Ammonia sorption by Dawson acid studied by IR spectroscopy and microbalance

Using in-situ microbalance and infrared spectroscopy techniques the double ammonia proton complexation was traced. The results confirm the formation of N₂H₇⁺ dimer in solid Dawson acid H₆P₂W₁₈O₆₂, previously reported only for N₂H₇I and for (N₂H₇)₄SiW₁₂O₄₀. The formation of such dimers was evidenced by the microbalance results, the molar ratio of ammonia to proton was measured as 2:1 at 10.7 kPa and 298 K. The formation of NH₄⁺ monomer (band at 1410 cm⁻¹) and N₂H₇⁺ dimer (1460 cm⁻¹) was revealed by IR spectroscopy. Enthalpy of ammonia sorption on Dawson structure was calculated to be −127.9 kJ mol⁻¹, indicating the lower acid strength of Dawson-type compared to that of the Keggin-type heteropolyacids, like H₄SiW₁₂O₄₀.     

CO_2在三聚氰胺酚醛纤维上的吸附分离

以三聚氰胺、间苯三酚和甲醛为原料,通过水热缩聚反应合成了三聚氰胺酚醛纤维(PMF),考察了温度对PMF合成的影响。以扫描电子显微镜(SEM)、透射电子显微镜(TEM)、N_2吸脱附和傅里叶变换红外(FT-IR)光谱等表征了PMF的形貌和结构,并采用体积法测定不同温度下CO_2和N_2在PMF上的单组分吸附平衡等温线。结果表明,在393 K下合成的PMF具有较大的比表面积(64 m2/g)和较高的CO_2吸附量(1.83 mmol/g,298 K、118 k Pa)。穿透柱实验表明,在298 K、200-600 k Pa,CO_2-N_2混合气在PMF上均可实现有效分离。将PMF在873 K下,N_2、H2及水蒸气等多种气氛中进行后处理,其比表面积和微孔孔容均显著增加,其中,在15%H_2O气氛中处理后,样品CO_2吸附量提高至2.83 mmol/g(298 K、118 k Pa)。     

Rh-V/SiO2上H2的化学吸附方式

CO加氢反应机理是许多研究者感兴趣的课题.负载的Rh是CO加氢反应的优良催化剂.CO在Rh上吸附态的研究已有许多报道,而对H₂有关的吸附态的研究却少见报道.     

H2,CO和H2/CO在ZrO2催化剂上吸附行为研究

用insituFTIR法研究了H₂、CO及CO/H₂在ZrO₂表面的吸附行为.结果表明,H₂在ZrO₂表面吸附存在两种形态的羟基(即ZrOH和ZrOHZr),吸附温度增加,羟基数量增加.CO在200℃易与ZrO₂表面羟基作用形成甲酸盐物种,吸附温度升高时,该物种逐渐分解生成CO和ZrOH.当CO和H₂共存时,表面甲酸盐的量明显增加,并随温度增加,逐渐加氢形成甲氧基,最后生成甲烷.甲氧基的加氢过程较慢,所需反应温度也较高,被认为是CO加氢合成醇的速控步骤.     

CATALYTIC PERFORMANCE OF MIXED-BIMETALLIC RUTHENIUM CARBONYL CLUSTERDERIVED CATALYSTS IN CO HYDROGENATION

The bimetallic catalysts prepared from SiO_2-supported Ru-Co,Ru-Fe and Ru-Mo carbonyl clusters exhibited high yields and selectivitiestowards oxygenates such as C_1-C_5 from CO+H_2,in contrast to the catalystsprepared from homometallic and bimetallic Ru,Ru-Ni,Ru-Rh,Ru-Mn,and Ru-Cr carbonyl clusters.The FTIR investigation revealed that the 1584 cm~(-1)species plays an important role in the formation of oxygenates in COhydrogenation,which is possibly assigned to surface formyl species.     

Ru添加对Co/SiO2费托合成催化剂性能的影响

用初湿含浸法制备了不同Ru添加量的Co/SiO₂模型催化剂,然后进行N₂物理吸附、XRD、H₂-TPD、DRIFTS等表征和微分固定床费托(F-T)反应评价。F-T反应结果表明,催化剂中添加Ru后,CO转化率显著提高,TOF值增大,CO₂和CH₄选择性降低,烯/烷比(O/P)降低。FT-IR表征说明,催化剂添加Ru后Co-O键的强度减弱,相对应的H₂-TPR也表明,催化剂的还原度得到显著提高。还原后的催化剂XRD结果进一步证实,加入Ru后,催化剂无钴氧化物被检出,并且当Ru添加量为0.5%(质量分数)时催化剂中金属钴主要以六方密堆(hcp)形式存在。CO-DRIFTS结果显示,Ru的加入使CO的吸收峰发生红移,即Ru促进了CO的解离。H₂-TPD结果则表明,随着Ru添加量的增加,催化剂表面CO_ads/Co_s和CO^*/Co_s增大,这是CH₄选择性降低的主要原因。     

硅纳米管负载的钌基催化剂费-托合成催化性能研究

以模板法合成的硅纳米管（SNT）为载体,用浆态浸渍法制备了钌基催化剂,采用氮气物理吸附、透射电子显微镜（TEM）、X射线粉末衍射（XRD）和氢气程序升温还原（H₂-TPR）等手段对其进行了表征。在固定床反应器上（503K,1.0MPa）考察了该催化剂的费-托合成反应活性及产物选择性,并与用商业二氧化硅为载体制备的催化剂上的反应结果进行了比较。结果表明,SNT和SiO₂负载的氧化钌在623K可被H₂完全还原;SNT负载的钌基催化剂上,钌氧化物颗粒较小、分散性好,还原后钌颗粒被较好地分散在硅纳米管上,且几乎所有的钌颗粒都分布在管内。与以SiO₂为载体的催化剂相比,以硅纳米管为载体的钌基催化剂具有较高的费-托合成活性。     

Isothermal Evaporation of Quaternary System Li^＋, K^＋, Mg^2＋//Cl^--H2O at 348K

The solubilities of the quaternary system Li^＋,K^＋,Mg2^＋//Cl^--H2O were investigated at 348 K via isothermal evaporation.The densities and refractive indices of its equilibrated solution were also determined experimentally.On the basis of the obtained data,the metastable phase diagram,the water content diagram,the diagrams of the density and refractive index against the composition of this quaternary system were constructed.The quaternary system Li^＋,K^＋,Mg^2＋//Cl^--H2O at 348 K belongs to a complex type with the formation of two carnallite double salts,which are potassium carnallite（K-carnallite） and lithium carnallite（Li-carnallite）.There are five salts like potassium chloride （KCl）,lithium chloride monohydrate（LiCl.H2O）,bischofite（MgCl2·6H2O）,K-carnallite（KCl·MgCl2·6H2O） and Li-carnallite（LiCl·MgCl2·7H2O）,seven unvariant curves named AH3,BH2,CH3,DH1,EH1,H1H2 and H2H3,and three invariant points,namely H1,H2 and H3,included in this metastable phase diagram.Comparisons between the stable phase diagram at 298 K and metastable phase diagram at 348 K of this quaternary system show that all the crystalline forms of the salts are not changed,whereas the crystallization areas of salts are changed significantly with temperature.The scope of KCl crystallization increases from 82% to 95% and that of K-carnallite decreases from 15.80% to 0.32% along with the temperature increasing from 298 K to 348 K,respectively.     

The multichannel reaction NH2 + NH2 at ambient temperature and low pressures

NH₂ profiles were measured in a discharge flow reactor at ambient temperature by monitoring reactants and products with an electron impact mass spectrometer. At the low pressures used (0.7 and 1.0 mbar) the gas-phase self-reaction is dominated by a ‘bimolecular’ H₂-eliminating exit channel with a rate coefficient of k_3b(300 K) = (1.3 ± 0.5) × 10⁻¹² cm³ molecule⁻¹ s⁻¹ and leading to N₂H₂ + H₂ or NNH₂ + H₂. Although the wall loss for NH₂ radicals is relatively small (k_w ≈ 6–14 s⁻¹), the contribution to the overall NH₂ decay is important due to the relatively slow gas-phase reaction. The heterogeneous reaction yields N₂H₄ molecules.     

纳米片层二硫化钼负载PtCo双金属催化甲醇水相重整制氢

采用水热法合成了层数只有六层的纳米片层二硫化钼（MoS₂）,并进一步负载Pt和PtM双金属（M=Ru、Pd、Co和Ni）,用于催化甲醇水相重整制氢反应。结果表明,PtCo/MoS₂对于甲醇水相重整具有最优异的催化性能,在220℃下产氢转换频率（TOF）为37142 h^-1。氮气吸附-脱附等温线、透射电子显微镜（TEM）、程序升温还原（H₂-TPR）以及X射线光电子能谱（XPS）等表征结果表明,PtCo/MoS₂中金属还原程度高,且Pt与载体MoS₂形成了强电子相互作用,使缺电子的Pt有利于吸附活化甲醇,并进一步促进甲醇重整反应。     

Pore size control and gas permeation kinetics of silica membranes by pyrolysis of phenyl-substituted ethoxysilanes with cross-flow through a porous support wall

A silica membrane was produced by chemical vapor deposition using tetraethoxysilane (TEOS), phenyltriethoxysilane (PTES) or diphenyldiethoxysilane (DPDES) as the Si source. Amorphous silica was deposited in the mesopores of a γ-alumina film coated on a porous -alumina tube, by evacuating the reactant through the porous wall. Hydrogen permeance at a permeation temperature of 600°C was of the order of 10⁻⁷ mol m⁻² s⁻¹ Pa⁻¹, and was not greatly dependent on the Si sources. The silica membrane produced using TEOS contained micropores permeable to both helium and hydrogen, but CO₂ and larger molecules were only slightly permeated through those mesopores which were left unplugged. The silica membrane produced from DPDES showed a single-component CO₂ permeance equivalent to that of single-component He, and CO₂/N₂ selectivity was approximately 9 at a permeation temperature of 30°C. When a mixture of CO₂ and N₂ was fed, however, CO₂ permeance decreased to the level of N₂ permeance. The H₂/N₂ selectivity, determined from single-component permeances to H₂ and N₂, was approximately 100, and these permeances remained unchanged when an equimolar mixture of H₂ and N₂ was fed. Thus, the DPDES-derived membrane possessed two types of micropores, abundant pores through which helium and hydrogen permeated and a small number of pores in which molecules of CO₂ and N₂ were permeable but not able to pass one another. Neither meso or macropores remained in the DPDES membrane.     

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.     

Rate constant of the reaction of NO3 with CH2I2 measured with use of cavity ring-down spectroscopy

We have applied cavity ring-down spectroscopy to a kinetic study of the reaction of NO₃ with CH₂I₂ in 25–100 Torr of N₂ diluent at 298 K. The rate constant of reaction of NO₃ + CH₂I₂ is determined to be (4.0 ± 1.2) × 10⁻¹³ cm³ molecule⁻¹ s⁻¹ in 100 Torr of N₂ diluent at 298 K. The rate constant increases with increasing pressure of buffer gas below 100 Torr. The reaction of CH₂I₂ with NO₃ has the potential importance at nighttime in the atmosphere.     

ZnSO_4和La_2O_3作共修饰剂单金属Ru催化剂上苯选择加氢制环己烯

用沉淀法制备了单金属纳米Ru(0)催化剂,考察了ZnSO4和La2O3作共修饰剂对该催化剂催化苯选择加氢制环己烯性能的影响,并用X射线衍射(XRD)、X射线荧光(XRF)光谱、X射线光电子能谱(XPS)、俄歇电子能谱(AES)、透射电镜(TEM)和N2物理吸附等手段对加氢前后催化剂进行了表征.结果表明,在ZnSO4存在下,随着添加碱性La2O3量的增加,ZnSO4水解生成的(Zn(OH)2)3(ZnSO4)(H2O)x(x=1,3)盐量增加,催化剂活性单调降低,环己烯选择性单调升高.当La2O3/Ru物质的量比为0.075时,Ru催化剂上苯转化率为77.6%,环己烯选择性和收率分别为75.2%和58.4%.且该催化体系具有良好的重复使用性能.传质计算结果表明,苯、环己烯和氢气的液-固扩散限制和孔内扩散限制都可忽略.因此,高环己烯选择性和收率的获得不能简单归结为物理效应,而与催化剂的结构和催化体系密切相关.根据实验结果,我们推测在化学吸附有(Zn(OH)2)3(ZnSO4)(H2O)x(x=1,3)盐的Ru(0)催化剂有两种活化苯的活性位:Ru0和Zn2+.因为Zn2+将部分电子转移给了Ru,Zn2+活化苯的能力比Ru0弱.同时由于Ru和Zn2+的原子半径接近,Zn2+可以覆盖一部分Ru0活性位,导致解离H2的Ru0活性位减少.这导致了Zn2+上活化的苯只能加氢生成环己烯和Ru(0)催化剂活性的降低.本文利用双活性位模型来解释Ru基催化剂上的苯加氢反应,并用Hückel分子轨道理论说明了该模型的合理性.     

三组Pt- Ru/C催化剂前驱体对其性能的影响

分别以三组不同的Pt和Ru化合物为前驱体, 采用热还原法制备了Pt-Ru/C催化剂, 比较不同前驱体对催化剂性能的影响；通过XRD和TEM技术对催化剂的晶体结构及微观形貌进行了分析. 结果表明以H₂PtCl₆+RuCl₃和自制(NH₄)₂PtCl₆+Ru(OH)₃为前驱体的催化剂Pt和Ru没有完全形成合金状态, 在Pt(111)和Pt(200)之间有Ru(101)存在；以Pt(NH₃)₂(NO₂)₂和自制含钌化合物为前驱体制备的催化剂未检测出Ru金属或其氧化物的衍射峰, Pt-Ru颗粒在载体上分散均匀, 粒径最小, 为3.7 nm. 利用玻碳电极测试了循环伏安、记时电流和阶跃电位曲线, 考核了上述催化剂对甲醇阳极催化氧化活性的影响；结果表明：以Pt(NH₃)₂(NO₂)₂和自制含钌化合物为前驱体制备的催化剂对甲醇的电催化氧化活性最高, 循环伏安曲线峰电流密度达11.5 mA•cm^-2.     

NO2、H2O和N2对碘荧光的猝灭

核燃料后处理工业产生的废气中的129I2被排到大气中会造成严重的环境污染,因此迫切需要一种简便、快速而又足够灵敏的检测方法．中子活化分析法的检测极限可达4·0×107mole／cm3[1],虽然其灵敏度可满足要求,但因耗时长无法用于实时监测·激光诱导荧光法（LIF）是一种选择性好且灵敏度高的方法,已被广泛用于痕量物质的测定．该方法用于测定微量碘也已有报道[2,3],Goles等[3]用单模CW激光在580nm波长激发碘分子,用光子计数检测,测定纯129I2检测极限为2×109mole／cm3．但LIF法的最大缺点是荧光的猝灭会使检测灵敏度显著下降．Atsu…     

Flash photolysis/temperature jump study of the vibrational relaxation of N2O(010) by O(P) and NO

This survey begins with the photochemistry at 254 nm and 298 K in the system H₂O₂COO₂RH, the primary objective of which is to determine the rate constants for the reaction OH + RH → H₂O + R relative to the well-known rate constant for the reaction OH + CO → CO₂ + H. Inherent in the scheme is that the reaction HO₂+CO→OH+CO₂ is negligible compared with the OH reaction, and a literature consensus gives k_HO2 < 10⁻¹⁹ cm³ molecule⁻¹ s⁻¹, or some 10⁶ less than k_OH at 298 K. Theoretical calculations establish that the first stage in the HO₂ reaction is the formation of a free radical intermediate HO₂ + CO → HOOCO (perhydroxooxomethyl) which decomposes to yield the products, and that the rate of formation of the intermediate is equal to the rate of formation of the products. The structure of the intermediate and a reaction profile are shown.

High temperature rate data reported subsequent to the data in the consensus and theoretical calculations lead here to a recommendation that, in the range 250–800 K, k_HO2 = 3.45 × 10⁻¹²T^1/2 exp(1.15 × 10⁴/T) cm³ molecule⁻¹ s⁻¹, the hard-sphere-collision Arrhenius modification. This yields k_HO2(298) = 1.0 × 10⁻²⁷ cm³ molecule⁻¹ s⁻¹ or some 10¹⁴ slower than k_OH(298).     

Ru/氧化物催化剂在甲苯部分加氢反应中的载体效应

采用浸渍-化学还原法制备了一系列负载型Ru催化剂,考察了一些常见的氧化物载体（SiO₂、m-ZrO₂、t-ZrO₂、γ-Al₂O₃和P25）对甲苯部分加氢制甲基环己烯催化性能的影响。采用N₂物理吸附、X射线粉末衍射（XRD）、透射电子显微镜（TEM）和X射线光电子能谱（XPS）等手段对催化剂进行了系统的表征。研究表明,载体通过影响Ru的粒径,进而影响甲苯部分加氢催化性能。当Ru纳米粒子的粒径由2.6 nm增大到17.3 nm时,甲苯的转换频率（TOF）以及甲基环己烯初始选择性（S₀）先增加,然后降低,呈火山型变化趋势,二者的最大值均在Ru粒径为3.0 nm时出现。在催化性能最优的Ru/P25催化剂上,进一步考察了修饰剂的种类和浓度、反应温度、反应压力等条件的影响。当反应温度为423 K、H₂压力为5.0 MPa,以0.25 g七水合硫酸锌为修饰剂时,Ru/P25催化剂上的初始加氢速率（r₀）为26 mmol·g^-1·min^-1,S₀为57%,甲基环己烯得率可达36%。     

Surface Structure and Electrocatalytic Activity of Ru(0001) and Ru/Pt(111) Single Crystal Electrodes:In-situ FTIR and ex-situ LEED,RHEED and AES Studies

In-situ FTIR spectroscopic and electrochemical data, and ex-situ (emersion) electron diffraction (LEED and RHEED) and Auger electron spectroscopic (AES) data are presented on the structure and reactivity, with respect to the electro-oxidation of CO, of the Ru(0001) single crystal surfaces in perchloric acid solution. In both the absence and presence of adsorbed CO, the Ru(0001) electrode shows the potential-dependent formation of well-defined and ordered oxygen-containing adlayers. At low potentials (eg. from -80 to +200 mV vs Ag/AgCl), a (2 x 2)-O phase is formed, which is unreactive toward CO oxidation, in agreement with UHV studies; increasing the potential results in the formation of (3 x 1) and (1 x 1) phases at 410 mV and 1100 mV, respectively, with a concomitant increase in the reactivity of the surface toward CO oxidation. Both linear (CO_L) and threefold-hollow (CO_H) binding CO adsorbates (bands at 2000-2040 cm^-1 and 1770-1800 cm^-1, respectively) were observed on the Ru(0001) electrode. The in-situ FTIR data show that the adsorbed CO species still remain in compact islands as CO oxidation proceeds, suggesting that the oxidation occurs at the boundaries between the CO_ad and active O_ad domains via the Langmuir-Hinshelwood mechanism. At low CO coverages,reversible relaxation, (at lower potentials), and compression, (at higher potentials), of the CO_L adlayer were observed and rationalised in terms of the reduction and formation of surface O-adlayers, The data obtained from the Ru(0001) electrode are in marked contrast to those observed at polycrystalline Ru, where only linear CO is observed.     

煤炭解耦燃烧过程N迁移与转化Ⅱ:单组分气相化学反应实验

在理想平推流反应器中进行了模拟热解气对模拟烟气中NO、N₂O的还原实验研究,考察了反应温度、过剩空气系数λ、热解气中CH₄、CO、H₂、NH₃浓度、烟气中NO、N₂O浓度变化对NO、N₂O出口浓度的影响。实验结果表明,当模拟热解气仅含其中一种气体时,在反应温度973~1 223 K时热解气中CH₄、CO、H₂基本不与NO发生反应,当λ小于或等于1.0时可降低N₂O浓度0%~30%;热解气中NH₃可降低NO 10%~60%,但NH₃不与N₂O发生反应。