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Reaction modeling approaches for complex hydrocarbon mixtures: Synthesis and application.

机译:复杂烃混合物的反应建模方法:合成与应用。

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The ability to process the heavy fraction of petroleum plays an important role in the financial viability of petroleum refining. Resid hydrotreating, visbreaking and coking are among the major processing steps in which large molecules are cracked into smaller molecules. The conversion in these processes is primarily thermal, with catalysts added in resid hydrotreating to desulfurize, demetallize and upgrade medium-size molecules. Understanding the mechanisms and kinetics of thermal reaction is a fundamental step in optimizing these processes.; Mechanistic reaction models summarize the current level of chemical knowledge in a form suitable for process optimization. The mechanistic modeling of pyrolysis reactions of petroleum mixtures has traditionally been limited by the complexity of the mixtures and a lack of computational power. A heavy-oil mixture may contain at least {dollar}10sp4{dollar} components and {dollar}10sp5{dollar} radicals and reaction pathways. Reaction models which seek to conserve this detail become very CPU intensive. A mechanism-based kinetic model has been developed with a small CPU requirement which would allow the model to be incorporated into a reactor simulation with fluid dynamics and heat and mass transfer.; The model utilizes a small CPU requirement by lumping radicals with similar reactivity together. A 42-lump subset of the {dollar}10sp5{dollar} radicals is used to describe all the elementary reactions with a high degree of accuracy. Structure/Reactivity relationships are utilized to provide rate constants for these elementary steps. The model predictions are compared to the results of full mechanistic simulations and the reaction of pure and synthetic mixtures of model compounds.; This dissertation also includes the development of useful tools to aid the modeling of thermal reaction systems. A simple modification of the long chain approximation has been developed and utilized in the Mechanism-Based Lumping model just described. Taylor series expansions also provide a way to derive semiempirical rate laws to approximate the mechanistic rate laws in limiting regimens. A simple inverse additive rule, analogous to parallel resistance addition, combines these limiting-case semiempirical rate laws to provide a rate law which is more accurate over the full range of experimental conditions.
机译:处理重质石油的能力在石油精炼的财务可行性中起着重要作用。残油加氢处理,减粘裂化和焦化是其中大分子裂化为小分子的主要加工步骤。这些过程中的转化主要是热转化,在渣油加氢处理中添加催化剂以对中型分子进行脱硫,脱金属和升级。了解热反应的机理和动力学是优化这些过程的基本步骤。机械反应模型以适合过程优化的形式总结了当前的化学知识水平。传统上,石油混合物热解反应的机理模型受到混合物的复杂性和缺乏计算能力的限制。重油混合物可能包含至少{sp} 10sp4 {dol}的成分和{sp} 10sp5 {dollar}的自由基和反应途径。试图保留此细节的反应模型会占用大量CPU。已经开发出了基于机制的动力学模型,其对CPU的要求很小,这将使该模型能够结合到具有流体动力学以及传热和传质的反应堆仿真中。该模型通过将具有相似反应性的自由基集中在一起来利用对CPU的少量需求。 {spul} 10sp5 {dollar}自由基的42块子集用于高度准确地描述所有基本反应。利用结构/反应性关系为这些基本步骤提供速率常数。将模型预测与完整机械模拟的结果以及模型化合物的纯混合物和合成混合物的反应进行比较。本文还包括开发有用的工具来辅助热反应系统的建模。已经开发了长链近似的简单修改,并在上述基于机制的集总模型中加以利用。泰勒级数展开还提供了一种方法,可以得出半经验率定律,以近似限定方案中的机械率定律。一个简单的逆加法则,类似于并联电阻加法,结合了这些极限情况半经验率定律,从而提供了在整个实验条件范围内更精确的率定律。

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