Method to recover and process methane and condensates from flare gas systems
Assignees1304338 Alberta Ltd., 1304342 Alberta Ltd.
InventorsJose Lourenco, MacKenzie Millar
Life of this patent
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Abstract
A method to recover and process hydrocarbons from a gas flare system to produce natural gas liquids (NGL), cold compressed natural gas (CCNG), compressed natural gas (CNG) and liquid natural gas (LNG). The method process provides the energy required to recover and process the hydrocarbon gas stream through compression and expansion of the various streams.
Claims16
A method to recover and process associated gas from an oil-producing well to produce natural gas liquids (NGLs), cold compressed natural gas (CCNG), compressed natural gas (CNG) and liquid natural gas (LNG), the method comprising the steps of:
- capturing associated gas produced from a wellhead, the associated gas comprising at least methane, water, and natural gas liquids (NGLs) in vapor form;
- compressing the associated gas to produce a pressurized natural gas stream;
- passing the pressurized natural gas stream through a dewatering unit to remove at least a portion of the water;
- cooling the pressurized natural gas stream to produce a cooled rich natural gas stream in which at least a portion of the NGLs are condensed;
- separating the cooled rich natural gas stream into a gaseous natural gas stream and an NGL stream;
- processing the gaseous natural gas stream to produce a fuel gas stream, a compressed natural gas (CNG) stream, a cold compressed natural gas (CCNG) stream, and a liquid natural gas (LNG) stream, wherein:
- producing the LNG stream comprises passing a portion of the gaseous natural gas stream through a carbon dioxide stripping unit to produce a stripped feed stream;
- the fuel gas stream comprises a fuel gas portion of the gaseous natural gas stream that is conditioned to a pressure and temperature suitable for use by a power plant;
- the CNG stream comprises a CNG portion of the gaseous natural gas stream that is compressed to a pressure greater than the fuel gas stream;
- and
- the LNG stream and the CCNG stream are produced by:
- producing a partially condensed stripped gas stream by expanding the stripped feed stream from the carbon dioxide stripping unit to achieve cryogenic temperatures, and passing the partially condensed stripped gas stream through a separator to obtain the LNG stream and a cold natural gas stream;
- and
- compressing the cold natural gas stream to produce the CCNG stream.
Dependencies are inferred from the claim text.