FIELD: chemical or physical processes.
SUBSTANCE: described is a method of liquefying a hydrocarbon-saturated fraction (A), in which a hydrocarbon-rich fraction is cooled by at least one circuit of a mixed refrigerant (E1, E2, E3). Refrigerating agent circulating in the mixed refrigerant circuit is compressed on at least two stages (C1, C2). Compressed refrigerant is divided into higher boiling point and lower boiling fraction of refrigerant. Higher-boiling fraction of refrigerant serves for preliminary cooling (E1), and lower-boiling fraction of refrigerant serves for liquefaction (E2) of fraction saturated with hydrocarbons. Liquefied fraction saturated with hydrocarbons (B) is overcooled in separate heat exchanger by means of a mixture of refrigerants from separate circuit of the expander, and a mixture of refrigerants from said contour of the dilator, in addition to N2 and CH4 components, contains at least one component of group O2, Ar, Kr, Xe, C2H4 and C2H6, wherein the fraction of components N2 and CH4 is at least 80 mol %.
EFFECT: technical result is reduction of capital costs.
13 cl, 3 dwg
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Authors
Dates
2020-07-07—Published
2016-09-20—Filed