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

被引:0
|
作者
Xu, Shao-Tao [1 ]
Lue, Xiao-Shu [2 ,5 ,6 ]
Wang, Han [2 ,4 ]
Sun, You-Hong [1 ,2 ,3 ,4 ]
Kang, Shi-Jie [7 ]
Wang, Zhen-Dong [8 ]
Guo, Wei [2 ,3 ,4 ]
Deng, Sun-Hua [2 ,3 ]
机构
[1] China Univ Geosci, Sch Engn & Technol, Beijing 100083, Peoples R China
[2] Jilin Univ, Coll Construct Engn, Changchun 130021, Jilin, Peoples R China
[3] Jilin Univ, Natl Local Joint Engn Lab Insitu Convers Drilling, Changchun 130021, Jilin, Peoples R China
[4] Jilin Univ, Key Lab Minist Nat Resources Drilling & Exploitat, Changchun 130021, Jilin, Peoples R China
[5] Univ Vaasa, Dept Elect Engn & Energy Technol, POB 700, FI-65101 Vaasa, Finland
[6] Aalto Univ, Sch Engn, Dept Civil & Struct Engn, POB 12100, FIN-02015 Espoo, Finland
[7] Chinese Acad Sci, Ganjiang Innovat Acad, Ganzhou 341000, Jiangxi, Peoples R China
[8] Shaanxi Coal Geol Grp CO Ltd, Key Lab Coal Explorat & Comprehens Utilizat, Minist Nat & Resources, Xian 710021, Shaanxi, Peoples R China
基金
国家重点研发计划; 中国博士后科学基金; 中国国家自然科学基金;
关键词
Oil shale; Oxygen initiation process; Isothermal kinetic analysis; Heat release; Product release characteristics; OXIDATION BEHAVIOR; ALTERNATIVE ENERGY; KINETICS; PRODUCTS;
D O I
10.1016/j.petsci.2024.07.024
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
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 degrees C. 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. (c) 2024 The Authors. Publishing services by Elsevier B.V. on behalf of KeAi Communications Co. Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/ 4.0/).
引用
收藏
页码:4481 / 4496
页数:16
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