Page 339 - Petroleum and Gas Field Processing

Contactor Pt Dew

to Water 1.0000 13.56* 62.05* 497.9 9177. 27.57 1.043eþ07
Gas

H 2 O only

þ — — — 0.0001055 0.01584 1.403e 05 —
Gas TEG

Saturate Gas

to Sales 1.0000 36.19 61.71 497.9 9177. 27.57 1.014eþ07
Water

Feed Recy 62.05 3.649 512.0 6.562eþ05 H 2 O 62.05 0.0005366

TEG To TEG 0.0000 48.89* 0.4543 XS 0.0000 13.56 0.009708 9.746e 06 36.93

Gas Out Out

Inlet Pump 0.0000 144.0 62.74* 3.649 512.0 0.4543 6.274eþ05 Gas 1.0000 13.56 62.05 497.9 9177. 27.57 1.043eþ07

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

Continued Fraction Flow Fraction Flow user.

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