Chemical looping integration with a carbon dioxide gas purification unit
View Patent ↗A chemical looping system that contains an oxidizer and a reducer is in fluid communication with a gas purification unit. The gas purification unit has at least one compressor, at least one dryer; and at least one distillation purification system; where the gas purification unit is operative to separate carbon dioxide from other contaminants present in the flue gas stream; and where the gas purification unit is operative to recycle the contaminants to the chemical looping system in the form of a vent gas that provides lift for reactants in the reducer.
1. A method comprising:
discharging a flue gas stream from a chemical looping system to a gas purification unit; where the chemical looping system comprises:
an oxidizer in fluid communication with a reducer; where the oxidizer is operative to oxidize an oxygen carrier including multivalence metal oxide or a calcium sulfide to a higher valence metal oxide or to a calcium sulfate respectively; and where the reducer is operative to reduce the oxygen carrier by reducing metal oxide to a lower valence metal oxide or the calcium sulfate to calcium sulfide; where the chemical looping system generates a flue gas stream comprising carbon dioxide during the reducing of the metal oxide or the reducing of the calcium sulfate; and
compressing the flue gas stream in the gas purification unit; where the gas purification unit comprises:
at least one compressor to compress the flue gas stream,
at least one dryer to remove water from the flue gas stream compressed by the at least one compressor; and
at least one distillation purification system;
separating carbon dioxide from other contaminants present in the flue gas stream exiting the at least one dryer; and
recycling the contaminants to the reactor of the chemical looping system in the form of a vent gas to carry the oxygen carrier upward within the reducer, without removing carbon monoxide from the flue gas or the contaminants;
wherein compressing the gas stream occurs at least prior to separating the carbon dioxide from the contaminants present in the flue gas stream.
2. The method of claim 1 , further comprising distilling a portion of the vent gas in the distillation purification system.
3. The method of claim 1 , further comprising drying the flue gas stream to remove water present.
4. The method of claim 3 , further comprising splitting the flue gas stream into two streams, of which one stream is recirculated to the reducer of the chemical looping system via the distillation purification system while the other stream is directly recycled to the reducer of the chemical looping system without contacting the distillation purification system.
5. The method of claim 4 , where the stream that contacts the distillation purification system is further split into two streams—one of which comprises the contaminants and the other comprising carbon dioxide; and where the stream that comprises the carbon dioxide is further compressed in one or more compressors.
6. The method of claim 4 , further comprising contacting the stream emanating from the distillation purification system with calcium oxide to further remove carbon dioxide from the vent stream; and where the vent stream is recycled to the reducer after removal of the carbon dioxide.
7. The method of claim 3 , further comprising contacting the stream emanating from the distillation purification system with a semi-permeable membrane to further remove carbon dioxide from the vent stream; and where the vent stream is recycled to the reducer after removal of the carbon dioxide.
8. The method system of claim 1 , where the vent gas comprises methane, carbon monoxide, hydrogen, oxygen, hydrogen sulfide and sulfur dioxide.