FIELD: process engineering.
SUBSTANCE: invention relates to chemistry. Hydrogen sulphide is removed from natural gas flow bearing methane CH4 and H2S to cool said flow in heat exchanger 13, 16, 18. At least, portion of cooled flow is fed via feed pipeline 19, 21 into cyclone expander-separator 1. Here, cooled flow is expanded in nozzle 4 to be additionally cooled to temperature and pressure below dew point of hydrogen sulphide and separated in tubular separation chamber 9 into fraction of cooled low-density fluid. Said fraction is rich in methane and hydrogen sulphide depleted. Another fraction of aforesaid cooled flow represents high-density fluid rich in hydrogen sulphide and methane-depleted. Low-density cooled fluid flow is fed in gas product pipeline 33 communicated with heat exchanger 14 to cool down natural gas flow fed into cyclone expander-separator 1. High-density cooled fluid flow is fed in fractionator 8 for additional separation.
EFFECT: higher yield.
4 dwg
Title | Year | Author | Number |
---|---|---|---|
NATURAL GAS LIQUEFACTION METHOD | 2012 |
|
RU2596764C2 |
COMPLEX METHOD FOR EXTRACTION OF GAS-CONDENSATE LIQUIDS AND LIQUEFACTION OF NATURAL GAS | 2013 |
|
RU2641778C2 |
METHOD OF SEPARATING HYDROCARBON-CONTAINING GAS MIXTURE | 2014 |
|
RU2568215C1 |
OPTIMISATION OF STRIPPER FEED CONFIGURATION FOR RICH/LEAN SOLVENT REGENERATION | 2014 |
|
RU2667285C2 |
UNITED EXTRACTION OF NATURAL GAS CONDENSATE AND MANUFACTURING OF LIQUEFIED NATURAL GAS | 2006 |
|
RU2367860C1 |
NATURAL GAS LIQUEFACTION PLANT WITH ETHYLENE-INDEPENDENT SYSTEM OF EXTRACTION OF HEAVY FRACTIONS | 2012 |
|
RU2607933C2 |
EXTRACTION OF LIQUEFIED NATURAL GAS FROM SYNTHETIC GAS USING MIXED REFRIGERANT | 2014 |
|
RU2604632C2 |
METHOD FOR REMOVAL OF VOLATILE COMPONENTS FROM NATURAL GAS | 1999 |
|
RU2224961C2 |
EXTRACTION OF HELIUM FROM NATURAL GAS | 2019 |
|
RU2743086C1 |
COMBINED SEPARATION OF HEAVY AND LIGHT COMPONENTS FROM NATURAL GAS | 2014 |
|
RU2668053C2 |
Authors
Dates
2012-09-27—Published
2008-06-27—Filed