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Original Paper | Open Access

Characterization of oxygen initiation process in the autothermic pyrolysis in-situ conversion of Huadian oil shale

Shao-Tao Xua, Xiao-Shu Lüb,e,f, Han Wangb,d( ), You-Hong Suna,b,c,d( ), Shi-Jie Kangg, Zhen-Dong Wangh, Wei Guob,c,d, Sun-Hua Dengb,c ( )
School of Engineering and Technology, China University of Geosciences, Beijing, 100083, China
College of Construction Engineering, Jilin University, Changchun, 130021, Jilin, China
National-Local Joint Engineering Laboratory of In-situ Conversion, Drilling and Exploitation Technology for Oil Shale, Jilin University, Changchun, 130021, Jilin, China
Key Lab of Ministry of Natural Resources for Drilling and Exploitation Technology in Complex Conditions, Jilin University, Changchun, 130021, Jilin, China
Department of Electrical Engineering and Energy Technology, University of Vaasa, P.O.Box 700, FIN-65101, Vaasa, Finland
Department of Civil and Structural Engineering, School of Engineering, Aalto University, PO Box 12100, FIN-02015, Espoo, Finland
Ganjiang Innovation Academy, Chinese Academy of Sciences, Ganzhou, 341000, Jiangxi, China
Key Laboratory of Coal Exploration and Comprehensive Utilization, Ministry of Nature and Resources, Shaanxi Coal Geology Group Co., Ltd., Xi'an, 710021, Shaanxi, China

Edited by Min Li

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Abstract

The oxygen initiation process, one of the key processes in the early stage of the autothermic pyrolysis in-situ conversion technology, has not been deeply investigated, which seriously limits its development. In this study, the reaction behaviors, kinetic parameters, heat and product release characteristics during the isothermal oxygen initiation process of Huadian oil shale in O2/N2 mixtures with different oxygen concentrations and initiation temperatures were investigated via TG/DSC-FTIR. The results show that the samples exhibit three different reaction behaviors during the initiation stage, consisting of two main parts, i.e., the oxidative weight-gain and the oxidative reaction phases. The former phase is mainly characterized by the oxygen addition reaction that produces oxidizing groups which increase the sample mass. And the latter stage consists of two main subreactions. The first subreaction involves the oxidative cracking and pyrolysis of oxidizing groups and kerogen to produce fuel deposits such as residual carbon, while the second subreaction focuses on the oxidation of the resulting fuels. Furthermore, increasing the oxygen concentration significantly promotes the above reactions, leading to an increase in the reaction intensity and reaction rate. Owing to the combined effect of oxygen concentration and residual organic matter content, the total heat release increases with the increasing initiation temperature and reaches its maximum at 330–370 ℃. In addition, the preheating stage primarily produces hydrocarbon gases, while the initiation stage predominantly generates CO2. As the preheating temperature increases, the CO2 output intensifies, the required reaction time shortens, and the release becomes more concentrated. Based on these findings, a reaction mechanism for the oxygen initiation process of Huadian oil shale was proposed, and recommendations were provided for optimizing the construction process.

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Petroleum Science
Pages 4481-4496

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Cite this article:
Xu S-T, Lü X-S, Wang H, et al. Characterization of oxygen initiation process in the autothermic pyrolysis in-situ conversion of Huadian oil shale. Petroleum Science, 2024, 21(6): 4481-4496. https://doi.org/10.1016/j.petsci.2024.07.024

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Received: 08 January 2024
Revised: 23 July 2024
Accepted: 24 July 2024
Published: 26 July 2024
© 2024 The Authors.

This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).