MethanolInjection.
xls
This spreadsheet calculates the minimum amount of required inhibotor usage.
Instructions:
1) Update input data in blue;
2) View result.
Input Data:
Gas flow rate: 10 MMscfd
Gas specific gravity (gg): 0.7 air = 1
Minimum pressure (pm): 900 psia
Inlet gas temperature (ti): 90 F
o
Hydrate temperature pm: 64 F
o
Operating temperature (to): 40 F
o
Water content at ti and pm: 48 lb/MMscf
Water content at to and pm: 9.6 lb/MMscf
Inhibitor solution density: 6.64 ppg
Inhibitor concentration (Win): 100 Wt %
Intermediate Calculations:
Water to be removed from gas (wG): 38.4 lb/MMscf
Molecular weight of inhibitor (MW)inh: 32
Hammerschmidt constant for inhibitor (KH): 2335
Depression of hydrate formation temperature (Dth): 24 F
o
Inhibitor requirement based on Hammerschmidt's method:
( MW )inh Δt h = 24.75 Wt %
W h= ×100
( MW )inh Δt h + K H
Liquid phase:
WG
I 100 = = 12.63 lb/MMscf
( 100
−
100
W out W in )
Gas phase:
lb m MeOH/MMscf
=f ( P , t ) = 1.05
WT % NeOH in Water
Inhibitor requirement: 25.99 lb/MMscf
System total:
Inhibitor requirement: 38.62 lb/MMscf
Daily injection rate: 386.18 lb/day
58.16 gal/day
Hourly injection rate: 2.42 gal/hour
Check:
WG
I 100 = = 12.63
KH 100
1+ −
( MW )inh Δt h W in