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430 Enhanced Oil Recovery in Shale and Tight Reservoirs
density
Oil API 13 04 06 07 05 00 07 07 06 00
Enthalpy Btu/lbmole þ 4.00E þ 4.06E þ 1.86E þ 2.35E þ 0.00E þ 1.57E þ 6.77E þ 1.22E þ 0.00E
Activation energy Btu/lbmole 04 þ 3.49E 04 þ 4.30E 04 þ 4.30E 04 þ 3.26E 05 þ 1.10E 05 þ 2.58E 05 þ 2.58E 05 þ 1.09E 05 þ 4.87E
06 06 06 06 03 08 08 00 15
Frequency factor þ 4.00E þ 1.00E þ 1.00E þ 1.00E þ 6.95E þ 5.03E þ 5.03E þ 6.95E þ 1.39E
2017).
Sheng, 14.5 CO x Coke þ inert Coke coke
and Asphaltenes Coke / 71 / H 2 O þ oil Water þ þ 19.35 16.64 4.59 0.43 þ
(Zhang / O 2 O 2 / Aspaltenes Coke Gas 1.06 coke 61 O 2 H 2 O O 2 / O 2 0.25 Light / energy Water / Water energy þ LO O 2 CO 2 / CO 2 / O 2 CO 2 C5eC20
/
data Reactions þ þ / / / / þ oil 19.35 þ 13 þ 87 þ H 2 O 1.03 þ / O 2 þ þ gas O 2 energy / O 2 þ gas 1.81 47.01 38.69 þ O 2 12.97 10.68 þ 1.12 0.93 þ /
kinetic Maltenes Asphaltenes Maltenes Asphaltenes Asphaltenes oil Heavy light oil CO x oil Heavy 63.4 þ þ CO x 1.0 oil Heavy oil inert þ Heavy þ gas þ inert / þ H 2 O þ H 2 O þ H2O C21eC30
with Light Coke Light Coke HO HO LO Coke
schemes Cracking Cracking Combustion Cracking Combustion Cracking Combustion Cracking
reaction LTO
of al. et 1984 Sierra
Summary Authors Belgrave 1993 al. et Lin Druganova 2010 al. Mercado Trevisan and 2014
13.7 et
Table Oil Bitumen Heavy oil

