TY - JOUR
T1 - Influence factors of coking amount during recovery of heavy oil by air injection
AU - Jiang, Hang
AU - Xu, Qianghui
AU - Ma, Desheng
AU - Tan, Wenbin
AU - Huang, Jia
AU - Li, Yang
AU - Chen, Xi
AU - Shi, Lin
N1 - Publisher Copyright:
© 2016, Editorial Office of ACTA PETROLEI SINICA. All right reserved.
PY - 2016/8/1
Y1 - 2016/8/1
N2 - Through building the experimental apparatus for reservoir HTHP reaction simulation and physically simulating the coke generation process during recovery of heavy oil by air injection, a study was conducted on the influences of reaction atmosphere, temperature, pressure and air ventilation intensity on the coking amount with certain Xinjiang heavy oil. The research indicated that in the air atmosphere, the low temperature oxidization (LTO) of crude oil can significantly promoted coke generation. with the reaction pressure 5 MPa, each gram of heavy oil can generate the maximum coking amount of 0.375 g, 2.5 times over that in N2 atmosphere. Influenced by LTO, the initial coke generation temperature is lower than that in N2 atmosphere by nearly 200℃. With the pressure rising, the aggravated LTO can increase the coking amount; when the pressure exceeds 5 MPa, its effect is not significant. With the increase of air ventilation intensity, the coking amount is not continuously increased, and a peak will appear at around 33.4 N·m3/(m2·h). A comparative analysis was carried out on the influences of coke high-temperature oxidization consumption as well as crude-oil component distillation and weightloss on coking amount. The results indicated that coke oxidization was the major cause of the reduction in net coking amount with the temperature ranging from 225℃ to 300℃ in air atmosphere. When the temperature reaches 450℃ in N2 atmosphere, the aggregated crude-oil pyrolysis condensation reaction can increase the coking amount, but the further rising of temperature will lead to coke pyrolysis and weightloss, resulting in a decline in coking amount. Additionally, the experiments revealed that when the temperature exceeds 200℃, the oil sand center temperature in the reaction tube was higher than the outer-wall heating control temperature. The analysis results showed that the temperature exceeding phenomenon was caused by the LTO of crude oil component and the high temperature oxidation of certain coke with high activity; This heavy oil has the spontaneous ignition potential.
AB - Through building the experimental apparatus for reservoir HTHP reaction simulation and physically simulating the coke generation process during recovery of heavy oil by air injection, a study was conducted on the influences of reaction atmosphere, temperature, pressure and air ventilation intensity on the coking amount with certain Xinjiang heavy oil. The research indicated that in the air atmosphere, the low temperature oxidization (LTO) of crude oil can significantly promoted coke generation. with the reaction pressure 5 MPa, each gram of heavy oil can generate the maximum coking amount of 0.375 g, 2.5 times over that in N2 atmosphere. Influenced by LTO, the initial coke generation temperature is lower than that in N2 atmosphere by nearly 200℃. With the pressure rising, the aggravated LTO can increase the coking amount; when the pressure exceeds 5 MPa, its effect is not significant. With the increase of air ventilation intensity, the coking amount is not continuously increased, and a peak will appear at around 33.4 N·m3/(m2·h). A comparative analysis was carried out on the influences of coke high-temperature oxidization consumption as well as crude-oil component distillation and weightloss on coking amount. The results indicated that coke oxidization was the major cause of the reduction in net coking amount with the temperature ranging from 225℃ to 300℃ in air atmosphere. When the temperature reaches 450℃ in N2 atmosphere, the aggregated crude-oil pyrolysis condensation reaction can increase the coking amount, but the further rising of temperature will lead to coke pyrolysis and weightloss, resulting in a decline in coking amount. Additionally, the experiments revealed that when the temperature exceeds 200℃, the oil sand center temperature in the reaction tube was higher than the outer-wall heating control temperature. The analysis results showed that the temperature exceeding phenomenon was caused by the LTO of crude oil component and the high temperature oxidation of certain coke with high activity; This heavy oil has the spontaneous ignition potential.
KW - Air injection recovery
KW - Coke
KW - High temperature oxidation
KW - In-situ combustion
KW - Low temperature oxidation
UR - http://www.scopus.com/inward/record.url?scp=84985898281&partnerID=8YFLogxK
U2 - 10.7623/syxb201608009
DO - 10.7623/syxb201608009
M3 - Article
AN - SCOPUS:84985898281
SN - 0253-2697
VL - 37
SP - 1030
EP - 1036
JO - Shiyou Xuebao/Acta Petrolei Sinica
JF - Shiyou Xuebao/Acta Petrolei Sinica
IS - 8
ER -