乙酸在Rh(100)表面吸附和分散的HREELS和TDS研究

 用高分辨电子能量损失谱（HREELS）和热脱附谱（TDS）研究了乙酸在Rh（100）表面上的吸附和分解,提出了乙酸吸附和分解反应的模式．130K时,高暴露量的乙酸在Rh（100）表面上形成多层吸附的凝聚态乙酸．升温至290K时,部分乙酸以分子形式直接脱附,另一部分乙酸分子通过O—H键断裂形成乙酸根和氢吸附在表面上;在升温至400K的过程中,乙酸根在表面发生两个相互竞争的反应,即乙酸根分解成CO,CHx,O和H,以及乙酸根分解成CHx,H和CO2;升温至500K,只剩下CHx,O和CO吸附在表面上;600K后,表面吸附的CHx完全解离,同时表面吸附的碳原子和氧原子结合成CO脱附．     

乙醇在Mn薄膜／Rh（100）上吸附和分解的研究

应用高分辨电子能量损失谱（HREELS）和热脱附谱（TDS）,研究了Mn薄膜／Rh(100)上乙醇的吸附和分解,提出了表面吸附和分解的反应工,在300K时,蒸镀的Mn在清洁Rh(100)表面上以层层模式生长;在130－300K间,在25mLMn/Rh(100)表面上吸附20L乙醇的TDS结果与乙醇在Rh(100)表面上的结果一致在155K处,脱附出多层凝聚态吸附的乙醇;升温到255K,脱附出H2和CH4,继续升温,出现了与乙醇在R (100)表面上不一致的现象,在470K,同时出现了第2个H2和CH4的脱附峰,在500K,脱附极少量的CO;在950K附近,脱附出大量CO。     

铁助剂对Rh-Mn-Li/SiO2催化剂表面上的CO脱附和CO加氢行为的影响

 采用一氧化碳程序升温脱附（CO－TPD）和吸附的一氧化碳加氢程序升温表面反应（TPSR）考察了Fe助剂对Rh基催化剂上CO的脱附行为及吸附CO的加氢行为的影响．CO－TPD实验表明，在Rh／SiO2催化剂上CO有三个脱附峰．在Rh－Mn－Li／SiO2中加入0．05％Fe后，高温脱附CO比Rh／SiO2催化剂上相应的CO量大．增加Fe的负载量，CO的脱附量减少．TPSR实验中，CO加氢反应的主要产物是甲烷．不同组分的催化剂上甲烷的生成温度有如下顺序：Rh／SiO2（482K）＜Rh－Mn－Li／SiO2（489K）＜Rh－Fe／SiO2（494K）＜Rh－Mn－Li－Fe／SiO2（501K）．甲烷峰的产生伴随着CO（s）高温脱附峰的消失，说明甲烷是由强吸附的CO加氢生成的．     

复合氧化物催化剂(Cu)CeO2上硝基苯加氢反应的研究

 基于用FT－IR表征H2与硝基苯在催化剂（Cu）CeO2上的吸附和反\r\n应行为，对硝基苯加氢反应进行了研究．结果表明，氢在催化剂表面的\r\n吸附主要为解离吸附，硝基苯的吸附也主要为化学吸附；两种吸附物种\r\n在催化剂上进行表面反应生成易脱附的苯胺，避免了产物与反应物间的\r\n竞争吸附，有利于反应物完全转化．在（Cu）CeO2催化剂上，硝基苯加\r\n氢反应机理为朗格缪尔－欣谢伍德型，即表面反应为控制步骤．     

不同方法制备的Ni／ZrO2-CeO2-Al2O3催化剂对CH4-CO2重整反应的催化性能

 采用水热合成法、溶胶凝胶法和共沉淀－负载法制备了相同NiO含量的Ni／ZrO2－CeO2－Al2O3催化剂，考察了它们在CH4－CO2重整反应中的催化性能及稳定性，测定了积碳量．用CO2程序升温脱附方法测试了它们的CO2吸附性能，用H2程序升温脱附方法测试了表面Ni的分散度．结果表明，随温度升高，CH4和CO2转化率降低的顺序是：溶胶凝胶法≈共沉淀－负载法＞水热合成法，并且反应产物中n（CO）／n（H2）比随温度升高而降低．水热法和共沉淀－负载法制备的催化剂稳定性好，且前者的活性比后者高；溶胶凝胶法制得的催化剂活性较高，但易失活．积碳量大小顺序是：水热法＞溶胶凝胶法＞共沉淀－负载法．与其他方法制备的催化剂相比，水热法制备的催化剂对CO2的吸附量更大，\r\n而且积碳主要存在于载体上，从而保证了催化剂的稳定性．     

CO偶联临氢反应Pd-Fe/Al2O3催化剂的XPS研究

 利用XPS及氩离子溅射等技术对CO偶联和临氢反应中所用催化剂\r\n表面活性组分和助剂的含量及其化学状态进行了分析，并通过测定氢在\r\n催化剂表面的化学吸附，以及氢浓度对催化剂活性的影响，探讨了CO偶\r\n联反应中催化剂临氢失活的主要原因．XPS表征结果表明，CO偶联反应\r\n中催化剂活性组分以Pd0和Pd2＋形式共存；而临氢反应后仅以Pd0形式\r\n存在，助剂FeO从催化剂的内部向表面迁移且有少量Fe2＋转变为Fe3＋\r\n．催化剂临氢失活的主要原因是H2在活性组分Pd及助剂Fe（主要是FeO\r\n）表面均可形成解离吸附，形成的金属氢化物可在低活化能条件下发生\r\n迁移．这种迁移有利于副产物乙醇的生成，从而削弱了CO偶联主反应，\r\n催化剂表面活性组分Pd的相对含量减少，并几乎处于钝化状态，导致临\r\n氢反应中CO转化率、草酸二乙酯选择性及空时收率均下降．停止通入H\r\n2后，催化剂的活性可恢复至正常状态．     

天然气-二氧化碳-水蒸气-氧转化制合成气的研究: 稀土助剂的作用

 研究了稀土氧化物（CeO2和La2O3）改性的镍基催化剂中助剂的\r\n作用，并考察了催化剂对天然气－二氧化碳－水蒸气－氧转化制合成气\r\n反应的活性．结果表明，La2O3改性的镍基催化剂具有较高的CH4转化率\r\n和H2选择性；经CeO2改性的镍基催化剂具有较高的CO选择性．量子化学\r\n计算和XRD研究结果表明，La2O3助剂的加入，可使还原后催化剂表面N\r\ni（111）晶面衍射峰的强度减小，较好地符合吸附活化CH4分子的“尺\r\n寸效应”和能量要求．添加CeO2助剂的催化剂，其Ni（111）晶面衍射\r\n峰强度较大，而Ni（110）晶面含量最小，不利于CH4的离解．同时，助\r\n剂RE2O3（尤其是CeO2）和MgO提高了Ni的d电子密度，因而一定程度上\r\n加强了Nid电子向CO2空反键π轨道的迁移，促进CO2分子的活化，提高\r\n其消碳活性．     

铁助剂对Rh-Mn-Li/SiO2催化剂CO加氢制二碳含氧化物性能的影响

 采用CO加氢反应、程序升温还原（TPR）、CO吸附和CO脱附等技术，研究了Fe助剂对Rh－Mn－Li／SiO2催化剂上CO加氢合成二碳含氧化物反应的影响．结果表明，Mn，Li和Fe的加入明显提高了Rh催化剂的活性及选择性，特别是在1％Rh－1％Mn－0．075％Li／SiO2催化剂中加入0．05％Fe后，C2＋含氧化物的时空收率由331．6g／（kg·h）提高到457．5g／（kg·h）．但当Fe的加入量继续增加时，催化剂的活性及选择性下降，甲醇的选择性上升．TPR实验表明，当加入少量Fe（0．05％～0．5％）时，TPR的峰面积随Fe加入量的增大而增大，Fe的加入使Rh的还原温度向高温移动，Mn的还原温度向低温移动，Fe的还原峰与Rh和Mn的还原峰相重叠，由此推断这些Fe与Rh是处于紧密接触状态的．当Fe含量增加到1％时，样品在522K出现一个新的谱峰，该峰可归属为与Rh非紧密接触的Fe的还原峰．CO的吸附实验表明，当Fe的加入量超过一定值后，CO吸附量下降．CO的脱附实验表明，在Rh基催化剂中加入少量Fe后，强吸附的CO增多，但当Fe的加入量超过一定值时，强吸附的CO量下降．     

异戊二烯催化脱氢环氧化的研究

 合成了钼－乙酰丙酮配合物，并进行了表征，确定了其组成为M\r\noO2（acac）2．以MoO2（acac）2为催化剂，以过氧化氢为氧化剂，对\r\n异戊二烯一步脱氢环氧化制3－甲基呋喃反应进行了研究．考察了反应\r\n条件（催化剂用量、反应底物之比、温度、时间、溶剂和助剂等）对该\r\n反应的影响．结果表明，在n（cat）∶n（CH2∶C（CH3）CH∶CH2）∶\r\nn（H2O2）＝1∶100∶100，θ＝40℃，t＝6h的反应条件下，异戊二烯\r\n转化率为70．8％，3－甲基呋喃选择性为54．8％．提出了异戊二烯脱\r\n氢环氧化可能的反应机理．     

CO在Sm/Rh(100)模型表面上的吸附与反应

应用AES,LEED,XPS和TDS研究了Rh(100)上Sm膜和Sm/Rh表面合金以及CO在这两类模型表面的吸附与反应.室温下Sm在Rh(100)上的生长遵从SK模式,Sm膜经900K高温退火后可形成有序表面合金.在室温制备的Sm膜/Rh(100)表面上,室温下CO在Sm上的吸附改变了表面结构,生成SmOx和表面碳.随着Sm覆盖度的增加,低温脱附峰(α-CO)面积迅速下降,且峰温向高温方向位移;表明Sm的空间位阻和电子效应同时起作用.在Sm/Rh合金表面上,CO在约590K出现新的脱附峰,可归属为受Sm电正性修饰的Rh原子上的CO脱附峰     

Rh（100表面乙醇吸附与分解的HREELS研究

利用热脱附谱和高分辨能量损失谱技术研究了乙醇在Ｒｈ（１００）表面的吸会和分解过程，结果表明，１３０时Ｒｈ（１００）面暴露乙醇，表面首先形成化学附层，随乙醇暴露增加，表面出现多层凝聚态，表面升温至１５０Ｋ，吸附乙醇从Ｒｈ（１００）表面脱附，同时部分化学吸附乙醇分子发生羟基断裂，生成表面乙氧基，进一步升谩，表面乙氧基脱氢分解，其分解的主要途径是发生甲基脱氧，β－Ｃ与表面发生作用，生成一种含氧的金属有机     

Rh-promoted methanol decomposition on cerium oxide thin films

Methanol adsorption and reaction have been studied on Rh-deposited cerium oxide thin films under UHV conditions using temperature-programmed desorption and synchrotron soft X-ray photoelectron spectroscopy. The methanol behavior was examined as a function of the Ce oxidation state, methanol exposure, and Rh particle size and coverage. When Rh nanoparticles were deposited on the ceria films, methanol decomposed on Rh to CO and H below 200 K. H atoms recombined and desorbed between 200 and 300 K. CO evolved from Rh deposited on fully oxidized ceria between 400 and 500 K. However, on reduced ceria films, the CO on Rh further decomposed to atomic C. Methanol adsorbed on the ceria films deprotonated to form methoxy as the only intermediate on the surface. This methoxy decomposed and desorbed as CO and H2 at higher temperatures regardless of the ceria oxidation state. Compared with the methanol reaction on Rh-free ceria thin films, formaldehyde formation from methoxy was completely suppressed after Rh deposition. Our results indicate that Rh can promote the decomposition of methoxy adsorbed on the ceria and that decomposition of methoxy intermediates occurred at the metal/oxide interfaces. On the other hand, the reduced ceria can promote total methanol decomposition on Rh.     

SiO2—Al2O3和MgO催化剂上吸附CH3NO2的TPD和IR研究

用TPD和IR方法研究了CH_3NO_2在典型固体酸SiO_2-Al_2O_3和固体碱MgO催化剂上的吸附分解。结果表明,在SiO_2-Al_2O_3表面CH_3NO_2吸附转化为表面甲酰胺物种,后者在高温下分解为CO_2和NH_3。在MgO表面CH_3NO_2吸附形成多种表面化学物种,它们在升温过程中脱附,并通过表面亚硝基甲烷物种分解为NO、C_2H_4、C_2H_6和N_2O.讨论了CH_3NO_2分解过程中表面酸、碱中心的作用。     

H2对Rh-Mn-Li-Ti/SiO2催化剂上CO吸附和脱附的影响

 应用红外光谱和程序升温脱附技术研究了Rh-Mn-Li-Ti/SiO2催化剂上H2对CO吸附和脱附的影响. 结果表明,预吸附的H2主要占据线式CO的吸附位. 共吸附时H2与CO在Rh位上形成了羰基氢化物,从而导致线式物种谱带红移,且高的H2浓度有利于CO的吸附. 在323 K下, H2对预吸附的CO谱带位置和强度没有影响. 但是,随着温度的升高, H2的存在促进了弱吸附CO的脱附,并使之重新吸附; 同时, H2促进了强吸附CO的解离,增强了CO的吸附强度和催化剂的吸附能力.     

Rh基催化剂上CO加氢制C2含氧化物的原位红外光谱研究

 用原位红外光谱考察了Rh-Mn-Li-Fe/SiO2和Rh/SiO2催化剂表面上CO的吸附态及CO加氢反应过程中吸附物种的变化. 结果表明,CO在Rh/SiO2催化剂上仅有线式吸附态存在,而CO在Rh-Mn-Li-Fe/SiO2催化剂上既有线式吸附态存在,又有孪生吸附态存在. 这说明Rh-Mn-Li-Fe/SiO2催化剂中Rh的分散度较高. 经CO加氢反应(3.0 MPa,593 K)后,在Rh-Mn-Li-Fe/SiO2催化剂上可观测到C2含氧化物前驱物种的吸收谱带,而在Rh/SiO2催化剂上未观测到相应的谱带; CO在这两种催化剂上主要以线式吸附态存在,孪生吸附态基本消失. 结合催化剂对CO加氢的催化性能,可以认为线式吸附的CO对生成C2含氧化物有贡献. Rh-Mn-Li-Fe/SiO2催化剂的高活性是由于助剂的存在削弱了其表面吸附CO的 C-O键,促进了CO的活化,从而有利于C2含氧化物前驱物的生成.     

Ethanol adsorption, decomposition and oxidation on Ir(111): a high resolution XPS study.

Ethanol (C(2)H(5)OH) adsorption, decomposition and oxidation is studied on Ir(111) using high-energy resolution, fast XPS and temperature-programmed desorption. During heating of an adsorbed ethanol layer a part of the C(2)H(5)OH(ad) desorbs molecularly, and another part remains on the surface and decomposes around 200 K; these two decomposition pathways are identified, as via acetyl (H(3)C--C=O) and via CO(ad)+CH(3ad), respectively. Acetyl and CH(3ad) decompose around 300 K into CH(ad) (and CO(ad)). CH(ad) decomposes forming C(x) and H(2) around 520 K. In the presence of O(ad) an acetate intermediate is formed around 180 K, as well as a small amount of CH(3ad) and CO(ad). Acetate decomposes between 400-480 K into CO(2), H(2)(/H(2)O) and CH(ad).     

Functionalization of beta-Ga2O3 nanoribbons: a combined computational and infrared spectroscopic study

The adsorption of H 2O, alcohols (CH 3OH and 1-octanol), and carboxylic acids (formic, acetic, and pentanoic) on beta-Ga 2O 3 nanoribbons has been studied using infrared reflection-absorption spectroscopy (IRRAS) and/or ab initio computational modeling. Adsorption energies and geometries are sensitive to surface structure, and hydrogen bonding plays a significant role in stabilizing adsorbed species. On the more stable (100)-B surface, computation shows that the physisorption of H 2O or CH 3OH is weakly exothermic whereas chemisorption via O-H bond dissociation is weakly endothermic. Experiment finds that a large fraction of a saturation coverage of adsorbed 1-octanol is displaced by exposure to acetic acid vapor. This is consistent with computational results showing that acids adsorb more strongly than methanol on this surface. The remaining alcohol, not displaced by acetic acid, suggests the presence of defects and/or (100)-A regions because computation shows that this less-stable surface adsorbs methanol more strongly than does the (100)-B. The nu(C-H) modes of adsorbed 1-octanol are easily detected whereas no adsorbed H 2O is observed even though H 2O and CH 3OH exhibit similar adsorption energies. It is inferred from this that the failure to detect H 2O on the dominant (100)-B surface results from the orientation of the physisorbed H 2O essentially parallel to the surface. Computation shows that this configuration is stabilized by H bonding. For chemisorbed formic acid, computation shows that a bridging carboxylate structure is favored over a bidentate or monodentate configuration. Computation also shows that chemisorption is favored on the (100)-A surface but physisorption is favored on the more stable (100)-B. Analysis of IRRAS data for acetic and pentanoic acids finds evidence for both types of adsorption. The carboxylate resists displacement by H 2O vapor, which suggests that carboxylic acids may be useful for functionalizing beta-Ga 2O 3 surfaces. The results provide insight into the interplay between surface structure and reactivity on an oxide surface and about the importance of hydrogen bonding in determining adsorbate structure.     

Experimental and DFT studies of the conversion of ethanol and acetic acid on PtSn-based catalysts

Reaction kinetics studies were conducted for the conversions of ethanol and acetic acid over silica-supported Pt and Pt/Sn catalysts at temperatures from 500 to 600 K. Addition of Sn to Pt catalysts inhibits the decomposition of ethanol to CO, CH4, and C2H6, such that PtSn-based catalysts are active for dehydrogenation of ethanol to acetaldehyde. Furthermore, PtSn-based catalysts are selective for the conversion of acetic acid to ethanol, acetaldehyde, and ethyl acetate, whereas Pt catalysts lead mainly to decomposition products such as CH4 and CO. These results are interpreted using density functional theory (DFT) calculations for various adsorbed species and transition states on Pt(111) and Pt3Sn(111) surfaces. The Pt3Sn alloy slab was selected for DFT studies because results from in situ (119)Sn M?ssbauer spectroscopy and CO adsorption microcalorimetry of silica-supported Pt/Sn catalysts indicate that Pt-Sn alloy is the major phase present. Accordingly, results from DFT calculations show that transition-state energies for C-O and C-C bond cleavage in ethanol-derived species increase by 25-60 kJ/mol on Pt3Sn(111) compared to Pt(111), whereas energies of transition states for dehydrogenation reactions increase by only 5-10 kJ/mol. Results from DFT calculations show that transition-state energies for CH3CO-OH bond cleavage increase by only 12 kJ/mol on Pt3Sn(111) compared to Pt(111). The suppression of C-C bond cleavage in ethanol and acetic acid upon addition of Sn to Pt is also confirmed by microcalorimetric and infrared spectroscopic measurements at 300 K of the interactions of ethanol and acetic acid with Pt and PtSn on a silica support that had been silylated to remove silanol groups.     

In situ FTIR study on the formation and adsorption of CO on alumina-supported noble metal catalysts from H2 and CO2 in the presence of water vapor at high pressures

The formation and adsorption of CO from CO(2) and H(2) at high pressures were studied over alumina-supported noble metal catalysts (Pt, Pd, Rh, Ru) by in situ FTIR measurements. To examine the effects of surface structure of supported metal particles and water vapor on the CO adsorption, FTIR spectra were collected at 323 K with untreated and heat (673 K) treated catalysts in the absence and presence of water (H(2)O, D(2)O). It was observed that the adsorption of CO occurred on all the metal catalysts at high pressures, some CO species still remained adsorbed under ambient conditions after the high pressure FTIR measurements, and the frequencies of the adsorbed CO species were lower either for the heat treated samples or in the presence of water vapor. It is assumed that the CO absorption bands on atomically smoother surfaces appear at lower frequencies and that water molecules are adsorbed more preferentially on atomically rough surfaces rather than CO species.     

Adsorption and Reaction of CO on Mo(100)-c(2×2)-N Surface Studied by HREELS

Molybdenum nitrides have attracted significant attention recently due to their uniquephysical and chemical properties. Many studies have shown that Mo,N is an activecatalyst for CO hydrogenation. The fundamental understanding concerning the reactionmechanisms over Mo=N. however, is not well established. The powerful surface sciencetechniques may provide an insight into the surface structure and properties of such animportant catalytic material. In previous paper', we described the results o…