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REACTION PROPERTIES OF RESIDUE FRACTIONS FROM LOW SEVERITY UPGRADING

机译:低严重度升级带来的残留馏分的反应特性

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摘要

As heavy oil production increases faster than the supply of diluents, such as natural gas condensate, the need for new strategies to reduce viscosity for pipelining are required. Low-severity upgrading processes for minimal field processing are becoming more attractive, but thermal cracking processes tend to be unstable with time, so that pipelines and storage tanks are fouled with sludge deposits. One mechanism for instability of a processed oil with time is polymerization reactions, which are very sensitive to oxygen and other contaminants. Because this type of instability is driven by chemical reaction, in addition to phase behavior and solubility, we term this phenomenon "chemical instability". The presence of any oxygen in thermally cracked oils may sensitize the mixture by forming peroxides, so that dimers and trimers can form with time. This increase in molecular weight, after processing is complete, is likely a major cause of chemical instability that can lead to sediments or to changes in physical and reactive properties. This presentation will give a case study on how the reactivity of thermally cracked material changes upon contact with air. By using a micro-scale flash coker, we can observe the behavior of thermally processed samples at temperatures of 450-550℃, and gain insights into process performance in downstream cracking and coking units.
机译:由于重油产量的增长快于稀释剂(例如天然气凝析油)的供应,因此需要采取新的策略来降低管道粘度。用于最低限度现场处理的低严重性升级过程变得越来越有吸引力,但是热裂解过程会随着时间的流逝而变得不稳定,因此管道和储罐会积聚污泥。加工油随时间不稳定的一种机制是聚合反应,该反应对氧气和其他污染物非常敏感。因为这种不稳定性是由化学反应驱动的,所以除了相行为和溶解度之外,我们将此现象称为“化学不稳定性”。热裂化油中任何氧气的存在都可能通过形成过氧化物而使混合物敏感,从而使二聚体和三聚体随时间形成。加工完成后,分子量的增加可能是化学不稳定性的主要原因,该化学不稳定性可能导致沉积物或物理和反应性质的变化。本演讲将提供案例研究,说明热裂化材料与空气接触后反应性如何变化。通过使用微型闪速焦化器,我们可以观察热处理样品在450-550℃的温度下的行为,并深入了解下游裂化和焦化装置的工艺性能。

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