Page 467 - Enhanced Oil Recovery in Shale and Tight Reservoirs

39.7
00
06
05
þ
þ
þ
0.00E
2.00E
9.30E
05
05
04
þ
þ
þ
1.77E
2.33E
5.35E
04
06
05
þ
þ
þ
2017).dcont'd
4.40E
1.00E
7.60E
heat
heat
heat
Sheng,
þ
þ
þ
CO x
CO x
CO x
þ
Coke
H 2 O
Coke
and
þ
þ
þ
heat
heat
heat
þ
(Zhang 432 Oil Activation density Enthalpy energy Frequency API Btu/lbmole Btu/lbmole factor 05 þ 2.84E 03 þ 3.25E 05 þ 1.50E Energy þ CO 2 32.7 04 þ 7.74E 10 þ 3.35E C7eC11 þ Coke 04 þ 7.74E 10 þ 3.35E C7eC11 þ 04 þ 4.86E 10 þ 4.00E H 2 O þ CO 2 / 04 þ 4.86E 10 þ 4.00E H 2 O CO 2 H 2 O 04 þ 4.
þ
H 2 O
H 2 O
H 2 O
/
/
þ
/
/
CO 2
HO
Asp
þ
þ
þ
O 2
O 2
O 2
data Reactions / / Coke / O 2 þ þ O 2 / O 2 Coke O 2 þ CO x þ þ CO x þ / O 2 C7eC15 þ CO x þ / O 2 / O 2 / O 2 þ LO / / O 2 / O 2 / O 2
kinetic O 2 þ C12eC17 þ C7eC11 C12eC17 þþ þ / C7eC15 H 2 O C16eC26 H 2 O þ / C16eC25 H 2 O þ þ þ / O 2 þ þ þ þ
with CO C18 C18 Coke C27 Coke C26 C26p Coke MO Asp LO MO HO Coke
schemes Cracking Combustion oil cracking Combustion oil cracking Combustion Cracking Combustion
reaction Heavy Heavy LTO
of al. al. et Batenburg 2013
Summary Authors et Fassihi 2000 Zwart 2008 van 2010 al. Barzin
13.7 de et
Table Oil