2023
DOI: 10.1016/j.energy.2023.126700
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A coupled thermo-hydro-mechanical-chemical model for production performance of oil shale reservoirs during in-situ conversion process

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Cited by 18 publications
(10 citation statements)
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“…The fitting results show that the porosity and pore radius were approximately positively correlated with the heat treatment temperature (Figure 4a,b), while the tortuosity was negatively correlated with the heat treatment temperature (Figure 4c). According to the characteristics of the relationship curve, porosity, pore radius, and tortuosity could be divided into three stages with the increase in heating temperature, as shown in Figure 4, corresponding to the three-stage change in the pore structure of oil shale [39][40][41]. In the three stages of <300, 300~550, and >550 degrees centigrade, the pore structure was mainly controlled through inorganic thermal stress, pyrolysis, and inorganic cracking.…”
Section: Influence Of Heating Temperature On Shale Matrix Transportmentioning
confidence: 99%
“…The fitting results show that the porosity and pore radius were approximately positively correlated with the heat treatment temperature (Figure 4a,b), while the tortuosity was negatively correlated with the heat treatment temperature (Figure 4c). According to the characteristics of the relationship curve, porosity, pore radius, and tortuosity could be divided into three stages with the increase in heating temperature, as shown in Figure 4, corresponding to the three-stage change in the pore structure of oil shale [39][40][41]. In the three stages of <300, 300~550, and >550 degrees centigrade, the pore structure was mainly controlled through inorganic thermal stress, pyrolysis, and inorganic cracking.…”
Section: Influence Of Heating Temperature On Shale Matrix Transportmentioning
confidence: 99%
“…To explore the generation process of oil and gas, the evolution of kerogen pyrolytic products in a closed system was studied in detail [7,12,14,54]. In general, pyrolytic products generated from kerogen can be described as follows [7,[10][11][12][13][14][15][16]:…”
Section: Medium-temperature Stagementioning
confidence: 99%
“…The factors affecting the efficiency of in situ conversion mainly include the final pyrolytic temperature, heating rate, and constant temperature time [7,55]. From the experimental simulation and field experiments, it can be concluded that the pyrolysis of kerogen has an initial temperature (ICT) regardless of what kind of shale-oil conversion technology is used [7,11,20,44,45,[49][50][51][55][56][57]. Therefore, only when the temperature exceeds the ICT is the increase in heat carrier energy called effective pyrolysis energy [20].…”
Section: Medium-temperature Stagementioning
confidence: 99%
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