Page 337 - Petroleum and Gas Field Processing

Contactor Bttms Pump (Continued)

to 1.0000 29.44 62.05 498.5 9191. 27.59 1.021eþ07 Regen 0.0000 204.4 1.034 3.648 511.9 0.4542 6.071eþ05 to TEG 0.0000 145.1 1.027 3.649 512.0 0.4543* 6.264eþ05
Gas

H 2 O TEG TEG

þ 0.9999 29.44* 62.05 498.6 9192. 27.59 1.021eþ07 0.0362 35.51 1.793 4.270 525.6 0.4727 6.949eþ05 0.0000 15.56* 1.027 0.0004591 0.06834 6.057e 05 87.51
Gas LP MakeUp

Saturate TEG Gas

to 0.5420 277.1 62.05 0.4990* 8.989 0.009007 2.961eþ04 Rich 0.0000 30.17 62.05 4.270 525.6 0.4727 6.949eþ05 Sour 1.0000 101.7 1.014 0.6216 13.71 0.01854 2.861eþ04

11 Water
Figure

in Feed 0.0000 48.89* 62.05* 3.649* 512.0 0.4543 6.562eþ05 Gas 1.0000 31.14 62.05 497.9 9177. 27.57 1.017eþ07 Feed 0.0531 104.4* 1.103* 4.270 525.6 0.4727 6.737eþ05
Sheet TEG Dry Regen

Flow

for Gas Out L/R

Balance Inlet 1.0000 29.44* 62.05* 498.1* 9183. 27.58 1.018eþ07 Water 0.0000 29.44 62.05 0.06651 1.200 0.001203 4527. from Lean 0.0000 145.1 1.027 3.648 511.9 0.4542 6.283eþ05

Energy (C) (C) (C)

and (bar) (kgmole/h) (kg/h) (m 3 /h) (kcal/h) (bar) (kgmole/h) (kg/h) (m 3 /h) (kcal/h) (bar) (kgmole/h) (kg/h) (m 3 /h) (kcal/h)

Material Flow Flow Flow

Stream Fraction Volume Fraction Volume Fraction Volume

3 Temperature Flow Flow Flow Temperature Flow Flow Flow Temperature Flow Flow Flow Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
Table Name Vapour Pressure Molar Mass Liquid Heat Name Vapour Pressure Molar Mass Liquid Heat Name Vapour Pressure Molar Mass Liquid Heat