Integrating liquid CO_(2)phase transition blasting(LCPTB)technology with hydraulic fracturing(HF)methods can help reduce wellbore damage,create multiple radial fractures,and establish a complex fracture network.This a...Integrating liquid CO_(2)phase transition blasting(LCPTB)technology with hydraulic fracturing(HF)methods can help reduce wellbore damage,create multiple radial fractures,and establish a complex fracture network.This approach significantly increases the recovery efficiency of low-permeability oil and gas fields.Accurately calculating the number of fractures caused by LCPTB is necessary to predict production enhancement effects and optimize subsequent HF designs.However,few studies are reported on large-scale physical model experiments in terms of a method for calculating the fracture number.This study analyzed the initiation and propagation of cracks under LCPTB,derived a calculation formula for crack propagation radius under stress waves,and then proposed a new,fast,and accurate method for calculating the fracture number using the principle of mass conservation.Through ten rock-breaking tests using LCPTB,the study confirmed the effectiveness of the proposed calculation approach and elucidated the variation rule of explosion pressure,rock-breaking scenario,and the impact of varying parameters on fracture number.The results show that the new calculation method is suitable for fracturing technologies with high pressure rates.Recommendations include enlarging the diameter of the fracturing tube and increasing the liquid CO_(2) mass in the tube to enhance fracture effectiveness.Moreover,the method can be applied to other fracturing technologies,such as explosive fracturing(EF)within HF formations,indicating its broader applicability and potential impact on optimizing unconventional resource extraction technologies.展开更多
The non-aqueous solid-liquid biphasic solvent of 2-amino-2-methyl-1-propanol(AMP)/piperazine(PZ)/dipropylene glycol dimethyl ether(DME)features a high CO_(2)absorption loading,favorable phase separation behavior and h...The non-aqueous solid-liquid biphasic solvent of 2-amino-2-methyl-1-propanol(AMP)/piperazine(PZ)/dipropylene glycol dimethyl ether(DME)features a high CO_(2)absorption loading,favorable phase separation behavior and high regeneration efficiency.Different with the liquid-liquid phase change solvent,the reaction kinetics of CO_(2)capture into solid-liquid biphasic solvent was rarely studied.In the present work,the reaction kinetics of CO_(2)absorption into AMP/PZ/DME solid-liquid biphasic solvent was investigated into the double stirred kettle reactor.The absorption reaction followed a pseudo-first-order kinetic model according to the zwitterion mechanism.The overall reaction rate constant(kov)and the enhancement factor(E)of CO_(2)absorption both increased with increasing temperature.The total mass transfer resistance of the absorbent decreased with increasing temperature and increased with increasing absorption loading,so the higher reaction temperature was conducive to the absorption,and the liquid phase mass transfer resistance was the main factor affecting the absorption rate.展开更多
基金supported by the National Key R&D Program of China (Grant No.2020YFA0711802).
文摘Integrating liquid CO_(2)phase transition blasting(LCPTB)technology with hydraulic fracturing(HF)methods can help reduce wellbore damage,create multiple radial fractures,and establish a complex fracture network.This approach significantly increases the recovery efficiency of low-permeability oil and gas fields.Accurately calculating the number of fractures caused by LCPTB is necessary to predict production enhancement effects and optimize subsequent HF designs.However,few studies are reported on large-scale physical model experiments in terms of a method for calculating the fracture number.This study analyzed the initiation and propagation of cracks under LCPTB,derived a calculation formula for crack propagation radius under stress waves,and then proposed a new,fast,and accurate method for calculating the fracture number using the principle of mass conservation.Through ten rock-breaking tests using LCPTB,the study confirmed the effectiveness of the proposed calculation approach and elucidated the variation rule of explosion pressure,rock-breaking scenario,and the impact of varying parameters on fracture number.The results show that the new calculation method is suitable for fracturing technologies with high pressure rates.Recommendations include enlarging the diameter of the fracturing tube and increasing the liquid CO_(2) mass in the tube to enhance fracture effectiveness.Moreover,the method can be applied to other fracturing technologies,such as explosive fracturing(EF)within HF formations,indicating its broader applicability and potential impact on optimizing unconventional resource extraction technologies.
基金supported by the National Natural Science Foundation of China(No.22276064)the Youth Innovation Grant of Xiamen,Fujian Province(No.3502Z20206006)+1 种基金the MOE Key Laboratory of Resources and Environmental System Optimization(No.KLRE-KF202205)Fujian Science and Technology Project(No.2022Y3007).
文摘The non-aqueous solid-liquid biphasic solvent of 2-amino-2-methyl-1-propanol(AMP)/piperazine(PZ)/dipropylene glycol dimethyl ether(DME)features a high CO_(2)absorption loading,favorable phase separation behavior and high regeneration efficiency.Different with the liquid-liquid phase change solvent,the reaction kinetics of CO_(2)capture into solid-liquid biphasic solvent was rarely studied.In the present work,the reaction kinetics of CO_(2)absorption into AMP/PZ/DME solid-liquid biphasic solvent was investigated into the double stirred kettle reactor.The absorption reaction followed a pseudo-first-order kinetic model according to the zwitterion mechanism.The overall reaction rate constant(kov)and the enhancement factor(E)of CO_(2)absorption both increased with increasing temperature.The total mass transfer resistance of the absorbent decreased with increasing temperature and increased with increasing absorption loading,so the higher reaction temperature was conducive to the absorption,and the liquid phase mass transfer resistance was the main factor affecting the absorption rate.
