Table 16 Component properties
Component
Mid vol
on crude
API
SG at
60
F
Sulfur
% wt
Viscosity at
100
F cSt
Viscosity at
210
F cSt
Pour
point
F
1
1.31
12
0.5811 0.04
2
3.56
105
0.5983 0.05
3
5.96
87.5 0.6461 0.05
4
8.92
71.0 0.6988 0.06
0.27
5
11.49
65.0 0.7201 0.06
0.33
6
14.28
60.5 0.7370 0.07
0.45
7
16.34
57.3 0.7495 0.07
0.48
8
18.12
55.5 0.7567 0.08
0.52
9
20.32
53.0 0.7669 0.09
0.70
10
22.54
51.5 0.7732 0.10
0.78
11
24.75
49.0 0.7839 0.12
0.90
0.60
À88.0
12
27.19
46.5 0.7949 0.14
1.25
0.68
À76.0
13
30.22
44.5 0.8040 0.20
1.82
0.78
À60.0
14
33.25
41.5 0.8178 0.26
1.95
0.90
À48.5
15
36.06
40.0 0.8251 0.40
2.23
1.13
À34.0
16
38.8
38.5 0.8324 0.62
2.85
1.25
À22.0
17
41.56
37.0 0.8398 0.89
4.00
1.52
À0.08
18
44.26
35.5 0.8473 1.16
5.20
1.70
2.0
19
46.85
34.5 0.8524 1.48
6.25
1.85
16.0
Table 17 CDU product streams
Product
stream
BPCD
SG at
60
F
MM
lbs/CD
Sulfur
% wt
Visc at
100
F cSt
Visc at
210
F cSt
Pour
point
F
Gas +
LSR
6,075 0.6512
1.383
0.053
<À100
HSR
7,100 0.7550
1.863
0.091
0.58
0.43
<À100
Kero
4,545 0.8048
1.279
0.21
1.60
0.80
À58
Diesel
6,915 0.8420
2.036
0.869
4.0
1.5
0
Atmos
residue
25,365 0.9485
8.405
3.92
>100
9.8
>100
Total
50,000 0.8565
14.966
2.35
8.00
2.20
À5.0
Table 18 The VDU product streams
Product
stream
BPCD
SG at
60
F
MM
lbs/CD
Sulfur
% wt
Visc at
100
F cSt
Visc at
210
F cSt
Pour
point
F
LVGO
5,425 0.8789
1.667
2.18
13.0
3.0
15
HVGO
9,275 0.9218
2.990
3.10
49.0
6.4
52
Vac res
10,665
1.007
3.748
5.35
>100.0
28.5
>100
Total
25,365 0.9485
8.405
3.92
>100.0
9.8
>100
98
D.S.J. Jones and S.A. Treese