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US 4,065,278 AGranted
Process for manufacturing liquefied methane
AssigneeAir Products and Chemicals, Inc.
InventorsCharles L. Newton, Lee S. Gaumer
Life of this patent
Estimating the term…
Abstract
A process for producing liquefied natural gas from a high pressure hydrocarbon feedstock is shown. In this process, the feedstock is isentropically expanded and distilled at a pressure lower than the critical pressure to form an overhead rich in methane and a bottom fraction. The methane rich overhead is compressed utilizing the energy obtained from the expansion and then the compressed overhead is liquefied in a refrigeration cycle.
Claims4
A liquefaction process for liquefying a natural gas feed stream comprising the steps of:
- a. supplying said natural gas feed stream at a pressure at or above 860 psia,
- b. cooling said feed stream in a plurality of heat exchange zones in indirect heat exchange with a refrigerant in a separate, closed loop refrigeration system,
- c. isentropically expanding said feed stream to a first pressure which is below the critical pressures of both the overhead and bottom streams found in subsequent step (d) and thereby obtaining mechanical energy,
- d. fractionating the expanded feed stream in a scrub column to form an overhead stream rich in methane and a bottom stream rich in heavy hydrocarbons,
- e. cooling and partially condensing said overhead stream in indirect heat exchange with a multi-component refrigerant in a separate, closed loop refrigeration system,
- f. phase separating said partially condensed overhead stream into a liquid fraction rich in heavy hydrocarbons and a methane-rich vapor stream,
- g. supplying said liquid fraction to said scrub column as reflux,
- h. supplying said methane-rich vapor stream at a temperature below -100.degree. F directly to a compressor, and compressing said stream to a pressure of at least 680 psia to form a high pressure methane-rich stream using the mechanical energy recovered in step (c),
- i. supplying said high pressure methane-rich stream to a heat exchange zone,
- j. cooling, liquefying and sub-cooling said high pressure methane-rich stream in said cooling zone in indirect heat exchange with said same multi-component refrigerant recited in clause (e), and
- k. withdrawing said liquefied and sub-cooled methane stream as an LNG product stream.
8 more elements
Dependencies are inferred from the claim text.