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Molecular modeling of the catalytic hydrocracking of complex mixtures: Reactions of alkyl aromatic and alkyl polynuclear aromatic hydrocarbons.

机译:复杂混合物催化加氢裂化的分子模型:烷基芳烃和烷基多核芳烃的反应。

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Increasing legislative and environmental concerns have focused attention on determining molecular composition of heavy oil feedstocks and their refined products. However, tracking the 10{dollar}sp3{dollar}-10{dollar}sp5{dollar} molecular constituents during heavy oil upgrading has posed a unique challenge to traditional process modeling, in which the molecules are grouped according to global properties, such as boiling point fractions and solubilities.; In an effort to incorporate chemically significant information into a process model, a molecular approach was used to simulate the hydrocracking chemistry of example heavy gas oil mixtures. This approach consisted of three elements: (1) the development of reaction pathways and kinetics for model systems, (2) the formulation of Linear Free Energy Relationships (LFERs) to account for reactivity dependence on reactant structure, and (3) the incorporation of the pathway analysis into a simulation of complex heavy oil mixtures.; The hydrocracking reaction pathways and kinetics of alkylbenzenes and alkyl polynuclear aromatics (PNAs), likely present in typical gas oils, were investigated over a NiW/USY zeolite. Langmuir-Hinshelwood-Hougen-Watson (LHHW) rate parameters were determined for an extensive model compound database that included hydrocracking reactions of alkyl aromatics with side-chains ranging from 0-19 and aromatic rings from 1-4. The principal reactions observed for alkylbenzenes and alkylPNAs were ring-dealkylation, side-chain cracking and ring-closure. Additionally, alkylPNAs underwent hydrogenation.; LFERs existed for ring-dealkylation, hydrogenation and ring-closure. The ring-dealkylation and ring-closure rate constant for C2- to {dollar}sim{dollar}C9 alkylbenzenes followed the intrinsic chemistry behavior. However, the intrinsic correlations failed beyond this length, which signified the onset of extrinsic effects. LFERs for the hydrogenation, ring-dealkylation and ring-closure of alkylPNAs were successfully identified. Although the decrease in reaction rate constants with ring number for dealkylation and closure followed the intrinsic correlations, these results were also consistent with the presence of extrinsic effects as well.; The rate parameters obtained from the reaction pathway analysis of alkylaromatics, alkylPNAs and LFERs were used as input into a molecular model. Monte Carlo techniques were employed to stochastically build and react example gas oil mixtures. The model predictions in all cases were in reasonable agreement to the experimental hydrocracking yields.
机译:越来越多的立法和环境关注集中在确定重油原料及其精制产品的分子组成上。但是,在重油改质过程中跟踪10 {dollar} sp3 {dollar} -10 {dollar} sp5 {dollar}分子组成对传统工艺建模提出了一个独特的挑战,在传统工艺建模中,根据全局特性将分子分组,例如沸点分数和溶解度。为了将化学上重要的信息整合到过程模型中,使用了分子方法来模拟示例重瓦斯油混合物的加氢裂化化学反应。该方法包括三个要素:(1)模型系统的反应途径和动力学的发展;(2)线性自由能关系(LFER)的制定以考虑反应物对反应物结构的依赖性;(3)引入将路径分析模拟为复杂的重油混合物。在NiW / USY沸石上研究了可能存在于典型粗柴油中的烷基苯和烷基多核芳烃(PNAs)的加氢裂化反应途径和动力学。为广泛的模型化合物数据库确定了Langmuir-Hinshelwood-Hougen-Watson(LHHW)速率参数,该数据库包括侧链为0-19的烷基芳族化合物和1-4为芳族环的加氢裂化反应。观察到的烷基苯和烷基PNA的主要反应是环脱烷基,侧链裂化和闭环。另外,烷基PNA进行氢化。存在用于环脱烷基,氢化和闭环的LFER。从C 2到{sim} C 9烷基苯的环脱烷基化和闭环速率常数遵循内在化学行为。然而,内在的相关性超过了这个长度而失败了,这表明了外在效应的开始。已成功鉴定了用于烷基PNAs的氢化,环脱烷基和闭环的LFER。尽管脱烷基和闭合的反应速率常数随环数的降低遵循内在相关性,但这些结果也与存在外在效应一致。从烷基芳族化合物,烷基PNAs和LFERs的反应路径分析获得的速率参数用作分子模型的输入。蒙特卡罗技术被用来随机地建立和反应示例性瓦斯油混合物。在所有情况下,模型预测均与实验加氢裂化产率合理地吻合。

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