Abstract: The invention relates a novel hybrid carbonic anhydrase catalyst with the potential to contribute significantly to meeting targeted reductions in greenhouse gas emissions. In a preferred embodiment of the present invention at least a portion of a cellulose binding domain (CBD) of a protein is fused to another protein, carbonic anhydrase, (CA) to create a new multifunctional protein which can bind tightly to cellulose while maintaining its native catalytic ability to process CO2. The resulting CA-CBD hybrid polypeptide can be immobilized to a cellulose support and used to cost-effectively capture CO2 from gas streams and other CO2-rich environs.

Abstract: The invention relates a novel hybrid carbonic anhydrase catalyst with the potential to contribute significantly to meeting targeted reductions in greenhouse gas emissions. In a preferred embodiment of the present invention at least a portion of a cellulose binding domain (CBD) of a protein is fused to another protein, carbonic anhydrase, (CA) to create a new multi-functional protein which can bind tightly to cellulose while maintaining its native catalytic ability to process CO2. The resulting CA-CBD hybrid polypeptide can be immobilized to a cellulose support and used to cost-effectively capture CO2 from gas streams and other CO2-rich environs.

Abstract: Two methods are provide for the separation of carbon dioxide from the flue gases. The first method utilizes a phase-separating moiety dissolved in an aqueous solution of a basic moiety to capture carbon dioxide. The second method utilizes a phase-separating moiety as a suspended solid in an aqueous solution of a basic moiety to capture carbon dioxide. The first method takes advantage of the surface-independent nature of the CO2 absorption reactions in a homogeneous aqueous system. The second method also provides permanent sequestration of the carbon dioxide. Both methods incorporate the kinetic rate enhancements of amine-based scrubbing while eliminating the need to heat the entire amine solution (80% water) in order to regenerate and release CO2. Both methods also take advantage of the low-regeneration temperatures of CO2-bearing mineral systems such as Na2CO3/NaHCO3 and K2CO3/KHCO3.