Table 8 Example of calculation of stripper bottom composition

From: Refinery Gas Treating Processes

Temperature			249 °F
Comp	Moles/h	Mole frac	K@ 34 psia	y = xk
H₂S	57.5	0.0062	45.4	0.2815
Water	8646.6	0.9256	0.79	0.7312
MEA	637.5	0.0682	0.09	0.0057
Total	9,341.6	1.0000		1.0184

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