ENGINEERED THERMOSTABLE CARBONIC ANHYDRASE ENZYMES
Disclosed herein are compositions and methods for making and using improved carbonic anhydrases for novel, sustainable, and low energy CO 2 waste gas scrubbing technologies that are also transformational carbon capture technologies. Embodiments of methods, systems and compositions disclosed herein include, but are not limited to, non-aqueous solvents, advanced membranes, sorbents, and cryogenic systems that significantly reduce the cost of CO 2 capture from coal and natural gas-fired power plants and industrial facilities. Methods disclosed herein reduce the energy and cost required for CO 2 separation and can be applied for both pre-combustion and post-combustion CO 2 capture.
1 . A non-naturally occurring carbonic anhydrase comprising at least one mutation that results in the substitution of at least one cysteine for at least one amino acid in a naturally occurring carbonic anhydrase; and wherein the non-naturally occurring carbonic anhydrase has increased activity at a temperature of greater than about 60 degrees Celsius when compared to the naturally occurring carbonic anhydrase.
2 . The non-naturally occurring carbonic anhydrase of claim 1 wherein the increased activity is for more than about 30 minutes, 1 hour, 2 hours, 3 hours, 4 hours, 5 hours, 6 hours, 24 hours, 44 hours, 48 hours, and 92 hours.
3 . The non-naturally occurring carbonic anhydrase of claim 1 wherein the increased activity is at a temperature greater than 65, 70, 75, 80, 85 or 90 degrees Celsius.
4 . The non-naturally occurring carbonic anhydrase of claim 1 wherein a nucleotide sequence encoding the non-naturally occurring carbonic anhydrase comprises a sequence that is greater than 70% identical to a sequence selected from the group consisting of SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 22, SEQ ID NO: 24 and SEQ ID NO: 26.
5 . The non-naturally occurring carbonic anhydrase of claim 1 comprising an amino acid sequence that is greater than 70% identical to a sequence selected from the group consisting of SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 21, SEQ ID NO: 23 and SEQ ID NO: 25.
6 . A method for CO 2 separation and CO 2 capture comprising the step of reacting CO 2 with a non-naturally occurring carbonic anhydrase comprising at least one mutation that results in the substitution of at least one cysteine for at least one amino acid in a naturally occurring carbonic anhydrase; and wherein the non-naturally occurring carbonic anhydrase has increased activity at a temperature of greater than about 60 degrees Celsius when compared to the naturally occurring carbonic anhydrase.
7 . The method of claim 6 wherein the step of reacting CO 2 with non-naturally occurring carbonic anhydrase is for more than about 30 minutes, 1 hour, 2 hours, 3 hours, 4 hours, 5 hours, 6 hours, 24 hours, 44 hours, 48 hours, and 92 hours.
8 . The method of claim 6 wherein the step of reacting CO 2 with the non-naturally occurring carbonic anhydrase is at a temperature greater than 65, 70, 75, 80, 85 or 90 degrees Celsius.
9 . The method of claim 6 wherein the non-naturally occurring carbonic anhydrase comprises a nucleotide sequence that is greater than 70% identical to a sequence selected from the group consisting of SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 22, SEQ ID NO: 24 and SEQ ID NO: 26.
10 . The method of claim 6 wherein the non-naturally occurring carbonic anhydrase comprises an amino acid sequence that is greater than 70% identical to a sequence selected from the group consisting of SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 21, SEQ ID NO: 23 and SEQ ID NO: 25.
11 . A system for CO 2 separation and CO 2 capture comprising s non-naturally occurring carbonic anhydrase comprising at least one mutation that results in the substitution of at least one cysteine for at least one amino acid in a naturally occurring carbonic anhydrase; and wherein the non-naturally occurring carbonic anhydrase has increased activity at a temperature of greater than about 60 degrees Celsius when compared to the naturally occurring carbonic anhydrase; and wherein the system further comprises a support wherein the with the non-naturally occurring carbonic anhydrase is immobilized to the support; and wherein the non-naturally occurring carbonic anhydrase is contacted with CO 2 .
12 . The system of claim 11 wherein the non-naturally occurring carbonic anhydrase has increased activity for more than about 30 minutes, 1 hour, 2 hours, 3 hours, 4 hours, 5 hours, 6 hours, 24 hours, 44 hours, 48 hours, and 92 hours.
13 . The system of claim 11 wherein the non-naturally occurring carbonic anhydrase reacts with CO 2 at a temperature greater than 65, 70, 75, 80, 85 or 90 degrees Celsius.
14 . The system of claim 11 wherein the CO 2 to be separated and captured results from the combustion of fossil fuels or biomass.
15 . The system of claim 11 further comprising a carbon capture unit wherein the carbon capture unit comprises an immobilized biocatalyst comprising an amino acid sequence that is greater than 70% identical to a sequence selected from the group consisting of SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 21, SEQ ID NO: 23 and SEQ ID NO: 25.