CATEGORY: PRODUCED WATER
ACS Sustainable Chem. Eng., 2013, 1 (10), pp
1218–1224
Increasing
Gas Hydrate Formation Temperature for Desalination of High Salinity Produced
Water with Secondary Guests
Jong-Ho Cha and Yongkoo Seol *
Yongkoo.Seol@netl.doe.gov
National Energy Technology Laboratory, U.S. Department of Energy, Morgantown,
West Virginia 26507, United
Abstract
Describes a novel gas hydrate-based desalination process using water-immiscible
hydrate formers; cyclopentane (CP) and cyclohexane (CH) as secondary hydrate
guests to alleviate temperature requirements for hydrate formation. Researchers
conducted the hydrate formation reactions in an isobaric condition of 3.1 MPa
to find the upper temperature limit of CO2 hydrate formation. Simulated
produced water mixed with the hydrate formers shows an increased upper
temperature limit from −2 °C for simple CO2 hydrate to 16 and 7 °C for double
(CO2 + CP) and (CO2 + CH) hydrates, respectively. The resulting conversion rate
to double hydrate was similar to that with simple CO2 hydrate at the upper
temperature limit.
Hydrate
formation rates (Rf) for the double hydrates with cyclopentane and cyclohexane
as secondary hydrate guests are shown to be 22 and 16 times higher,
respectively, than that of the simple CO2 hydrate at the upper temperature
limit. Such mild hydrate formation temperature and fast formation kinetics
indicate increased energy efficiency of the double hydrate system for the
desalination process.
Full Text Source (Subscription or Fee): http://pubs.acs.org/doi/abs/10.1021/sc400160u
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