异戊烯与甲醇成醚反应机理的量子化学研究

对2-甲基-1-丁烯、2-甲基-2-丁烯与甲醇反应生成甲基叔戊基醚的反应历程进行了量子化学研究, 结果表明, 反应过程包括两个基元步骤: 2-甲基-1-丁烯和2-甲基-2-丁烯与氢离子作用生成碳正离子, 活化能分别为E1=2.26 kJ/mol, E2=7.72 kJ/mol; 甲醇与叔碳正离子反应成醚, 活化能为E3=1.29 kJ/mol, 碳正离子的生成是反应的速控步骤. 2-甲基-1-丁烯与2-甲基-2-丁烯相互转化的异构化活化能分别为E'1=4.40 kJ/mol, E'2=63.11 kJ/mol, 高于成醚的活化能, 反应体系不发生烯烃相互转化的异构化反应.     

Pt/SAPO-11临氢异构化催化剂反应特性的研究

以正庚烷为模型化合物，在10 mL连续流动固定床反应装置上，考察了温度、压力、空速与氢烃摩尔比对0.4%Pt/SAPO-11催化剂临氢异构化反应性能的影响。结果表明，催化反应以烷烃异构化为主，正庚烷转化率达70%时异构产物选择性保持在90%以上，压力和氢烃摩尔比较小时，产物的选择性较高；压力太高裂解产物生成量增多对异构化选择性不利。获得了正庚烷在Pt/SAPO-11催化剂上临氢异构化的优化反应条件为，360 ℃～380 ℃，0.5 MPa～1.0 MPa，2.1 h-1～4.1 h-1，H2/CH(摩尔比)2～6；烷烃临氢异构化反应的一个条件变化，需要其他条件的改变来达到最佳的匹配。     

铝钛合金溴化物对直链烷烃异构化反应的催化作用

首次研究了铝铁合金溴化物的合成及其对直链烷烃异构化反应的催化作用,讨论了正戊烷的异构化反应,得到其动力学方程为1nC/C_0=-0.50t,表观活化能为26.3 kJ/moJ,测定了正己烷、正庚烷、正辛烷在不同溶剂中、不同温度下催化异构化反应的动力学曲线,为铝铁合金溴化物的工业应用提供了理论依据。     

载Ce介孔分子筛催化剂上庚烷异构化性能研究

采用分步浸渍法制备了Ni-SiW12-Ce/Al-MCM-41双功能催化剂,通过X射线衍射(XRD)、BET和扫描电子显微镜(TEM),H2-TPR等方法对催化剂进行了表征.在常压连续流动固定床气固反应装置上,研究了催化剂的正庚烷临氢异构化反应性能,考察了催化剂制备条件对正庚烷临氢异构化反应效果的影响.结果表明,Ce的掺入改善了活性组分Ni的分散性,优化了催化剂庚烷异构化性能,同时增加了催化剂的稳定性.在Ce含量为0.8%、硅钨酸含量为20%、Ni含量4%、还原温度为400℃、还原氢气流速50 mL/min的条件下制备的催化剂的效果最好.以4%Ni-20%SiW12-0.8%Ce/Al-MCM-41为催化剂,当庚烷转化率为22.3%时,异庚烷选择性达到65.4%.     

Catalytic Performance of Mesoporous Molecular Sieve in n-heptane Hydroisomerization

采用分步浸渍法制备了Ni-SiW12-Ce/Al-MCM-41双功能催化剂,通过X射线衍射（XRD）、BET和扫描电子显微镜（TEM）,H2-TPR等方法对催化剂进行了表征.在常压连续流动固定床气固反应装置上,研究了催化剂的正庚烷临氢异构化反应性能,考察了催化剂制备条件对正庚烷临氢异构化反应效果的影响.结果表明,Ce的掺入改善了活性组分Ni的分散性,优化了催化剂庚烷异构化性能,同时增加了催化剂的稳定性.在Ce含量为0.8%、硅钨酸含量为20%、Ni含量4%、还原温度为400℃、还原氢气流速50 mL/min的条件下制备的催化剂的效果最好.以4%Ni-20%SiW12-0.8%Ce/Al-MCM-41为催化剂,当庚烷转化率为22.3%时,异庚烷选择性达到65.4%.     

6-甲基-4-羟基嘧啶单体及二聚体质子转移过程的理论研究

应用密度泛函理论的B3LYP/6-311+G(d)方法研究了6-甲基-4-羟基嘧啶单体及二聚体质子转移的异构化反应.对反应势能面的研究发现,该化含物可能存在9种单体异构体,对其最稳定的单体构型进行分析.各单体间异构化反应的过渡态共有9种,反应的活化能最小为22.06 kJ/mol,最大为356.55 kJ/mol,最可能的反应路径在室温下即可进行. 研究了2种二聚体及其异构化反应的过渡态,发现二聚体均比其对应的单体稳定,而且质子转移所需要的活化能仅为20.13 kJ/mol,比单体低很多. 氢键在这种变化中起了主要作用,由单体和二聚体的总能量计算了氢键的键能.     

Ga_2O_3对Pt/WO_3/ZrO_2催化剂上正庚烷异构化反应的促进作用

考察了Ga2O3掺杂的Pt/WO3/ZrO2(Pt/WGZ)催化剂在200℃时正庚烷临氢异构化反应性能.结果表明,少量Ga2O3的加入能显著提高Pt/WGZ的催化活性,异构化选择性也有所增加,这是由于B酸位增加和B酸/L酸比的改变而引起的.Pt/WGZ催化剂连续反应80 h,正庚烷转化率和异构化选择性分别稳定在76%和94%.     

分子内C—H键胺化反应机理的DFT研究

采用密度泛函理论研究了溴化亚铁催化芳基叠氮化物C—H键胺化生成苯并咪唑的反应机理.研究结果表明,溴化亚铁催化剂使反应由协同机理转变为分步机理,反应活化能降低了大约167kJ/mol.催化反应由氮气消去、C—N形成和2H-苯并咪唑异构化3个基元步骤组成.其中金属亚胺/金属氮烯FeNR PhNCPh进攻C形成C—N键是无能垒过程,且与金属氮烯中氮的电荷密切相关.氮气消去与2H-苯并咪唑异构化反应的能垒均在41~54kJ/mol之间.     

不同方法制备Ni-WO_3/TiO_2-ZrO_2催化剂及其性能研究

考察了Ti O2-Zr O2载体制备方法对Ni-WO3/Ti O2-Zr O2催化正庚烷异构化反应性能的影响.通过BET、XRD、SEM和NH3-TPD的表征结果表明,以模板-溶胶-凝胶法制备Ti O2-Zr O2载体时,Ni-WO3/Ti O2-Zr O2催化剂晶相结晶度较好,具有较适宜的表面酸性和比表面积,从而在正庚烷异构化反应中表现出较高的催化活性和选择性,正庚烷的转化率和异庚烷的选择性分别为72.62%和80.81%.实验结果还表明,Ti O2-Zr O2比Zr O2、Si O2-Zr O2和Al2O3-Zr O2更适宜作为载体制备催化剂应用于正庚烷异构化的反应中.     

板状镍催化剂上氨分解和氨部分氧化制氮氢气的研究

研制了一种 Ni/Al₂O₃多孔板状催化剂.该催化剂在反应温度高于750℃,氨分解率高于99.5%时,允许反应空速达10000—40000h^-1.用该催化板组装的反应器可采用内加热形式,和一般的外加热反应器相比可节约能耗约30%.在催化板上氨分解的经验动力学方程是γ=kp²NH₃,表观活化能为153.0kJ/mol.将该催化剂用于氨部分氧化时,在空气和氨比为1.0—1.7,680—750℃,氨空速10000—40000h^-1条件下,在氨点火后无外加能源情况下,能制得含氢30～43%,残氧小于0.1%的氮氢混合气,氨的转化率>99.5%,连续250小时反应表明,催化剂活性稳定.宏观动力学研究得出,反应对氨呈零级,表观活化能为37.2kJ/mol.     

SiO2骨架支撑MoOx催化剂用于正庚烷异构化反应

 采用SEM，XRD，EDS及N2吸附－脱附方法研究了骨架型MoOx－SiO2催化剂和负载型MoOx／SiO2催化剂的物理化学结构，并在常压固定床流动反应器上考察了两种催化剂对正庚烷异构化反应的催化性能．结果表明，在MoOx－SiO2催化剂中，44．6％的SiO2即可起到很好的骨架支撑作用；MoOx晶相以足够大的空间区域聚集包裹在SiO2骨架中，形成类似MoOx催化剂的独特的中孔结构．与MoOx催化剂相比，MoOx－SiO2催化剂显著提高了机械强度，并维持了MoOx催化剂较高的活性和选择性．由于钼物种和载体之间的相互作用，负载型MoOx／SiO2催化剂表现出较低的比活性．脉冲注入H2S实验结果表明，MoOx－SiO2催化剂具有较好的抗硫性能．     

Preparation and Catalytic Property of MoOx with Meso-porosity

A partially reduced molybdenum oxide (MoOx) with meso-porosity was prepared for the first time and its catalytic performance in n-heptane isomerization carried out in a fixed bed flow reactor has been studied. And the evolvement of MoOx formation has been characterized by X-ray diffraction and catalytic performance in n-heptane isomerization. The MoOx catalyst obtained from H2 reduction for 12 h, possessing a maximum pore volume at diameter ca. 4.1 nm, exhibited high activity in n-heptane isomerization. The composition of this catalyst is of the predominant MoOx phases, MoO2 phase and trace amount of metal Mo phase.     

NiO/WO3/TiO2-Al2O3催化剂上正庚烷的临氢异构化

采用溶胶凝胶法制备了TiO2-Al2O3复合载体,用分步浸渍法制备了NiO/WO3/TiO2-Al2O3催化剂。 在常压连续流动固定床反应器上考察了NiO/WO3/TiO2-Al2O3对正庚烷临氢异构化反应的催化性能。 研究了催化剂中WO3含量、Ni含量、焙烧温度和还原温度及催化反应温度对临氢异构化反应的影响。 采用XRD和BET方法对催化剂进行了表征。 结果表明,当w(WO3)=25%、w(Ni)=10%时,所制备的NiO/WO3/TiO2-Al2O3催化剂对正庚烷异构化反应的催化性能最好,活性可达15.50%,选择性可达84.06%。     

正庚烷在Ni-Sn/SAPO-11催化剂上的临氢异构化反应

分别以浸渍法和分步浸渍法制备了Ni/SAPO-11催化剂和Ni-Sn/SAPO-11双金属催化剂,利用XRD、F T-IR、NH_3-TPD、Py-IR、SEM等手段对其进行了表征,考察了Sn含量对分子筛结构和酸性的影响,并以正庚烷临氢异构化为探针反应,考察了Sn含量及反应条件对催化剂临氢异构化性能的影响.结果表明,在我们所考察的Sn含量范围(加入锡含量)内,所制备的催化剂均能保持SAPO-11分子筛晶相,金属Sn均可调节催化剂酸性.加入Sn可以明显提高正庚烷的转化率和异庚烷的选择性,其中,在氢烃比n(H_2)/n(n-C_7H_(16))为14、H_2流速为30m L/min、还原温度为430℃、还原时间为5 h、反应温度为300℃、反应时间为5 h、重时空速(WHSV)为6.8 h-1、反应压力为常压条件下,5%Ni-4%Sn/SAPO-11催化剂的催化性能较佳,其正庚烷转化率可达43%,异庚烷的选择性可达71%.     

New insights on molybdenum suboxide: nature of carbons in isomerization reactions

MoO3 transformations under isomerization process conditions were studied. The products obtained after different times under stream (H2/n-heptane mixture, 18.5 bar, at 370 degrees C) were characterized by X-ray diffraction, Raman spectroscopy, thermal analysis, and high-resolution transmission electron microscopy (HRTEM). Theoretical quantum calculations were carried out with the aim of understanding the paradox of the real active phase in isomerization reactions. Theoretical calculations predict the existence of a metallic-like MoO phase with a structure that matches the X-ray diffraction experimental results. From experimental and simulated HRTEM images it was possible to identify the presence of small MoO cubic crystallites inside MoOx matrix phases. These results also support the previously proposed idea that isomerization reactions take place as a result of the existence of a bifunctional catalyst. The Raman and thermo-programmed oxidation (TPO) analyses show the existence of at least two types of carbonaceous deposits which tend to increase its ordering with the increase of time under stream. The carbon K edge in electron energy loss spectroscopy (EELS) of a sample after 24 h under stream shows that these carbonaceous deposits consist of a mixture of sp2- and sp3-hybridized carbons.     

Catalytic properties of the dioxomolybdenum siloxide MoO2(OSiPh3)2 and its 2,2'-bipyridine adduct MoO2(OSiPh3)2(bpy)

The tetrahedral triphenylsiloxy complex MoO(2)(OSiPh(3))(2) (1) and its Lewis base adduct with 2,2'-bipyridine, MoO(2)(OSiPh(3))(2)(bpy) (2), were prepared and characterised by IR/Raman spectroscopy, and thermogravimetric analysis. Both compounds catalyse the epoxidation of cis-cyclooctene at 55 degrees C using tert-butylhydroperoxide (t-BuOOH) is decane as the oxidant, giving 1,2-epoxycyclooctane as the only product. The best results were obtained in the absence of a co-solvent (other than the decane) or in the presence of 1,2-dichloroethane, while much lower activities were obtained when hexane or acetonitrile were added. With no co-solvent, catalyst 1 (initial activity 272 mol x molMo(-1) x h(-1)for a catalyst:substrate: oxidant molar ratio of 1:100:150) is much more active than 2(initial activity 12 mol x molMo(-1) x h(-1)). The initial reaction rates showed first order dependence with respect to the initial concentration of olefin. With respect to the initial amount of oxidant, the rate order dependence for 1 (1.9) was higher than that for 2 (1.6).The dependence of the initial reaction rate on reaction temperature and initial amount of catalyst was also studied for both catalysts. The lower apparent activation energy of 1 (11 kcal x mol(-1)) as compared with 2 (20 kcal x mol(-1)) is in accordance with the higher activity of the former.     

Synthesis of Ni-Ru alloy nanoparticles and their high catalytic activity in dehydrogenation of ammonia borane

We report the synthesis and characterization of new Ni(x)Ru(1-x) (x = 0.56-0.74) alloy nanoparticles (NPs) and their catalytic activity for hydrogen release in the ammonia borane hydrolysis process. The alloy NPs were obtained by wet-chemistry method using a rapid lithium triethylborohydride reduction of Ni(2+) and Ru(3+) precursors in oleylamine. The nature of each alloy sample was fully characterized by TEM, XRD, energy dispersive X-ray spectroscopy (EDX), and X-ray photoelectron spectroscopy (XPS). We found that the as-prepared Ni-Ru alloy NPs exhibited exceptional catalytic activity for the ammonia borane hydrolysis reaction for hydrogen release. All Ni-Ru alloy NPs, and in particular the Ni(0.74)Ru(0.26) sample, outperform the activity of similar size monometallic Ni and Ru NPs, and even of Ni@Ru core-shell NPs. The hydrolysis activation energy for the Ni(0.74)Ru(0.26) alloy catalyst was measured to be approximately 37?kJ?mol(-1). This value is considerably lower than the values measured for monometallic Ni (≈70?kJ?mol(-1)) and Ru NPs (≈49?kJ?mol(-1)), and for Ni@Ru (≈44?kJ?mol(-1)), and is also lower than the values of most noble-metal-containing bimetallic NPs reported in the literature. Thus, a remarkable improvement of catalytic activity of Ru in the dehydrogenation of ammonia borane was obtained by alloying Ru with a Ni, which is a relatively cheap metal.     

Effect of Ni Loading on the Catalytic Properties of Molybdenum Oxides for the Isomerization of Heptane

The catalytic properties of MoOx and incorporation Ni onto the MoOx for the isomerization of heptane have been investigated under atmospheric pressure at different conditions such as different flow rate of H2,different reaction temperature tec. Compared with MoOx, the Ni addition to the MoOx markedly improved the isomerization activity of heptane by improving the reducibility of MoO3 and activation of H2 in reaction.