B. Asadizeydabadi a,*, M. Haghshenas b , S. Roshani c,
M. Moshfeghian d
a Shell Global Solutions International B.V., Shell Development Iran B.V., Tehran – Iran
b Chemical and Process Engineering Department, Namvaran Management and Engineering, Tehran – Iran
c Process Engineering Department, Petrochemical Industries Design & Engineering Co., PIDEC, Shiraz – Iran
d John M Campbell & Company, Norman, Oklahoma USA
Abstract
A concise and accurate methodology has been developed using well known software packages to predict the type and amount of inhibitor required during sudden depressurization of a system to prevent hydrate formation. The outlined procedure exhibits the P-T history of the system and hence the hydrate formation temperature profile. A practical example of using such procedure clearly indicates the ease and accuracy of designing a hydrate inhibition package for any units in the gas, oil and petrochemical industries. © 2006 Hydrocarbon Processing®
