TY - JOUR
T1 - Insight into kerogen II pyrolysis mechanism by master plot method based on TG-FTIR analysis
AU - Zhang, Yanlong
AU - Zhao, Qiuyang
AU - Lu, Hao
AU - Wang, Guozhu
AU - Song, Zhiwei
AU - Jin, Hui
AU - Guo, Liejin
N1 - Publisher Copyright:
© 2025 Elsevier Ltd
PY - 2025/9/1
Y1 - 2025/9/1
N2 - The study of hydrocarbon generation from kerogen pyrolysis holds significant industrial and technological importance. However, the pyrolysis process is complex and current understanding remains insufficient. This article combines TG-FTIR analysis with master plot method to analyze the overall and each stage pyrolysis models of Chang 7 shale kerogen. The results show that the pyrolysis of kerogen follows order reaction with exponent of 4.5 across all temperature. Pyrolysis process can be divided into three distinct stages. The first stage involves the decarboxylation of oxygen-containing organic matter, leading to the generation of CO2. The second stage encompasses the intense pyrolysis of aliphatic and aromatic organic matter. The third stage involves the transformation from semicoke into coke with the generation of a few hydrocarbon gases. Kerogen pyrolysis is divided into four independent pseudo components (abbreviation: pc) by Fraser Suzuki function, successively namely organic matter containing carboxyl groups, aromatic compounds in organic matter, aliphatic compounds, and coke. At lower heating rates, pyrolysis of pc1 and pc2 is primarily governed by surface reactions and nucleation models. Pc3 is predominantly influenced by surface reaction and diffusion models. At higher heating rates, pc1 and pc3 are primarily governed by surface reaction and diffusion models, whereas pc2 is predominantly influenced by nucleation model. Pc4 is influenced by all three models though it exhibits minimal variation with different heating rate. This paper provides theoretical guidance for the cognition of kerogen pyrolysis mechanism and its future development.
AB - The study of hydrocarbon generation from kerogen pyrolysis holds significant industrial and technological importance. However, the pyrolysis process is complex and current understanding remains insufficient. This article combines TG-FTIR analysis with master plot method to analyze the overall and each stage pyrolysis models of Chang 7 shale kerogen. The results show that the pyrolysis of kerogen follows order reaction with exponent of 4.5 across all temperature. Pyrolysis process can be divided into three distinct stages. The first stage involves the decarboxylation of oxygen-containing organic matter, leading to the generation of CO2. The second stage encompasses the intense pyrolysis of aliphatic and aromatic organic matter. The third stage involves the transformation from semicoke into coke with the generation of a few hydrocarbon gases. Kerogen pyrolysis is divided into four independent pseudo components (abbreviation: pc) by Fraser Suzuki function, successively namely organic matter containing carboxyl groups, aromatic compounds in organic matter, aliphatic compounds, and coke. At lower heating rates, pyrolysis of pc1 and pc2 is primarily governed by surface reactions and nucleation models. Pc3 is predominantly influenced by surface reaction and diffusion models. At higher heating rates, pc1 and pc3 are primarily governed by surface reaction and diffusion models, whereas pc2 is predominantly influenced by nucleation model. Pc4 is influenced by all three models though it exhibits minimal variation with different heating rate. This paper provides theoretical guidance for the cognition of kerogen pyrolysis mechanism and its future development.
UR - https://www.scopus.com/pages/publications/105001576758
U2 - 10.1016/j.fuel.2025.135237
DO - 10.1016/j.fuel.2025.135237
M3 - 文章
AN - SCOPUS:105001576758
SN - 0016-2361
VL - 395
JO - Fuel
JF - Fuel
M1 - 135237
ER -