IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0854075
(2010-08-10)
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등록번호 |
US-8632627
(2014-01-21)
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발명자
/ 주소 |
- Frydman, Arnaldo
- Ayala, Raul Eduardo
- Potnis, Shailesh Vijay
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출원인 / 주소 |
|
대리인 / 주소 |
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인용정보 |
피인용 횟수 :
1 인용 특허 :
25 |
초록
▼
A gas dehydrator system, including, a desiccant transport wheel configured to rotate a solid desiccant from a first dehydration section to a first regeneration section, a first gas path extending through the first dehydration section, wherein the solid desiccant is configured to collect moisture fro
A gas dehydrator system, including, a desiccant transport wheel configured to rotate a solid desiccant from a first dehydration section to a first regeneration section, a first gas path extending through the first dehydration section, wherein the solid desiccant is configured to collect moisture from a first gas in the first gas path, and a second gas path extending through the first regeneration section, wherein the solid desiccant is configured to release the moisture into a second gas in the second gas path to regenerate the solid desiccant.
대표청구항
▼
1. A system, comprising: a carbon dioxide dehydration system, comprising: a desiccant transporter configured to transport a desiccant chamber with solid desiccant from a first dehydration section to a first regeneration section;a CO2 path extending through the first dehydration section, wherein the
1. A system, comprising: a carbon dioxide dehydration system, comprising: a desiccant transporter configured to transport a desiccant chamber with solid desiccant from a first dehydration section to a first regeneration section;a CO2 path extending through the first dehydration section, wherein the solid desiccant is configured to collect moisture from CO2 in the CO2 path;a gas path extending through the first regeneration section, wherein the solid desiccant is configured to release the moisture into a gas in the gas path to regenerate the solid desiccant, and the CO2 path and the gas path are independent from one another; anda controller configured to use instructions to depressurize the desiccant chamber in the first regeneration section with the gas at a first temperature and a first pressure, wherein the controller is configured to execute instructions to repressurize the desiccant chamber in the first regeneration section with the gas at a second temperature and a second pressure, the controller is configured to execute instructions sweeping the gas from the desiccant chamber in the first regeneration section with CO2, the first temperature is greater than the second temperature, and the first pressure is less than the second pressure. 2. The system of claim 1, wherein the desiccant chamber is a first desiccant chamber containing a first volume of the solid desiccant, and the desiccant transporter is configured to move the first desiccant chamber from the first dehydration section to the first regeneration section. 3. The system of claim 2, wherein the desiccant transporter comprises a wheel having the first desiccant chamber, and the wheel is configured to rotate the first desiccant chamber from the first dehydration section to the first regeneration section. 4. The system of claim 3, wherein the carbon dioxide dehydration system comprises a second dehydration section and a second regeneration section, the wheel comprises second, third, and fourth desiccant chambers, and the wheel is configured to rotate the first, second, third, and fourth desiccant chambers sequentially among the first dehydration section, the first regeneration section, the second dehydration section, and a second regeneration section. 5. The system of claim 2, wherein the desiccant transporter comprises a second desiccant chamber containing a second volume of the solid desiccant, and the desiccant transporter is configured to move the first and second desiccant chambers sequentially among the first dehydration section and the first regeneration section. 6. The system of claim 1, wherein the first regeneration section is configured to heat the solid desiccant with the gas in the gas path. 7. The system of claim 6, comprising a heat exchanger configured to transfer heat from a steam path to the gas path. 8. The system of claim 6, wherein the gas path comprises a nitrogen path through the first regeneration section. 9. The system of claim 1, wherein the controller is configured to control the carbon dioxide dehydration system based on feedback indicative of a moisture level. 10. The system of claim 9, wherein the controller is configured to control a CO2 flow rate through the CO2 path, a gas flow rate through the gas path, a heat transfer to the gas path, a movement of the solid desiccant, or a combination thereof. 11. The system of claim 10, wherein the controller is configured to control a rotation of a wheel to control the movement of the solid desiccant, and the wheel comprises the first dehydration section and the first regeneration section of the desiccant transporter. 12. The system of claim 9, wherein the controller is configured to control the carbon dioxide dehydration system to maintain the CO2 below a threshold moisture level. 13. The system of claim 1, wherein the desiccant transporter comprises a wheel having the first dehydration section and the first regeneration section, and a controller is configured to iteratively rotate the wheel, stop the wheel to enable the first dehydration section to receive the CO2 along the CO2 path and to enable the first regeneration section to receive the gas along the gas path, and subsequently rotate the wheel after a time delay. 14. The system of claim 1, comprising a carbon capture system configured to capture the CO2 from a source, wherein the carbon dioxide dehydration system is configured to receive the CO2 from the carbon capture system. 15. A gas dehydrator system, comprising: a desiccant transport ring configured to rotate a solid desiccant in a sealed desiccant chamber from a first dehydration section to a first regeneration section;a first gas path extending through the first dehydration section, wherein the solid desiccant is configured to collect moisture from a first gas in the first gas path;a second gas path extending through the first regeneration section, wherein the solid desiccant is configured to release the moisture into a second gas in the second gas path to regenerate the solid desiccant, and the first and second gas paths are independent from one another; anda controller configured to execute instructions to depressurize the sealed desiccant chamber in the first regeneration section with the second gas at a first temperature and a first pressure, wherein the controller is configured to execute instructions to repressurize the desiccant chamber in the first regeneration section with the second gas at a second temperature and a second pressure, the controller is configured to execute instructions sweeping the second gas from the desiccant chamber in the first regeneration section with the first gas, the first temperature is greater than the second temperature, and the first pressure is less than the second pressure. 16. The system of claim 15, wherein the first gas path comprises a carbon dioxide (CO2) path. 17. The system of claim 15, wherein the second gas path comprises a nitrogen path. 18. The system of claim 15, wherein the desiccant transport ring comprises a plurality of sealed desiccant chambers each defining a separate volume of the solid desiccant, and the desiccant transport ring is configured to rotate the plurality of sealed desiccant chambers from the first dehydration section to the first regeneration section. 19. The system of claim 18, wherein the system further comprises a second dehydration section and a second regeneration section, and the desiccant transport ring is configured to rotate the plurality of sealed desiccant chambers sequentially among the first dehydration section, the first regeneration section, the second dehydration section, and a second regeneration section. 20. The system of claim 15, wherein the first regeneration section is configured to depressurize a sealed desiccant chamber with the second gas at a first temperature and a first pressure, the first regeneration section is configured to repressurize the sealed desiccant chamber with the second gas at a second temperature and a second pressure, the first regeneration section is configured on the second gas from the sealed desiccant chamber with the first gas downstream of the gas dehydrator, the first temperature is greater than the second temperature, and the first pressure is less than the second pressure. 21. The system of claim 15, wherein the controller is configured to control the gas dehydration system based on feedback indicative of a moisture level to maintain the first gas below a threshold moisture level. 22. The system of claim 21, wherein the first gas is carbon dioxide (CO2) and the second gas is nitrogen. 23. A gas dehydrator system, comprising: a desiccant transporter configured to rotate a solid desiccant within a sealed desiccant chamber from a first dehydration section to a first regeneration section;a first gas path extending through the first dehydration section, wherein the solid desiccant is configured to collect moisture from a first gas in the first gas path;a second gas path extending through the first regeneration section, wherein the solid desiccant is configured to release the moisture into a second gas in the second gas path to regenerate the solid desiccant, and the first and second gas paths are independent from one another; anda controller configured to execute instructions to depressurize the sealed desiccant chamber in the first regeneration section with the second gas at a first temperature and a first pressure, wherein the controller is configured to execute instructions to repressurize the desiccant chamber in the first regeneration section with the second gas at a second temperature and a second pressure, the controller is configured to execute instructions sweeping the second gas from the desiccant chamber in the first regeneration section with the first gas, the first temperature is greater than the second temperature, and the first pressure is less than the second pressure. 24. The system of claim 23, wherein the desiccant transporter comprises a ring having a plurality of sealed desiccant chambers each defining a separate volume of the solid desiccant, and the desiccant transporter is configured to rotate the plurality of desiccant chambers sequentially from the first dehydration section to the first regeneration section.
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