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<strong>BUITEMS</strong><br />

Quality & Excellence in Education<br />

Optimization of Energy Consumption during Natural Gas Dehydration<br />

Abdul Qadeer 1* , Adnan Aftab 2 , Imran Nazir 3<br />

1<br />

Department of Chemical Engineering, 2 Department of Petroleum and Gas Engineering,<br />

Balochistan University of Information Technology Engineering & Management Sciences<br />

Quetta, 3 Department of Chemical Engineering, Mehran University of Engineering and<br />

Technology, Jamshoro, Pakistan.<br />

Abstract<br />

The aim of this work is to design an efficient Natural gas dehydration plant (using TEG as<br />

desiccant) in both terms i.e., optimized desiccants flow rate as well as optimized energy<br />

requirements. For this purpose the Natural Gas Plant of Hassan Gas Field, Shikarpur was<br />

selected as case model and the basic design study was carried out for the said plant. Natural<br />

gas is one of the important fossil fuels, used after treatment. Treatment includes removal of acid<br />

gases and dehydration. The major methods of dehydration are Direct Cooling, Absorption and<br />

Adsorption. The present work is the study of efficient design for Dehydration using absorption<br />

column by Triethylene Glycol (TEG) as desiccant. Efficiency of the Natural Gas Dehydration<br />

Column can be measured through optimized flow rates of desiccant or optimized energy<br />

requirements.<br />

Keywords:<br />

Energy Consumption, Natural Gas, Optimal Energy<br />

INTRODUCTION<br />

Pakistan is one of Natural gas dependent<br />

economies of the world. Pakistan has<br />

27.89527 TCFT proven reservoirs of gas. This<br />

include 34.78 MMCF of associated reservoirs<br />

(Pakistan Energy Yearbook, 2010). During the<br />

financial year 2009-10 Pakistan produced<br />

1482846 MMCFT (Pakistan Statistical Year<br />

Book, 2011).<br />

The pressure and temperature of natural gas<br />

are reduced, when the gas is produced from<br />

the reservior during flow from subsurface to<br />

wellhead; hence the gas yields liquid water<br />

condensate. Due to presence of water vapors<br />

in gas may cause gas hydrates in sale gas<br />

transmission lines which could stop gas<br />

transportation or supply (Donald and Robert,<br />

1990; Boyun and AIi 2005, Vincente et al,<br />

1992). Natural gas some time may contain<br />

H 2 S, which itself is a poisoning gas (Gas<br />

Processors Suppliers Association, 1987). It<br />

is necessary to remove H 2 S gas (gas<br />

sweetening) prior to the dehydration of NG<br />

because it may corrode transportation and<br />

processing facilities, which may create many<br />

health, safety and environment issues<br />

(Meyers, 2003).<br />

Natural gas dehydration may be achieved<br />

by four techniques i.e. direct cooling,<br />

compression followed by cooling,<br />

absorption and adsorption. In Absorber the<br />

hydrates are removed by hygroscopic liquid,<br />

i.e. ethylene glycol (EG), diethylene glycol<br />

(DEG), triethylene glycol (TEG), and<br />

tetraethylene glycol (T 4 EG) (Saeid et al.,<br />

2006; Lurance, 1978). Pipeline specification<br />

for water content in NG is 7lb m /MMSCF<br />

(Donald and Robert, 1990).<br />

TEG flow rate in absorption column is<br />

dependent on water content in the NG,<br />

commonly flow rate of 2 to 6 gallon of TEG/<br />

lb m of water with concentration of 99.0% to<br />

99.9% is used (Landreau et al., 1999; Kohl,<br />

and Riesenfeld, 1985).<br />

Process Description<br />

Sweet gas / wet gas delivered to the bottom<br />

of gas absorber tower and lean TEG is<br />

showered from top of the tower. Both gas<br />

and TEG solution counter affect each other<br />

during this phenomena.<br />

Glycol achieves solubility with water phase<br />

7

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