一种制备用于正庚烷异构化的Pt-WO3/ZrO2催化剂的新方法

 采用不同的ZrO(OH)2前驱体制备了WO3-ZrO2和Pt/WO3-ZrO2催化剂. 结果表明,与常规的ZrO(OH)2水凝胶为前驱体制备的WO3-ZrO2-CP催化剂相比,以常压流动氮气中干燥处理的ZrO(OH)2乙醇凝胶为前驱体制备的WO3-ZrO2-AN催化剂对正庚烷临氢异构化反应具有更高的催化活性. 当在 WO3-ZrO2-AN中添加少量Pt时,其催化活性和稳定性均得到显著提高. 表明以ZrO(OH)2醇凝胶为前驱体可以制备出高效稳定的Pt/WO3-ZrO2-AN催化剂.     

正庚烷与正十四烷在Pt/SAPO-11催化剂上临氢异构化

采用连续流动固定床反应装置，研究了0.6%Pt/SAPO-11催化剂上正庚烷与正十四烷的临氢异构转化。实验结果表明，在反应温度200 ℃～420 ℃，压力0.5 MPa，质量空速2.0 h－1的反应条件下，两种原料在高转化时均可保持90%以上的异构化选择性。在转化率小于55%时，C7与C14临氢异构所遵循的反应规律是一致的，即异构化和裂解的相对反应速率相同。依据产物分布组成随转化率变化的规律，提出了烷烃在Pt/SAPO-11催化剂上加氢转化的反应网络。同时，实验结果支持烷烃异构化反应在分子筛孔道内进行的观点。     

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.     

Effect of Crystallization of Zirconium Hydroxide on the Structure and Isomerization Performance for n-Heptane Hydroisomerization of Ni-WO3/ZrO2

采用XRD、BET、IR、SEM、NH3-TPD方法对以无定形Zr（OH）4和已晶化的ZrO2为载体制备的Ni-WO3/ZrO2催化剂进行了表征,考察了载体晶化对催化剂结构、酸性及催化性能的影响。结果表明,载体晶化减弱了W与Zr间的相互作用,抑制了四方相ZrO2的生成,减少了催化剂上强酸中心的数目,从而降低了Pt-WO3/ZrO2催化剂上正庚烷异构化反应活性.     

Hydroisomerization of n-heptane over bimetal-bearing H_3PW_(12)O_(40) catalysts supported on dealuminated USY zeolite

The bimetal-bearing (CePt or LaPt) 12-tungstophosphoric acid (H3PW12O40 (PW)) catalysts supported on dealuminated USY zeolite (DUSY) were prepared by impregnation and characterized by XRD, BET, IR, and H2-chemisorption. Their catalytic activities were tested in the hydroisomerization of n-heptane with a continuous atmospheric fixed-bed reactor. After the steam treatment combined with the acid leaching, as well as the supporting with PW and the bimetals, the DUSY support retains the Y zeolite porosity and the PW well keeps its Keggin structure in catalysts. The doping of Ce into the catalysts enhances the dispersion of Pt on the catalyst surface. The Pt-bearing PW catalysts doped with Ce or La, especially Ce, exhibit much higher catalytic activity and selectivity than the catalysts without dopants at lowered reaction temperatures. At the optimal reaction conditions, i.e., the reaction temperature of 250℃ and WHSV of 1.4 h1, the catalyst with a Pt loading of 0.4%, PW loading of 10% and a molar ratio of Ce to Pt of 15:1 shows a conversion of n-heptane of 70.3% with a high selectivity for isomerization products of 94.1%.     

正庚烷化学动力学简化模型的构建及优化

提出了一个新的适用于HCCI发动机燃烧模拟的正庚烷化学反应动力学简化模型(40种组分和62个反应)。由三个子模型组成:低温反应子模型是在Li等人模型的基础上,定义具体的醛类(RCHO)产物和小分子碳氢产物(Rs)而构建;增加了用于链接低温反应向高温反应过渡的大分子直接裂解成小分子反应子模型;高温反应子模型是在Griffiths等人模型的基础上,去除了无关的基元反应,增加两个关于CO和CH3O的氧化反应而构建。另外,采用遗传优化技术对模型动力学参数进行调整。计算表明,新模型能够在当量比0．2-1．2,温度从300-3000 K的范围内精确模拟正庚烷HCCI燃烧时冷焰和热焰反应过程,与详细模型(544种组分和2446个反应)计算结果吻合较好。     

Issues arising in the construction of QSSA mechanisms: the case of reduced n-heptane/air models for premixed flames

A model reduction methodology, based on the quasi steady-state approximation (QSSA), is employed for the construction of reduced mechanisms in the case of an n-heptane/air premixed flame. Several issues related to the construction of these reduced mechanisms are discussed; such as the influence of the size of the starting skeletal mechanism, the stiffness reduction, and the truncation/simplification of (i) the expressions of the global rates and (ii) the steady-state relations. The starting point for the reduction is two skeletal mechanisms that involve 177/768 and 66/326 species/reactions, respectively [J. Prager, H.N. Najm, M. Valorani, and D.A. Goussis, Skeletal mechanism generation with CSP and validation for premixed n-heptane flames, Proc. Combust. Inst. 32 (2009), pp. 509–517] and which were derived from the detailed mechanism of Curran et al. [H.J. Curran, P. Gaffuri, W.J. Pitz, and C.K. Westbrook, A comprehensive modeling study of iso-octane oxidation, Combust. Flame 129 (2002), pp. 253–280], which involves 561/2538 species/reactions. From these two skeletal mechanisms, a number of reduced mechanisms of various sizes are produced and analysed. The validity of the reduced mechanism with the minimum size is demonstrated by considering its accuracy regarding the mass fractions of major and minor species, the temperature, and the flame speed, over a wide range of equivalence ratios and pressures.     

高压下氮气在正庚烷-正辛烷混合溶剂中的溶解度研究

高压下气体在混合溶剂中溶解度的测定与研究,无论在理论研究或是实际应用方面均具有重要的意义。但由于进行这类研究,特别是在升温升压下,费时,昂贵和有一定难度,目前这方面的数据十分缺乏。作为本实验室研究系列之一部份,本文将报导文献中尚未见发表的氮气在正庚烷-正辛烷混合溶剂中的溶解度研究结果。实验部份1.试剂氮气纯度99.999%,由北京氧气厂提供;正庚烷,正辛烷由北京化工厂产分析纯试剂,本实验室又进一步精馏纯化。纯化后的试剂用气相色谱分析其纯度高于99.4%.混合溶剂的组成用重量法配制。     

正庚烷相变序列的高压拉曼光谱研究

在室温条件下, 利用金刚石对顶砧超高压实验技术, 对液态的正庚烷进行了原位高压拉曼光谱研究, 采用红宝石荧光压标测压, 实验的最高压力为20.78 GPa。实验中发现, 当压力达到1.2 GPa左右时, 原本透明的样品腔内有小晶粒形成, 此时测量的拉曼谱上发现有许多新的拉曼峰出现。因此, 我们判断正庚烷在此压力下发生了一次相变; 当压力增加到3 GPa左右时, 在92.42 cm-1和2913.6 cm-1处又出现了2个新的拉曼峰, 并且拉曼频移随压力变化的曲线出现拐点, 我们推测在此压力下正庚烷可能又发生第二次相变; 当压力高于14.5 GPa时, 正庚烷发生了第三次压致相变; 而当压力介于7.5~14.5 GPa之间正庚烷处于两相共存的状态。我们给出了液体正庚烷在高压下的相变序列为: 液相-旋转相Ⅲ-旋转相Ⅳ-结晶相。该研究结果为进一步理解和研究其他正烷烃在高压下的结构、物理和化学特性提供了理论基础。     

金属羰基络合物制备的Pt-Re/Al_2O_3催化剂的性能 Ⅰ.不同方法制备的Pt-Re/Al_2O_3催化剂上正庚烷的转化

考察了由[Pt_3(CO)_6]_5[NEt_4]_2与Re_2(CO)_(10)共浸或分浸制备的一系列催化剂在接近工业运转的压力下的正庚烷转化反应。以羰基金属原子簇化合物作为前身物制备的Pt-Re/Al_2O_3催化剂的活性、芳构化选择性和稳定性等明显地优于常规的以H_2PtCl_6与HReO_4溶液共浸制备的催化剂。常规Pt-Re/Al_2O_3催化剂的活性和稳定性比Pt/Al_2O_3好,但芳构化选择性降低,若引入Re_2(CO)_(10),则其催化活性、芳构化选择性和稳定性均显著提高。不同方法制备的Pt-Re/Al_2O_3催化剂的活性和稳定性的变化趋势为Pt_5Re_2>Pt_5 Re_2>Pt Re_2>PtRe,表明Pt,Re之间存在相互作用程度的差异。