System for acid gas removal
View Patent ↗A gas purification system including a hydrogen sulfide (H 2 S) absorber, a carbon dioxide (CO 2 ) absorber, a flash tank, and a H 2 S concentrator. The gas purification system may also include a gas path though the H 2 S absorber prior to the CO 2 absorber, a first solvent path sequentially through the CO 2 absorber, the H 2 S absorber, and the H 2 S concentrator, and a second solvent path sequentially through the CO 2 absorber, the flash tank, and the H 2 S concentrator, wherein the first and second solvent paths flow a common solvent.
1. A gas purification system, comprising:
a hydrogen sulfide (H 2 S) absorber;
a carbon dioxide (CO 2 ) absorber;
a flash tank;
a H 2 S concentrator;
a gas path though the H 2 S absorber upstream of the CO 2 absorber;
a first solvent path sequentially and directly through the CO 2 absorber, the H 2 S absorber, and the H 2 S concentrator; and
a second solvent path sequentially and directly through the CO 2 absorber, the flash tank, and the H 2 S concentrator, wherein the first and second solvent paths flow a common solvent.
2. The gas purification system of claim 1 , comprising a controller configured to adjust an amount of the common solvent flowing through the first solvent path and the second solvent path.
3. The gas purification system of claim 2 , wherein the controller is configured to receive measurement signals relating to an amount of H 2 S in a sweet syngas stream exiting the CO 2 absorber.
4. The gas purification system of claim 3 , wherein the controller is configured to adjust a ratio of the common solvent flowing through the first solvent path and the second solvent path based on the received measurement signals.
5. The gas purification system of claim 1 , wherein a syngas in the gas path interacts with the common solvent in the first solvent path in the H 2 S absorber to transfer H 2 S from the syngas to the common solvent.
6. The gas purification system of claim 5 , wherein the syngas in the gas path interacts with the common solvent in the first solvent path in the CO 2 absorber to transfer CO 2 from the syngas to the common solvent.
7. The gas purification system of claim 1 , wherein the flash tank is configured to generate a change in pressure to strip at least a portion of CO 2 from the common solvent in the second solvent path.
8. The gas purification system of claim 1 , wherein the H 2 S concentrator is configured to strip at least a portion of CO 2 from the common solvent to increase a concentration of H 2 S in the common solvent.
9. The gas purification system of claim 1 , wherein the second solvent path extends sequentially through the H 2 S concentrator and a solvent stripping column configured to remove H 2 S from the common solvent and to generate an acid gas stream.
10. A gas purification system, comprising:
a hydrogen sulfide (H 2 S) absorber configured to remove H 2 S from a raw gas to produce a sweet gas and an H 2 S rich fluid;
a solvent recovery unit configured to generate an acid gas stream from the H 2 S rich fluid; and
a carbon dioxide (CO 2 ) recovery unit configured to remove CO 2 from the sweet gas to produce a CO 2 capture gas, wherein the H 2 S absorber and the CO 2 recovery unit utilize a common amine solvent to remove the H 2 S from the raw gas and the CO 2 from the sweet gas, wherein the solvent recovery unit is configured to receive the common amine solvent from each of the H 2 S absorber and the CO 2 recovery unit, wherein the solvent recovery unit is configured to separate CO 2 from the common amine solvent to generate a CO 2 stream and to transmit the CO 2 stream to a CO 2 compression unit, wherein the CO 2 compression unit is configured to combine the CO 2 stream from the solvent recovery unit with the CO 2 removed from the sweet gas to produce the CO 2 capture gas.
11. The gas purification system of claim 10 , wherein the sweet gas comprises sweet syngas that includes at most approximately 25 parts per million H 2 S.
12. The gas purification system of claim 10 , wherein the CO 2 capture gas includes at most approximately 2000 parts per million H 2 S.
13. A gas purification system, comprising:
a hydrogen sulfide (H 2 S) concentrator column configured to be pressurized to a first pressure level, comprising:
a first solvent inlet configured to receive a first solvent that is rich in carbon dioxide (CO 2 ) and lean in H 2 S;
a second solvent inlet configured to receive a second solvent that is rich in H2S and rich in CO 2 ;
packing material configured to facilitate mass transfer between vapor and liquid phases of the first and second solvents;
a solvent outlet configured to transfer a mixture of the first and second solvents out of the H 2 S concentrator column;
a first gas inlet configured to receive a stripping gas rich in CO 2 ; and
a first gas outlet configured to exhaust the stripping gas rich in CO 2 .
14. The gas purification system of claim 13 , comprising a flash tank configured to flash the mixed solvent to separate CO 2 from the mixed solvent.
15. The gas purification system of claim 13 , comprising a reboiler configured to heat the mixture of the first and second solvents above a temperature wherein a vapor pressure of dissolved components in the mixture of the first and second solvents exceeds the first pressure.
16. The gas purification system of claim 15 , wherein the reboiler comprises a second gas inlet configured to receive a stripping gas lean in CO 2 and a second gas outlet configured to exhaust the stripping gas rich in CO 2 to the gas inlet of the H 2 S concentrator, wherein the stripping gas lean in CO 2 is configured to strip the CO 2 from the mixture of the first and second solvents to generate the stripping gas rich in CO 2 .