A new kinetic inhibitor blend GHI1 for natural gas hydrate was proposed
which contained polyvinlypyrrolidone and diethylene glycol monobutyl ether in the weight ratio 1:1. The inhibition of GHI1 was investigated at 4 ℃ and 8.5-9.0 MPa in a 1.072-liter reactor through temperature and pressure change during reaction
the comparative analysis on the temperature change with reaction time was conducted among without inhibitors
with polyvinlypyrrolidone
Inhibex501(50% copolymer of vinyl caprolactam and vinyl pyrrolidone in butoxyethanol)and GHI1. In addition the inhibition mechanism for GHI1 was also discussed. The results show that catastrophic growth of gas hydrate can be delayed effectively and the average induction time was 4800min when 0.5%GHI1 was added
2100 min when 0.5% Inhibex501 added
and 650min when 0.5% polyvinlypyrrolidone added. Polyvinlypyrrolidone in GHI1 can mainly prevent natural gas molecules from reaching the hydrate cage while diethylene glycol monobutyl ether can inhibit dissociated water to further combine with hydrate cage.
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references
HAMMERSCHMIDT E G. Formation of gas hydrates in natural gastransmission lines [J]. Ind Eng Chem, 1934,26(8):851-855.
LOVELL D, PAKULSKI M. Hydrate inhibition in gas wells treated with two low dosage hydrate inhibitors [C]∥Proceedings of the SPE International Symposium on Gas Technology.Alberta,Canada:SPE, 2002.
KELLAND M A. History of the development of low dosage hydrate inhibitors [J]. Energy Fuel,2006,20(3):825-847.
LEDERHOS J P, LONG J P, SUM A, et al. Effective kinetic inhibitors for natural gas hydrate[J]. Chemical Engineering Science, 1996,51(8):1221-1229.
KARAASLAN U, PARLAKTUNA M. PEO-a new hydrate inhibitor polymer [J]. Energy Fuels, 2002,16:1387-1391.
FU S B, CENEGY L M, NEFF C S. A summary of successful field application of a kinetic hydrate inhibitor [C]∥Proceedings of the SPE International Symposium. Texas,USA: SPE, 2001.
GLENAT P, PEYTAVY J L, Nick H J, et al. South-pars phases 2 and 3:the kinetic hydrate inhibitor(KHI)experience applied at field start-up [C]∥Proceedings of the SPE International Symposium. Abu Dhabi,UAE: SPE, 2004.
SWANSON T A, PETRIE M, Sifferman T R. The successful use of both kinetic hydrate and paraffin inhibitors together in a deepwater pipeline with a high water cut in the Gulf of Mexico [C]∥Proceedings of the SPE International Symposium.Texas,USA: SPE, 2005.
THIEU V, FROSTMAN L M. Use of low-dosage hydrate inhibitors in sour systems [C]∥Proceedings of the SPE International Symposium.Texas,USA: SPE,2005.
CAO Xin, ZHAO Wei, QIAO Xin, et al. Enhanced hydrate inhibition in an Alberta gas field [J]. Foreign Oilfield Engineering, 2005,21(10):14-16.
LEE J D, ENGLEZOS P. Enhancement of the perfor-
mance of gas hydrate kinetic inhibitors with polyethylene oxide [J]. Chemical Engineering Science, 2005,60(19): 5 323-5 330.
MAKOGON T Y, SLOAN E D. Mechanism of kinetic hydrate inhibitors [C]∥Proceedings of 4th International Hydrate Conference. Yokohama, Japan:Keio University, 2002:498-503.
KELLAND M A, SVARTAAS T M. A new class of kinetic hydrate inhibition [J]. Annals New York Academy of Sciences, 2000, 912: 281-293.