Page 128 - Petroleum Production Engineering, A Computer-Assisted Approach

Guo, Boyun / Computer Assited Petroleum Production Engg 0750682701_chap10 Final Proof page 123 4.1.2007 8:26pm Compositor Name: SJoearun

SEPARATION SYSTEMS 10/123
Table 10.4 Settling Volumes of Standard Vertical Low-Pressure Separators (125 psi working pressure)
V L (bbl)
Size (D H) Oil/Gas separators Oil/Gas/Water separators
00 0
24 5 0.65 1.10
00 1 0
24 7 ⁄ 2 1.01 1.82
00 0
30 10 2.06 3.75
00 0
36 5 1.61 2.63
00 1 0
36 7 ⁄ 2 2.43 4.26
00 0
36 10 3.04 5.48
00 0
48 10 5.67 10.06
00 0
48 15 7.86 14.44
00 0
60 10 9.23 16.08
00 0
60 15 12.65 12.93
00 0
60 20 15.51 18.64
Table 10.5 Settling Volumes of Standard Horizontal High-Pressure Separators (230–2,000 psi working pressure)
V L (bbl)
Size (D L) 1 ⁄ 2 Full 1 ⁄ 3 Full 1 ⁄ 4 Full
3 00
12 ⁄ 4 5 0 0.38 0.22 0.15
3 00 1 0
12 ⁄ 4 7 ⁄ 2 0.55 0.32 0.21
3 00
12 ⁄ 4 10 0 0.72 0.42 0.28
00 0
16 5 0.61 0.35 0.24
00 1 0
16 7 ⁄ 2 0.88 0.50 0.34
00 0
16 10 1.14 0.66 0.44
00 0
20 5 0.98 0.55 0.38
00 1 0
20 7 ⁄ 2 1.39 0.79 0.54
00 0
20 10 1.80 1.03 0.70
00 0
24 5 1.45 0.83 0.55
00 1 0
24 7 ⁄ 2 2.04 1.18 0.78
00 0
24 10 2.63 1.52 1.01
00 0
24 15 3.81 2.21 1.47
00 0
30 5 2.43 1.39 0.91
00 1 0
30 7 ⁄ 2 3.40 1.96 1.29
00 0
30 10 4.37 2.52 1.67
00 0
30 15 6.30 3.65 2.42
00 1
36 7 ⁄ 2 4.99 2.87 1.90
00 0
36 10 6.38 3.68 2.45
00 0
36 15 9.17 5.30 3.54
00 0
36 20 11.96 6.92 4.63
00 1 0
42 7 ⁄ 2 6.93 3.98 2.61
00 0
42 10 8.83 5.09 3.35
00 0
42 15 12.62 7.30 4.83
00 0
42 20 16.41 9.51 6.32
00 1 0
48 7 ⁄ 2 9.28 5.32 3.51
00 0
48 10 11.77 6.77 4.49
00 0
48 15 16.74 9.67 6.43
00 0
48 20 21.71 12.57 8.38
00 1 0
54 7 ⁄ 2 12.02 6.87 4.49
00 0
54 10 15.17 8.71 5.73
00 0
54 15 12.49 12.40 8.20
00 0
54 20 27.81 16.08 10.68
00 1 0
60 7 ⁄ 2 15.05 8.60 5.66
00 0
60 10 18.93 10.86 7.17
00 0
60 15 26.68 15.38 10.21
00 0
60 20 34.44 19.90 13.24
Table 10.6 Settling Volumes of Standard Horizontal Low-Pressure Separators (125 psi working pressure)
V L (bbl)
Size (D L) 1 ⁄ 2 Full 1 ⁄ 3 Full 1 ⁄ 4 Full
00 0
24 5 1.55 0.89 0.59
00 1 0
24 7 ⁄ 2 2.22 1.28 0.86
00 0
24 10 2.89 1.67 1.12
(Continued )