甲醇气相羰基化Ni/AC催化剂的失活行为

采用连续流动固定床反应装置，Ni/AC作为催化剂，在533 K、1.5 MPa、CO/CH3OH/CH3I摩尔比20/19/1、7.5 gcat·h·mol－1下考察了催化剂的稳定性，并通过XPS、ICP和XRD等技术对甲醇气相羰基化反应前后Ni/AC催化剂进行了表征。结果表明，长时间运转催化剂表面形成NiI2，使具有催化活性的Ni0活性中心数量减少，活性降低。XPS结果显示羰基化活性中心Ni不断迁移并在催化剂表面富集，导致积炭效应，堵塞催化剂孔道，使催化剂失活。进一步对积炭类型研究，发现形成的碳物种主要是石墨型碳。Ni向催化剂表面迁移富集，并与CO形成可挥发的Ni(CO)4，造成金属镍的大量流失由ICP所证实。     

Ni-Sn-Cr/AC催化剂上乙酸甲酯气相羰基化合成醋酐反应的研究

以活性炭为载体,采用浸渍法制备Ni-Sn-Cr/AC催化剂,在连续流动固定床反应器上研究其对乙酸甲酯气相羰基化合成醋酐反应的催化性能。分别考察了Ni、Sn、Cr三种金属组分的负载量对催化活性的影响,进一步考察了反应压力、反应温度、反应时间对反应的影响。实验结果表明,在Ni9%-Sn12%-Cr6%/AC催化剂上,当反应温度205℃,压力5.5MPa,催化剂焙烧温度600℃,催化剂焙烧时间为4h的条件下,乙酸甲酯的转化率为38.8%,醋酐的选择性为81.1%。采用X射线衍射和元素分析技术分别对反应前和不同反应时间后的催化剂进行了表征。分析结果表明,Ni⁰是催化剂的主要活性中心,随着反应时间的延长,活性组分镍的流失现象比较严重,同时催化剂上出现积炭及载体骨架遭到破坏,是导致催化剂失活的主要原因。     

甲烷无氧芳构化反应中Co助剂对Mo／HZSM-5

 甲烷在Co－Mo／HZSM－5催化剂上进行无氧芳构化反应的评价结果表明，Co的添加大大提高了Mo／HZSM－5催化剂在反应过程中的稳定性．BET实验证明，反应后的积炭对Co－Mo／HZSM－5催化剂孔道堵塞的程度较小．对积炭催化剂进行的一系列程序升温表面反应（如TPH，TPCO2和TPO）结果表明，TPO谱上有两个峰温明显不同的烧炭峰，Co的添加明显抑制了高温积炭的生成．H2主要与高温积炭发生反应，这部分积炭是催化剂失活的主要原因；CO2对低温积炭的影响则尤为明显．TEM结果表明，积炭催化剂上存在丝状积炭物种．碳丝不能与H2反应，但能被CO2除去．Co的添加促进了丝状积炭物种的生成，碳丝并不是导致催化剂失活的因素．     

CH4、CO2与O2制合成气催化剂研究Ⅵ.催化剂表面积炭种类和积炭动力学研究

利用XPS考察了甲烷、二氧化碳和氧气制合成气反应前后Ni/γ-Al2O3和Ni-Ce-Mn-Li/γ-Al2O3催化剂表面炭物种.发现反应后Ni/γ-Al2O3催化剂表面积炭有四种类型-表面碳酸盐、污染炭、金属炭化物和非活性炭,而高活性和稳定性Ni-Ce-Mn-Li/γ-Al 2O3催化剂表面积炭仅有两种类型--污染炭和金属炭化物.非活性炭是导致催化剂失活的主要原因之一.积炭动力学研究表明: Ni-Ce-Mn-Li/γ-Al 2O 3催化剂上积炭反应的动力学方程为: r0=A·e(-E)/(RT)·PCH41.1·PO2-0.45·PO2-1.80,该催化剂积炭反应的表观活化能较高,从而抑制积炭反应的进行.     

~（13）C，~（27）Al，~（129）Xe固体NMR研究在ZSM－5型沸石上的积炭行为

以~（１３）Ｃ，~（２７）ａｌ，~（１２９）Ｘｅ为探针用固体核磁共振技术并辅以氨程序升温脱附（ＴＰＤ）技术研究了在ＺＳＭ－５型沸石上的积炭行为。结果表明，脱铝改变了沸石骨架酸中心数目及其分布，沸石酸度及骨架铝含量均对积炭起着重要作用，高温预处理能降低催化剂积炭率。催化剂积炭中心与芳构化活性中心是一致的，焦最初在催化剂外表面形成，然后逐渐深入内表面并引起孔道堵塞及失活。     

Cr—P／SiO催化剂上异丁烯——甲醛气相缩合制异戊二烯失活动力学考察

本文用积分固定床反应器对异丁烯－甲醛一步缩合制异戊二烯用Cr-P/SiO2催化剂的失活动力学进行了研究。测定了在反应温度为260－340℃，常压及不同反应物组成时的反应速度。建立了失活动力学方程，估算出反应级数，活化能、以及失活级数和失活因子。所得失活动力学方程式为：r=1.07×10^6exp(-35.2/RT)·P1^0.9·P2^1.5a a-0.47 0.53exp(-4.83×10^4t) -da/dt=2.56×10^4exp(-4.83×10^4t)从上述方程式推测，在Cr-P/SiO2催化剂上可能存在两种活性中心，一种是既能进行缩合反应同时又伴随积炭的中心，另一种中心则只进行缩合反应。催化剂的失活机理为反应物没有内扩散阻力的平行一串联失活，反应物与产物均能在催化剂表面形成焦炭，覆盖活性中心或堵塞洞口而导致失活。经烧炭催化剂活性可获得恢复。     

丙烷脱氢PtSn/Al_2O_3催化剂积炭行为研究

通过HRTEM、XRD、FT-IR、Raman、~(13)C NM R、NH_3-TPD、DTG及元素分析等表征手段,研究了丙烷脱氢PtSn催化剂积炭性质及其对催化剂结构的影响,分析了催化剂的积炭失活过程。结果表明,积炭覆盖活性位并堵塞催化剂孔道是催化剂失活主要因素;与新鲜催化剂相比,催化剂积炭完全失活后,Pt颗粒粒径并没有明显变化;完全失活时,XRD谱图出现了无定形石墨炭的衍射峰;随着积炭量的增加,焦的石墨化程度越高,芳构化程度加深,难以消除的炭增多,再生难度加大。提出丙烷在Pt活性位深度脱氢形成积炭并向载体转移的历程,认为更为稳定的C_(24)H_(12)是积炭前驱体。     

在HZSM-5沸石上甲苯歧化反应的积炭过程

采用高温大空速予积炭的方法,考察了HZSM-5沸石催化剂用于甲苯歧化反应时的积炭过程。结果表明,HZSM-5沸石上的失活方程为C_T=C_(Te~(-0.0225t))。水汽处理后HZSM-5沸石的失活速率减慢,随处理时间的增加,k 值下降。用比表面,孔隙率,吸附量以及ESR的测定考察了积炭前后沸石物性的变化,认为沸石在积炭过程中,炭沉积在沸石的表面或孔道中,使沸石孔径缩小或孔道堵塞,从而物性发生变化,反应活性下降。文中分析了沸石催化剂用于甲苯歧化反应失活的原因。     

CH_4、CO_2与O_2制合成气催化剂研究 VI.催化剂表面积炭种类和积炭动力学研究

利用XPS考察了甲烷、二氧化碳和氧气制合成气反应前后Ni/γ-Al2O3和Ni-Ce-Mn-Li/γ-Al2O3催化剂表面炭物种.发现反应后Ni/γ-Al2O3催化剂表面积炭有四种类型-表面碳酸盐、污染炭、金属炭化物和非活性炭,而高活性和稳定性Ni-Ce-Mn-Li/γ-Al2O3催化剂表面积炭仅有两种类型——污染炭和金属炭化物.非活性炭是导致催化剂失活的主要原因之一.积炭动力学研究表明:Ni-Ce-Mn-Li/γ-Al2O3催化剂上积炭反应的动力学方程为:-0.45·PO2-1.80,该催化剂积炭反应的表观活化能较高,从而抑制积炭反应的进行.1.1·PO2r0=A·e-ERT·PCH4     

HZSM-5分子筛催化剂在催化苯氧化合成苯酚反应中的积炭和失活行为

 在固定床反应器中进行了HZSM-5分子筛催化剂催化苯氧化生成苯酚时的积炭和失活实验,催化剂经高温水蒸气处理,反应条件为: 9.7%N2O-90.3%N2混合气流速115 ml/min,苯流速6 g/h,反应温度400 ℃. 采用TG,吸附吡啶的IR谱,13C NMR和低温N2吸附法对催化剂进行了表征,并用连续流动吸附法测定催化剂上正己烷和环己烷的吸附量. 结果表明,苯氧化生成苯酚的反应过程中,催化剂表面积炭导致分子筛微孔孔口堵塞是造成催化剂失活的主要原因. 与其他有机物在ZSM-5上的积炭相似,B酸中心是积炭的活性中心. 积炭物种主要为带有烷基的芳烃和多环芳烃,同时含有少量带有羟基的多环芳烃,这可能是由在L酸中心上生成的苯酚进一步氧化、脱氢和聚合形成的.     

Isolation and characterization of an iodide bridged dimeric palladium complex in carbonylation of methanol

Palladium-catalyzed carbonylation of methanol in presence of iodide promoters was investigated. Iodide bridged palladium dimeric complex, [PPh₃CH₃]₂[Pd₂I₆] was isolated from the carbonylation reaction mixture and characterized using X-ray crystallography. Reaction mechanism was proposed based on IR and UV spectroscopic characterizations of catalytic species involved in the catalytic cycle. The isolated dimeric palladium species, [Pd₂I₆]²⁻ underwent carbonylation to give monomeric species [PdI₃CO]⁻ at atmospheric pressure of carbon monoxide. It was also observed that PPh₃ plays an important role to avoid catalyst deactivation at higher temperatures. Turnover frequency (TOF) of 1052 h⁻¹ was achieved using Pd(OAc)₂-HI-PPh₃ catalyst system at 175 °C.     

Surface Structure and Catalytic Performance of CuCl/SiO2-Al2O3 Catalysts for Methanol Oxidative Carbonylation

Aluminum was doped into amorphous silica gel to modify its surface structure. The obtained SiO₂-Al₂O₃ support was used to prepare the CuCl/SiO₂-Al₂O₃ catalyst by solid-state ion exchange, and the catalyst activity for liquid-phase oxidative carbonylation of methanol to dimethyl carbonate was investigated. The results showed that the prepared SiO₂-Al₂O₃ support kept the amorphous structure of the silica gel. The BET specific surface area of the silica gel was decreased to 200 m²/g, and the surface acid sites (including Brønsted acid sites) were increased. In the CuCl/SiO₂-Al₂O₃ catalyst, CuCl was not only dispersed on surface but also was ion exchanged with surface Brønsted acid sites of the SiO₂-Al₂O₃ support to form Cu⁺ species, which resulted in a decrease in BET specific surface area to 148 m²/g. These two kinds of Cu⁺ species on the catalyst surface were both active centers for the oxidative carbonylation of methanol to dimethyl carbonate. When the catalyst was prepared with Si/Al molar ratio of 5 and was calcined at 500 °C, the selectivity and space-time yield of dimethyl carbonate reached 74% and 1.27 g/(g·h), respectively.     

Kinetics of the R + HBr RH + Br (CH3CHBr, CHBr2 or CDBr2) equilibrium. Thermochemistry of the CH3CHBr and CHBr2 radicals

The kinetics of the reaction of the CH₃CHBr, CHBr₂ or CDBr₂ radicals, R, with HBr have been investigated in a temperature-controlled tubular reactor coupled to a photoionization mass spectrometer. The CH₃CHBr (or CHBr₂ or CDBr₂) radical was produced homogeneously in the reactor by a pulsed 248 nm exciplex laser photolysis of CH₃CHBr₂ (or CHBr₃ or CDBr₃). The decay of R was monitored as a function of HBr concentration under pseudo-first-order conditions to determine the rate constants as a function of temperature. The reactions were studied separately from 253 to 344 K (CH₃CHBr + HBr) and from 288 to 477 K (CHBr₂ + HBr) and in these temperature ranges the rate constants determined were fitted to an Arrhenius expression (error limits stated are 1σ + Student’s t values, units in cm³ molecule⁻¹ s⁻¹, no error limits for the third reaction): k(CH₃CHBr + HBr) = (1.7 ± 1.2) × 10⁻¹³ exp[+ (5.1 ± 1.9) kJ mol⁻¹/RT], k(CHBr₂ + HBr) = (2.5 ± 1.2) × 10⁻¹³ exp[−(4.04 ± 1.14) kJ mol⁻¹/RT] and k(CDBr₂ + HBr) = 1.6 × 10⁻¹³ exp(−2.1 kJ mol⁻¹/RT). The energy barriers of the reverse reactions were taken from the literature. The enthalpy of formation values of the CH₃CHBr and CHBr₂ radicals and an experimental entropy value at 298 K for the CH₃CHBr radical were obtained using a second-law method. The result for the entropy value for the CH₃CHBr radical is 305 ± 9 J K⁻¹ mol⁻¹. The results for the enthalpy of formation values at 298 K are (in kJ mol⁻¹): 133.4 ± 3.4 (CH₃CHBr) and 199.1 ± 2.7 (CHBr₂), and for α-C–H bond dissociation energies of analogous compounds are (in kJ mol⁻¹): 415.0 ± 2.7 (CH₃CH₂Br) and 412.6 ± 2.7 (CH₂Br₂), respectively.     

Coordination networks constructed with supramolecular synthon RX–CCAgn (n = 4, 5; RX = halophenyl)

Eight new silver(I) double salts: AgL¹·2AgCF₃COO (1), AgL¹·3AgNO₃ (2), 2AgL²·5AgCF₃COO·2CH₃CN·H₂O (3), 4AgL³·6AgCF₃COO·5CH₃CN (4), 4AgL⁴·6AgCF₃COO·5CH₃CN (5), 2AgL⁵·4AgCF₃COO·NC(CH₂)₄CN (6), 2AgL⁵·4AgCF₃COO·2CH₃CN (7) and AgL⁶·2CF₂(CF₂COOAg)₂·2CH₃CN (8) (L¹ = 4-iodophenylethynide; L² = 3,4-dichlorophenylethynide; L³ = 3-chlorophenylethynide; L⁴ = 3-bromophenylethynide; L⁵ = 2-chlorophenylethynide; L⁶ = 2-fluorophenylethynide) have been synthesised and characterized by X-ray crystallography. All compounds contain the silver–halophenylethynide supramolecular synthon R_X−CCAg_n (n = 4, 5). In particular, the three-dimensional supramolecular structures in 1 and 2 are stabilized by strong AgI interactions, while that in 3 is consolidated by both AgCl and van der Waals type FCl interactions. In isomorphous compounds 4 and 5, the presence of respective FCl or FBr contact contributes to the stability of the network. The silver aggregates in 6, 7 and 8 are stabilized by AgCl or AgF interactions between the ortho-halo substituent and the Ag_n basket.     

The O–H···O, O–H···N and C–H···O hydrogen bonds in 1,4-dimethylpiperazine mono-betaine monohydrate

1,4-Dimethylpiperazine mono-betaine (1-carboxymethyl-1,4-dimethylpiperazinium inner salt, MBPZ) crystallizes as monohydrate. The crystals are orthorhombic, space group Pccn. Two MBPZ molecules and two water molecules form a cyclic oligomer, (MBPZ·H₂O)₂. The O–H···O and O–H···N hydrogen bonds are of 2.769(1) and 2.902(1) Å, respectively. The dimers interact with the neighboring molecules through the C–H···O hydrogen bonds of 3.234(1) Å. The piperazine ring assumes a chair conformation with the N(4)–CH₃ and N⁺(1)–CH₂COO⁻ groups in the equatorial position and the N⁺(1)–CH₃ group in the axial one. The FTIR spectrum is compared with that calculated by the B3LYP/6-31G(d,p) level of theory.     

Study of activated carbon supported iron catalysts for the Fischer-Tropsch synthesis

Summary Characterization (BET and TPD) and reaction studies were conducted with activated carbon supported iron catalysts (Fe/AC) used for the Fischer-Tropsch synthesis (FTS). The TPD study showed that there existed interactions between metals and the AC surface. Greater association of Cu and K promoters with the AC surface resulted in stronger promoter to surface interaction, which enhanced the H₂ desorption ability of the Cu and K promoted Fe/AC catalyst prepared under vacuum impregnation (VI). Catalytic behavior of a Fe/AC catalyst (VI-15 Fe/2 Cu/2 K/81 AC, in parts per weight) was studied in a 1-liter slurry phase continuous stirred tank reactor. The catalyst presented moderate syngas conversion (44.3-60.6%) and high gaseous selectivity (CH₄, 12.8-15.1% and C₂-C₄, 42.4-46.1%) under 304^oC, 3.0 MPa, 1.1 L(STP)/g-cat/h, and H₂/CO = 2.0 during 166 h of testing. Detectable hydrocarbons up to C₁₈ were formed on the Fe/AC catalyst.     

Deactivation and regeneration of the B2O3/TiO2-ZrO2 catalyst in the vapor phase Beckmann rearrangement of cyclohexanone oxime

The deactivation and regeneration of B₂O₃/TiO₂-ZrO₂ catalyst for the vapor phase Beckmann rearrangement of cyclohexanone oxime to -caprolactam were studied. The fresh, deactivated and regenerated catalysts were characterized by using adsorption of nitrogen, X-ray diffraction (XRD), thermogravimetry (TG) and NH₃-temperature-programmed desorption (NH₃-TPD) techniques. The crystal structure and pore size distribution of the catalyst were retained after reaction, but the number of acid sites decreased significantly. There was a relationship between the amount of coke deposited on the catalyst and the decline in catalytic activity. These results suggest that the coke deposition on the surface of catalyst is mainly responsible for the catalyst deactivation. The catalytic activity can be recovered completely after calcining the deactivated catalyst in air flow at 600 °C for 8 h.     

Zur theorie der α-ketosa¨uren: Mechanismus der enolisierung einiger brenztraubensa¨ureamide

The mechanism of enolisation of pyruvamide is discussed by the influence of substituents on the kinetic CH₃-acidity, by general base-catalysis of enolisation, by the enthalpy and entropy of activation and primary kinetic and kinetic solvent deuterium isotope effects respectively. A Bro¨nsted coefficient β = 0·71 has been obtained in the general base catalysis of pyruvdiethylamide enolisation. The effect of car☐ylsubstituents on the kinetic CH₃-acidity is produced not only by an inductive mechanism. The importance of solvent structure is demonstrated by a strong negative entropy of activation for the H₂O-catalysed reaction. In the H₂O-catalysed enolisation of pyruvdiethylamide a large kinetic deuterium solvent isotope effect k_o^H₂O/k_o^D₂O = 2·39) was obtained at 25°C. In contrast, when hydroxid is the catalyst, the primary kinetic deuterium isotope effect is unusually low (k_H/k_D = 3·5). Thus, in comparison to other keto compounds, a different mechanism of enolisation for the pyruvic acid derivatives must be postulated. Some aspects of this mechanism are discussed in the paper.     

Self-assembly of the pre-formed inclusion complexes between cyclodextrins and alkanethiols on gold electrodes

A new kind of self-assembled monolayer (SAM) formed in aqueous solution through the pre-formed inclusion complexes (abbreviated CD · C_n) between α, β-cyclodextrins (CDs) and alkanethiols (CH₃(CH₂)_n−1)SH, n = 10, 14 and 18) was prepared successfully on gold electrodes. High-resolution ¹H NMR was used to confirm the formation of CD · C_n. X-ray photoelectron spectroscopy, cyclic voltammetry and chronoamperometry were used to characterize the resulting SAMs (denoted as M_CD·Cn). It was found that M_CD·Cn were more stable against repeated potential cycling in 0.5 M H₂SO₄ than SAMs of CH₃(CH₂)_n−1SH (denoted as M_Cn), with a relative sequence of M_β−CD·Cn > M_α−CD·Cn > M_Cn. In addition, an order of blocking the electron transfer between gold electrodes and redox couples (both Fe(CN)³₆ and Ru(NH₃)³⁴₆) in solution, M_CD·C10 > M_CD·C14 > M_CD·C18, was observed. A plausible explanation is provided to elucidate some of the observations.