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Title: Cryogenic separation of gaseous mixtures

Patent ·
OSTI ID:5362813

This patent describes a cryogenic separation process for recovering C{sub 2} hydrocarbons from a hydrocarbon feedstream comprising methane, ethene and ethane. It comprises introducing the hydrocarbon feedstream into a dephlegmation zone at cryogenic temperatures; dephlegmating the hydrocarbon feedstream into a primary methane-rich gas stream and a primary liquid condensate stream rich in C{sub 2} + hydrocarbon components and containing a minor amount of methane; passing the primary liquid condensate stream to a moderately low cryogenic temperature primary demethanizer unit and separating the primary liquid condensate stream into a C{sub 2} + liquid bottoms stream and intermediate methane-rich overhead vapor stream; and further separating the intermediate methane-rich overhead vapor stream from the moderately low cryogenic temperature primary demethanizer unit in an ultra-low temperature final demethanizer unit operating below about 175 psia to recover a first liquid ethene-rich hydrocarbon product stream and a final demethanizer ultra-low temperature vapor stream; whereby total energy requirements for refrigeration to separate the C{sub 2} + hydrocarbon from the C{sub 1} and lighter components are low.

Assignee:
Stone and Webster Engineering Corp., Boston, MA (United States)
Patent Number(s):
US 5035732; A
Application Number:
PPN: US 7-462395
OSTI ID:
5362813
Resource Relation:
Patent File Date: 4 Jan 1990
Country of Publication:
United States
Language:
English