1 V,最大功率密度为680 mW·cm~(-2),比未改良电池的最大功率密度(372 mW·cm~(-2))提高了83%。直接采用固体碳为燃料时,具有双过渡层阴极的电池在850℃时的开路电压达到0.95 V,最大输出功率密度达429 mW·cm~(-2),几乎比无过渡层阴极的电池(225 mW·cm~(-2))高出1倍,特别是双过渡层阴极还使直接使用碳燃料的SOFC(DC-SOFC)的燃料利用率提高了33%。     

直接甲烷固体氧化物燃料电池Ni-BZCYYb阳极抗积炭性能研究

直接以甲烷(CH₄)为燃料的固体氧化物燃料电池(Solid Oxide Fuel Cell,SOFC)具有操作系统简单、发电效率高、环境友好等优点,但传统镍基阳极使用CH₄时极易产生积炭,导致电池性能下降甚至破裂。因此,如何有效抑制积炭的产生是目前镍基阳极面临的重要挑战。本文针对传统Ni-Y_0.08Zr_0.92O_2-δ(Ni-YSZ)阳极使用CH₄时存在严重的积炭行为,采用质子导体Ba Zr_0.1Ce_0.7Y_0.1Yb_0.1O_3-δ(BZCYYb)代替氧离子导体YSZ,考查了Ni-BZCYYb对CH₄水蒸气重整反应的催化活性和抗积炭性能,同时与Ni-YSZ进行比较。以Ni-BZCYYb为阳极的SOFC,在700–600℃、湿CH₄(97%CH₄-3%H₂O)为燃...     

采用简易方法合成直接乙醇固体氧化物燃料电池海胆状Pd催化层

在室温下,通过电位置换反应在固体氧化物燃料电池的Ni-YSZ(钇掺杂氧化锆)阳极表面制备海胆状Pd催化层。该催化层的结构和性能通过SEM、XRD和电化学等表征手段进行表征。结果表明,三维纳米花状Pd催化剂是由在Ni-YSZ阳极表面形成的多条纳米棒有序的组合而成。通过在Ni/YSZ阳极表面引入该催化层,相比与传统Ni-YSZ阳极,燃料电池的最高功率和稳定性都获得了很大的提升。该研究表明,电位置换反应是一种很高效的在传统Ni-YSZ阳极表面制备纳米抗积炭的功能层的方法。     

采用简易方法合成直接乙醇固体氧化物燃料电池海胆状Pd催化层（英文）

在室温下,通过电位置换反应在固体氧化物燃料电池的Ni-YSZ(钇掺杂氧化锆)阳极表面制备海胆状Pd催化层。该催化层的结构和性能通过SEM、XRD和电化学等表征手段进行表征。结果表明,三维纳米花状Pd催化剂是由在Ni-YSZ阳极表面形成的多条纳米棒有序的组合而成。通过在Ni/YSZ阳极表面引入该催化层,相比与传统Ni-YSZ阳极,燃料电池的最高功率和稳定性都获得了很大的提升。该研究表明,电位置换反应是一种很高效的在传统Ni-YSZ阳极表面制备纳米抗积炭的功能层的方法。     

中温平板型固体氧化物燃料电池研究

采用流延法制备Ni/YSZ阳极支撑体 YSZ电解质复合膜素坯.经等静压,共烧结而得到的复合膜,其YSZ电解质层的厚度在1530μm之间,面积大于100cm2.再将由柠檬酸盐法合成的Ce0.8Sm0.2O1.9(CSO)和固相法合成的La0.6Sr0.4CoO3(LSCO)相继沉积到YSZ膜上形成有CSO中间层的复合阴极,从而构成Ni/YSZ/CSO/LSCO的中温平板型固体氧化物燃料(单体)电池,其中Ni/YSZ为阳极,CSO是中间层,LSCO为阴极.以H2作燃料气,O2为氧化气,850℃下,该单电池开路电压达1.1V,最大输出功率密度0.2W/cm2.本文还对该单电池复数阻抗谱进行了分析讨论.     

Measurements of thermal energy neon ion—neutral reaction rate coefficients and product ion distributions

Reaction rate coefficients and product ion distributions have been measured for the reaction of Ne⁺ with H₂, N₂, CO, CO₂, N₂O, CH₄, O₂, NO, NH₃, SO₂, CH₃Cl, COS, H₂O and C₂H₄ at 300 K using a selected ion flow tube (SIFT) apparatus. In most cases the major reaction channel involves dissociative ionization while for N₂, CO⁺, H₂O, CH₄ and CH₃Cl these reactions proceed mainly or exclusively by simple charge transfer. For H₂ the process is exclusively hydrogen atom abstraction. The measured rate coefficients are compared with the values given by the Langevin and average-dipole orientation theories of ion—molecule collisions. In general the reaction probability (ratio of measured rate to the Langevin or ADO rate) is greater for the dissociative ionizaton reactions, although H₂O is an exception with quite fast simple charge transfer.     

理论空燃比天然气汽车尾气中H2O和O2对CH4与NO反应的影响

共沉淀法制备CeZrYLa+LaAl 复合氧化物载体, 等体积浸渍法制备了Pt 催化剂, 用于研究理论空燃比天然气汽车(NGVs)尾气净化反应中CH₄与NO的反应规律. 并考察了10% (体积分数, φ)H₂O和计量比O₂对CO₂存在时的CH₄+NO反应的影响. 结果表明: 对于不同条件下的NO+CH₄反应, 主要生成N₂和CO₂, 高温区有CO生成. 低温区无O₂时可以生成N₂O, 有O₂时可以生成NO₂; 添加10% (φ)的H₂O后, CH₄ 转化活性降低, NO转化活性基本不变, 这是由于H₂O减弱了CH₄与CO₂的重整反应, 但是对CH₄与NO的反应基本没有影响; 添加计量比的O₂后, CH₄转化活性提高, 而NO转化活性降低, 这是由于O₂和NO之间存在竞争吸附, CH₄被O₂氧化为主要反应, 从而减弱了NO的转化; 同时添加计量比的O₂和10% (φ) H₂O, CH₄与CO₂的重整反应受到抑制,CH₄与NO的反应、甲烷蒸汽重整反应和甲烷被O₂氧化反应同时发生, CH₄和NO的转化活性均提高.     

Mechanistic Study of Partial Oxidation of Methane to Syngas over c Pd/SiO2 Catalyst

Partial oxidation of methane (POM) to make syngas has been largely studied in recent years because of its potential to reduce the cost of syngas. Two reaction schemes have been proposed for the reaction:one is the sequence of combustion of CH₄ followed by reforming of unconverted CH₄ with CO₂ and H₂O,and the other is the direct partial oxidation of CH₄ to CO and H₂ without the experience of CO₂ and H₂O as reaction intermediates. In the industrial process, if the combustion-reforming mechanism predominantly contributes to the conversion of methane to syngas, severe heat management problems have to be taken into account. Therefore, the elucidation of the reaction pathway is of vital importance. In this paper, in situ time-resolved FTIR (in situ TR-FTIR) spectroscopy was used to study the POM reaction over lwt%Pd/SiO₂. The results of catalytic performance evaluation on the POM reaction over lwt%Pd/SiO₂ under different space velocity are also presented. It is expected that the additional proof can be presented to interpret POM mechanism.     

甲烷自热重整制氢的热力学和动力学分析

对甲烷自热重整进行了系统的热力学分析,并采用预混合层流模型结合甲烷氧化、蒸汽重整、干重整机理对反应过程进行了动力学分析。结果表明,甲烷自热重整的平衡产物及其浓度主要受温度、O₂/CH₄、H₂O/CH₄的影响;压力影响不是十分明显,主要影响达到平衡的速度。在715℃~730℃、压力0.7MPa~1.0MPa,控制O₂/CH₄在0.60~0.70、H₂O/CH₄在3.15~3.25,可以得到H₂>68%、CO<10%的产物气,积炭率接近于0。动力学分析表明,自热重整过程分为两个主要阶段进行,在起始阶段主要发生甲烷氧化反应,产物主要为H₂O和CO₂;第二阶段以甲烷蒸汽重整反应为主,伴随水气变换反应（WGS）和微弱的干重整,H_2、CO和CO₂为主要产物。调节初始水浓度可以控制快速氧化阶段反应速率,避免“热点”出现,抑制CO的生成。     

NO reduction and CO oxidation over Cu/Ce/Mg/Al mixed oxide catalyst in FCC operation

Simultaneous NO reduction and CO oxidation in the presence of O₂, H₂O and SO₂ over Cu/Mg/Al/O (Cu-cat), Ce/Mg/Al/O (Ce-cat) and Cu/Ce/Mg/Al/O (CuCe-cat) were studied. At low temperatures (<340 °C), the presence of O₂ or H₂O enhanced the activity of CuCe-cat for NO and CO conversions, but significantly suppressed the activity of Cu-cat and Ce-cat. At high temperature (720 °C), the presence of O₂ or H₂O had no adverse effect on the NO and CO conversions over these catalysts. The addition of SO₂ to NO+CO+O₂+H₂O system had no effect on the reaction of CO+O₂ over Cu-cat, but deactivated this catalyst for NO+CO and CO+H₂O reactions; over Ce-cat, all of these reactions of NO+CO,CO+O₂ and CO+H₂O were suppressed significantly; over CuCe-cat, NO+CO and CO+O₂ reactions were not affected while the reaction of CO+H₂O was slightly inhibited.     

Four Coordination Polymers Assembled with a New Biscarboxyl-functionalized Schiff Base Ligand

Based on a new biscarboxyl-functionalized Schiff base ligand 1,2-cyclohexanediamino-N,N'-bis[3-methoxyl-5-(p-carboxyl-phenylazo)] salicylidene(H₄L), four polymers,[(CH₃)₂NH₂]₂·[Mn₃(L)₂(H₂O)₄]·2DMF(CP1),[Fe₂(L)(H₂O)(DMF)](CP2),[(CH₃)₂NH₂]·[Cu(HL)]·H₂O(CP3) and[Ni₂(L)(teta)]·2DMF·H₂O(CP4), have been synthesized(teta=5,5,7,12,12,14-hexamethyl-1,4,8,11-tetraazacyclotetradecane). In CP1, both of the internal[N₂O₂] pocket and the external carboxylate groups of L^4- anion are ligated by Mn²⁺ ions, and the structure displays a layer. In CP2, the Fe²⁺ cations are linked by L^4- anions to form a binuclear double chain. CP3 displays a[Cu₂(HL)₂] dimer. In CP4, the Ni²⁺ ions are connected by L^4- anions to form a chain. The structures are further linked by hydrogen bonds to form 2D or 3D supramolecular architectures, respectively. CP1 exhibits adsorption ability to three organic dyes.     

CeO2/Co3O4氧载体的制备及其甲烷化学链燃烧性能研究

制备了系列甲烷化学链燃烧用CeO₂/Co₃O₄复合氧载体,采用XRD、H₂-TPR、甲烷程序升温和恒温反应对氧载体进行了表征与评价。研究了不同CeO₂的负载量对复合氧载体的结构、氧化还原性、产物选择性的影响。结果表明,氧化铈的添加不仅降低了氧载体的初始反应温度,还延长了有效反应时间,但铈添加量过高会降低产物CO₂选择性,使甲烷向部分氧化进行。CeO₂(30%)/Co₃O₄氧载体在650 ℃经20次循环后甲烷转化率和CO₂选择性均未明显降低,表现出较高的活性和化学链循环稳定性。     

Ni/TiO2 Catalyst for Partial Oxidation of Methane to Syngas

Ni/TiO₂ catalyst was firstly used for the partial oxidation of methane to produce synthesis gas. The reaction was carried out in a fixed-bed continuous flow quartz reactor at atmospheric pressure. The flow rate was regulated by a mass controller with a space velocity of 1.5×10⁵ h^-1 and a CH₄/O₂ molar ratio of 2/1. Prior to the introduction of feed gas, the Ni/TiO₂ catalyst was activated in flowing H₂ at 700℃ for 30 min. TiO₂ is known to be a poor support for partial oxidation because which can easily result in complete oxidation. But at 700℃, Ni/TiO₂ catalyst exhibited a better performance than Ni/SiO₂ and Ni/ZrO₂. The conversion of methane was 81.5, and the selectivity of hydrogen and carbon monoxide were 93.4 and 89.4 respectively. After 6h of continuous reaction, the conversion of methane descended a little and then remained a steady yield on the whole,but the selectivity of H₂ and CO gradually declined, as far as to a constant. The selectivity of H₂ was always higher than that of CO and the ratio of H₂/CO wouldn't change with the increasing of reaction time.     

La3+-NaY型沸石的水热交换反应

作者根据在100℃、180℃时La³⁺-NaY型沸石交换反应等温线的测定和十三种单一稀土(Ln)元素在180℃时的交换度与相应Ln³⁺离子水合焓关系的研究以及在不同温度下交换反应速率常数、反应级数与交换反应表观活化能的测定,比较系统地研究了La³⁺-NaY型的水热交换反应,从而比较有据地提出这类交换反应的机理。