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首页> 外文期刊>Organic Geochemistry: A Publication of the International Association of Geochemistry and Cosmochemistry >Role of NSO compounds during primary cracking of a Type II kerogen and a Type III lignite
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Role of NSO compounds during primary cracking of a Type II kerogen and a Type III lignite

机译:NSO化合物在II型干酪根和III型褐煤一次裂解中的作用

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The aim of this work is to follow the generation of NSO compounds during the artificial maturation of an immature Type II kerogen and a Type III lignite in order to determine the different sources of the petroleum potential during primary cracking. Experiments were carried out in closed system pyrolysis in the temperature range from 225 to 350 degrees C. Two types of NSOs were recovered: one is soluble in n-pentane and the second in dichloromethane. A kinetic scheme was optimised including both kerogen and NSO cracking. It was validated by complementary experiments carried out on isolated asphaltenes generated from the Type II kerogen and on the total n-pentane and DCM extracts generated from the Type Ill lignite. Results show that kerogen and lignite first decompose into DCM NSOs with minor generation of hydrocarbons. Then, the main source of petroleum potential originates from secondary cracking of both DCM and n-pentane NSOs through successive decomposition reactions. These results confirm the model proposed by Tissot [Tissot, B., 1969. Premieres donnees sur les mecanismes et la cinetique de la formation du petrole dans les bassins sedimentaires. Simulation d'un schema reactionnel sur ordinateur. Oil and Gas Science and Technology 24, 470-501] in which the main source of hydrocarbons is not the insoluble organic matter, but the NSO fraction. As secondary cracking of the NSOs largely overlaps that of the kerogen, it was demonstrated that bulk kinetics in open system is a result of both kerogen and NSO cracking. Thus, another kinetic scheme for primary cracking in open system was built as a combination of kerogen and NSO cracking. This new kinetic scheme accounts for both the rate and amounts of hydrocarbons generated in a closed pyrolysis system. Thus, the concept of successive steps for hydrocarbon generation is valid for the two types of pyrolysis system and, for the first time, a common kinetic scheme is available for extrapolating results to natural case studies. (c) 2007 Elsevier Ltd. All rights reserved.
机译:这项工作的目的是跟踪未成熟的II型干酪根和III型褐煤的人工成熟过程中NSO化合物的产生,以便确定初次裂解过程中石油潜力的不同来源。在温度为225至350摄氏度的密闭系统中进行热解实验。回收了两种NSO:一种可溶于正戊烷,另一种可溶于二氯甲烷。优化了动力学方案,包括干酪根和NSO裂解。通过对由II型干酪根产生的分离的沥青质以及由III型褐煤产生的总正戊烷和DCM提取物进行的补充实验验证了该方法。结果表明,干酪根和褐煤首先分解为DCM NSO,生成的烃较少。然后,石油潜力的主要来源来自DCM和正戊烷NSOs通过连续的分解反应的二次裂解。这些结果证实了天梭[Tissot,B.,1969年提出的模型。石油和石油沉积的首映。模拟d'un模式反应堆。石油和天然气科学与技术24,470-501],其中烃的主要来源不是不溶性有机物,而是NSO馏分。由于NSO的二次裂解在很大程度上与干酪根的二次裂解重叠,因此证明了开放系统中的整体动力学是干酪根和NSO裂解的结果。因此,将干酪根和NSO裂解相结合,建立了开放系统中初级裂解的另一种动力学方案。这种新的动力学方案说明了密闭热解系统中生成烃的速率和数量。因此,用于烃生成的连续步骤的概念对于两种类型的热解系统都是有效的,并且首次有通用的动力学方案可用于将结果外推到自然案例研究中。 (c)2007 Elsevier Ltd.保留所有权利。

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