Staged complementary psa system for low energy fractionation of mixed fluid
US-2017136402-A1 · May 18, 2017 · US
US10071338B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10071338-B2 |
| Application number | US-201615339978-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 1, 2016 |
| Priority date | Nov 17, 2015 |
| Publication date | Sep 11, 2018 |
| Grant date | Sep 11, 2018 |
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Systems and methods for using pressure swing adsorption to separate and/or capture resulting emissions are provided. A stream of recycled exhaust gas is passed into a first swing adsorption reactor comprising a first adsorbent material which adsorbs CO 2 . An enriched N 2 stream is recovered from a forward end of the first swing adsorption reactor. The pressure in the first swing adsorption reactor is reduced. The first swing adsorption reactor is purged with a portion of the first N 2 stream recovered from the first swing adsorption reactor. The first purge output is passed to a second swing adsorption reactor comprising a second adsorbent material which adsorbs CO 2 . A second N 2 stream is recovered from the second swing adsorption reactor. The pressure in the second swing adsorption reactor is reduced. The second swing adsorption reactor is purged with a steam purge.
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The invention claimed is: 1. A method for capturing emissions comprising: passing a stream of recycled exhaust gas into a first swing adsorption reactor comprising a first adsorbent material; adsorbing CO 2 on the first adsorbent material; recovering a first N 2 stream from a forward end of the first swing adsorption reactor wherein the first N 2 stream is an enriched N 2 stream; reducing the pressure in the first swing adsorption reactor by outputting a blow down stream from at least one end of the first swing adsorption reactor; purging the first swing adsorption reactor with a portion of the first N 2 stream recovered from the first swing adsorption reactor to create a first purge output from the first swing adsorption reactor; passing the first purge output to a second swing adsorption reactor comprising a second adsorbent material; adsorbing CO 2 on the second adsorbent material; recovering a second N 2 stream from a forward end of the second swing adsorption reactor; reducing the pressure in the second swing adsorption reactor by outputting a blow down stream from at least one end of the second swing adsorption reactor; and purging the second swing adsorption reactor with a steam purge to create an output from the second swing adsorption reactor. 2. The method of claim 1 , wherein reducing the pressure in the first swing adsorption reactor comprises reducing the pressure to an intermediate pressure value lower than a pressure value of the recycled exhaust gas and higher than a pressure value of the output from the second swing adsorption. 3. The method of claim 2 , wherein the intermediate pressure value is between 3 and 12 bar. 4. The method of claim 1 , wherein at least one of the first swing adsorption reactor and the second swing adsorption reactor comprises multiple adsorbent beds. 5. The method of claim 4 , wherein adsorption of CO 2 by the multiple adsorbent beds is cycled to allow regeneration of at least one bed without completely ceasing adsorption. 6. The method of claim 1 , wherein the first adsorbent material is different from the second adsorbent material. 7. The method of claim 1 , wherein the first adsorbent material is sensitive to steam. 8. The method of claim 1 , wherein the first adsorbent material is any one of CaO, Ca(OH) 2 , CaO—La 2 O 3 , and CaMg(CO 3 ) 2 . 9. A system for capturing emissions comprising: a first swing adsorption reactor which receives a stream of recycled exhaust gas, wherein the first swing adsorption reactor comprises: a first adsorbent material which adsorbs CO 2 ; a first forward end from which a first N 2 stream is output wherein the first N 2 stream is an enriched N 2 stream; a first blow down output feed which outputs a blow down stream to reduce the pressure in the first swing adsorption reactor; a first purge input feed which receives a portion of the first N 2 stream; a first purge output feed which outputs a first purge output comprising CO 2 and N 2 ; a second swing adsorption reactor which receives the first purge output, wherein the second swing adsorption reactor comprises: a second adsorbent material which adsorbs CO 2 ; a second forward end from which a second N 2 stream is output; a second blow down output feed which outputs a blow down stream to reduce the pressure in the second swing adsorption; a second purge input feed which receives a steam purge; and a second purge output feed which outputs a second purge output comprising CO 2 and steam. 10. The system of claim 9 , wherein the first blow down output feed reduces the pressure to an intermediate pressure value lower than a pressure value of the recycled exhaust gas and higher than a pressure value of the output from the second swing adsorption. 11. The system of claim 10 , wherein the intermediate pressure value is between 3 and 12 bar. 12. The system of claim 9 , wherein at least one of the first swing adsorption reactor and the second swing adsorption reactor comprises multiple adsorbent beds. 13. The system of claim 12 , wherein adsorption of CO 2 by the multiple adsorbent beds is cycled to allow regeneration of at least one bed without completely ceasing adsorption. 14. The system of claim 9 , wherein the first adsorbent material is different from the second adsorbent material. 15. The system of claim 9 , wherein the first adsorbent material is sensitive to steam. 16. The system of claim 9 , wherein the first adsorbent material is any one of CaO, Ca(OH) 2 , CaO—La 2 O 3 , and CaMg(CO 3 ) 2 .
Depressurization · CPC title
Metal oxides · CPC title
by using a purge gas (B01D2259/4009 takes precedence) · CPC title
Pressure swing adsorption · CPC title
Nitrogen · CPC title
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