Patent ID: 11946691
Assignee: L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE
Field: Chemical engineering (Chemistry)
Classification: CPC F  C  Y | IPC F

Claim 0:
1. 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, comprising a distillation column, the distillation column comprising a top and a bottom, and producing a methane stream at the top of the distillation column and a CO2-enriched liquid stream at the bottom of the distillation column,
a second exchanger for liquefying the methane stream produced at the top of the distillation 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 the CO-enriched liquid stream, thereby producing an expanded CO2-enriched liquid stream, and the first heat exchanger configured to heat the expanded CO2-enriched liquid stream for recovering cold from the expanded CO2-enriched liquid stream, thereby producing an expanded CO2 enriched stream
a second separator vessel for receiving the expanded CO2-enriched stream from the expanding means and the first heat exchanger for producing 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,
and
the cryogenic separation unit comprising:
the distillation column comprising a cold section at the top of the distillation column and a hot section at the bottom of the distillation column,
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.