4
owable max Nat Gas velocity in pipelines, as a function of operating press Assumed temperature oC 50 50 50 50 50 50 Operating pressure Barg 75 40 15 10 5 2 Natural gas MW kg/kgmo 20.43 20.43 20.43 20.43 20.43 20.43 0.84 0.92 0.98 0.98 0.99 0.99 kg/m3 68.6 33.9 12.5 8.6 4.6 2.3 Allowable max gas velocity a Erosional velocity, API 14E m/s 14.7 20.9 34.6 41.7 56.7 80.3 b m/s 29.5 41.9 69.1 83.4 113.4 160.7 a' Allowable max gas velocity m/s 7.4 10.5 17.3 20.8 28.4 40.2 b' Allowable max gas velocity m/s 14.7 20.9 34.6 41.7 56.7 80.3 c Per Norsok standard P-001 m/s 28.4 38.4 59.2 60.0 60.0 60.0 NOTES b non corrosion service without solid particles, C=200 lb/s/ft2 per API 14E (1 a' considered as 50% of erosional velocity per a b' considered as 50% of erosional velocity per b Gas compressibility factor (assumed) Gas density (at operating cond As above, no corrosion/solid part 0 10 20 30 40 50 60 70 80 90 0 10 20 30 40 50 60 70 80 90 100 Series a' Series b' Series c ( Pressure, barg Allowable max velocity, m/s

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Guide gas Velocity

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Page 1: NGvel

Allowable max Nat Gas velocity in pipelines, as a function of operating pressure (50 oC)Assumed temperature oC 50 50 50 50 50 50 50Operating pressure Barg 75 40 15 10 5 2 0.2Natural gas MW kg/kgmol 20.43 20.43 20.43 20.43 20.43 20.43 20.43

0.84 0.92 0.98 0.98 0.99 0.99 1.00kg/m3 68.6 33.9 12.5 8.6 4.6 2.3 0.9

Allowable max gas velocitya Erosional velocity, API 14E (1984) m/s 14.7 20.9 34.6 41.7 56.7 80.3 126.9b m/s 29.5 41.9 69.1 83.4 113.4 160.7 253.7a' Allowable max gas velocity per a m/s 7.4 10.5 17.3 20.8 28.4 40.2 63.4b' Allowable max gas velocity per b m/s 14.7 20.9 34.6 41.7 56.7 80.3 126.9c Per Norsok standard P-001 m/s 28.4 38.4 59.2 60.0 60.0 60.0 60.0

NOTESb non corrosion service without solid particles, C=200 lb/s/ft2 per API 14E (1984).a' considered as 50% of erosional velocity per ab' considered as 50% of erosional velocity per b

Gas compressibility factor (assumed)

Gas density (at operating conditions)

As above, no corrosion/solid particles

0 10 20 30 40 50 60 70 80 900

10

20

30

40

50

60

70

80

90

100

Series a'

Series b'

Series c (Norsok)

Pressure, barg

All

ow

able

max

vel

oci

ty,

m/s

D5
so that density will be 68.61 kg/m3, as given.
E5
Assumed same as that for CH4 at 15 oC.
F5
Assumed same as that for CH4 at 15 oC.
G5
Assumed same as that for CH4 at 15 oC.
H5
Assumed same as that for CH4 at 15 oC.
I5
Assumed same as that for CH4 at 15 oC.
J5
Assumed same as that for CH4 at 15 oC.
Page 2: NGvel

Allowable max CH4 (g) velocity in pipelines, as a function of operating pressure (15 oC)Assumed temperature oC 15 15 15 15 15 15 15Operating pressure Barg 80 40 15 10 5 2 0.2

kg/kgmol 16 16 16 16 16 16 16Gas compressibility factor 0.85 0.92 0.98 0.98 0.99 0.99 1.00

kg/m3 63.4 29.8 10.9 7.5 4.1 2.0 0.8Allowable max gas velocity

a Erosional velocity, API 14E (1984) m/s 15.3 22.3 36.9 44.5 60.5 85.7 135.4b m/s 30.6 44.7 73.8 89.0 121.0 171.5 270.7a' Allowable max gas velocity per a m/s 7.7 11.2 18.4 22.2 30.3 42.9 67.7b' Allowable max gas velocity per b m/s 15.3 22.3 36.9 44.5 60.5 85.7 135.4c Per Norsok standard P-001 m/s 29.4 40.7 60.0 60.0 60.0 60.0 60.0

NOTESb non corrosion service without solid particles, C=200 lb/s/ft2 per API 14E (1984).a' considered as 50% of erosional velocity per ab' considered as 50% of erosional velocity per b

Natural gas MW (assumed 100% CH4)

Gas density (at operating conditions)

As above, no corrosion/solid particles

0 10 20 30 40 50 60 70 80 900

10

20

30

40

50

60

70

80

90

100

Series a'

Series b'

Series c (Norsok)

Pressure, barg

All

ow

able

max

vel

oci

ty,

m/s