Hydrate Formation in Gas-Dominant Systems Using a Single-Pass Flowloop

A 130 ft single-pass, gas-dominant flowloop has been constructed to study hydrate formation in an annular flow regime by exposing warm process fluids to a cold pipe wall. Hydrate was formed in six experiments from a natural gas mixture, with 6–18 °F subcooling from hydrate equilibrium. At lower subcooling values a stenosis-type hydrate film growth model without adjustable parameters was used to estimate the resulting pressure drop and yielded an average deviation of 15.8 psi from the experimental value. The accuracy of this model decreases appreciably with increasing subcooling, suggesting the occurrence of a transition after which the pressure drop becomes dominated by additional hydrate phenomena such as particle deposition or wall sloughing. For experiments with 18 °F subcooling, the pressure drop signal contained periodic peak-and-trough behavior and the primary hydrate restriction was observed to migrate downstream at a rate of 3 ft/min over the course of the experiment. Average hydrate growth rates ...

[1]  P. Rasmussen,et al.  A mass transport limited model for the growth of methane and ethane gas hydrates , 1994 .

[2]  E. Dendy Sloan,et al.  Methane hydrate formation and an inward growing shell model in water-in-oil dispersions , 2009 .

[3]  David T Wu,et al.  Jamming of particles in a two-dimensional fluid-driven flow. , 2012, Physical review. E, Statistical, nonlinear, and soft matter physics.

[4]  Christian Jallut,et al.  Modelling of frost growth and densification , 1997 .

[5]  Zachary M Aman,et al.  Interfacial mechanisms governing cyclopentane clathrate hydrate adhesion/cohesion. , 2011, Physical chemistry chemical physics : PCCP.

[6]  E. D. Sloan,et al.  Influence of model oil with surfactants and amphiphilic polymers on cyclopentane hydrate adhesion forces , 2010 .

[7]  Carolyn A. Koh,et al.  MACROSCOPIC INVESTIGATION OF HYDRATE FILM GROWTH AT THE HYDROCARBON/WATER INTERFACE , 2007 .

[8]  Carolyn A. Koh,et al.  Measuring hydrate/ice deposition in a flow loop from dissolved water in live liquid condensate , 2009 .

[9]  E. D. Sloan,et al.  Adhesion force between cyclopentane hydrates and solid surface materials. , 2010, Journal of colloid and interface science.

[10]  Dvora Barnea,et al.  A unified model for predicting flow-pattern transitions for the whole range of pipe inclinations , 1987 .

[11]  Michael W. Eaton,et al.  Formation of Hydrate Slurries in a Once-Through Operation , 2012 .

[12]  James P. Brill,et al.  Empirical equations to predict flow patterns in two-phase inclined flow , 1985 .

[13]  A. I. Majeed,et al.  Industrial Experience in Evaluation of Hydrate Formation, Inhibition, and Dissociation in Pipeline Design and Operation , 1994 .

[14]  P. Bishnoi,et al.  Kinetics of ethane hydrate formation , 1985 .

[15]  Carolyn A. Koh,et al.  Predicting Hydrate-Plug Formation in a Subsea Tieback , 2009 .

[16]  E. D. Sloan,et al.  Droplet size scaling of water-in-oil emulsions under turbulent flow. , 2012, Langmuir : the ACS journal of surfaces and colloids.

[17]  E. D. Sloan,et al.  Gas Hydrate Deposition on a Cold Surface in Water-Saturated Gas Systems , 2013 .

[18]  E. D. Sloan,et al.  Hydrate plug prevention by anti-agglomeration , 2001 .