Cryogenic purification of biogas with pre-separation and external solidification of carbon dioxide
AssigneeL'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude
InventorJorge Ernesto TOVAR RAMOS
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Abstract
A combined plant for cryogenic separation and liquefaction of methane and carbon dioxide in a biogas stream, including a mixing means, a compressor, a first exchanger, a distillation column, a second exchanger, a separating means, an expanding means, and a separator vessel. Wherein, the mixing means is configured such that the recycle gas is the overhead vapour stream, and the first exchanger and the expanding means are combined.
Claims20
A combined facility for cryogenic separation and liquefaction of methane and carbon dioxide in a biogas stream, comprising:
- a mixing means for mixing a biogas stream with a recycle gas stream, thereby producing a mixed biogas stream,
- a compressor for compressing the mixed biogas stream to a pressure suitable for distillation, thereby producing a compressed stream,
- a first exchanger for cooling the compressed stream, thereby producing a cooled stream,
- a first separator vessel for receiving the cooled stream and for recovering an overhead vapour stream and a CO2-enriched liquid stream,
- a cooling means for cooling the overhead vapour stream, thereby producing a cooled overhead vapor stream,
- a cryogenic separation unit supplied with the cooled overhead vapour stream and producing a methane stream at the top of the column and a CO2-enriched liquid stream at the bottom of the column,
- a second exchanger for liquefying the methane stream produced at the top of the column, thereby producing a liquefied methane stream,
- a separation means for separating the liquefied methane stream into two portions:
- a “reflux” portion and a “product” portion,
- an expanding means for expanding and heating the CO2-enriched liquid stream, thereby producing an expanded CO2 enriched stream, and for recovering the cold from the CO2-enriched liquid stream, and
- a second separator vessel for receiving the expanded CO2-enriched stream from the expanding means and for recovering an overhead vapour stream and liquid CO2 stream,
- wherein
- the mixing means is configured such that the recycle gas stream corresponds to the overhead vapour stream recovered at the outlet of the second separator vessel,
- the first exchanger and the expanding means are combined, and
- the cryogenic separation unit comprising:
- a distillation column comprising a cold section at the top of the column and a hot section at the bottom of the column,
- a means for physically separating the cold section and the hot section,
- at least two containers external to the distillation column, for placing in contact a liquid from the cold section and a vapour rising from the hot section and for trapping all solid CO2, and
- a device for regenerating the at least two external containers, comprising a means for extracting a fluid from the distillation column which is configured to liquefy the solid CO2, a means for introducing the fluid into the at least two external containers in regeneration thereby bringing about the melting of the solid CO2 and a means for reintroducing the resulting liquid CO2-vapour stream into the distillation column.
The process according to claim 10, wherein step e) is performed by cooling the methane stream produced by means of a refrigerant fluid.
Dependencies are inferred from the claim text.