Numerical Simulation of an Industrial Absorber for Dehydration of Natural Gas Using Triethylene Glycol

Table 2

Outlet conditions [20].

Components	Output streams
	Gas stream		Glycol stream
	Weight %	Mol %	Weight %	Mol %
TeG	—	—	95.36	71.127
H2O	0.01	0.011	4.04	28.873
Gas	99.99	99.989	—	—
Total	100.00	100.00	100.00	100.00
Temperature °C	51.3		51