Pressure swing adsorption process for enhanced separation of lighter from heavier species
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B01D-053/047
B01D-053/053
출원번호
US-0153917
(2016-05-13)
등록번호
US-9579598
(2017-02-28)
발명자
/ 주소
Ritter, James A.
Ebner, Armin D.
Ho, Jason G. S.
출원인 / 주소
Apache Corporation
대리인 / 주소
Bracewell LLP
인용정보
피인용 횟수 :
0인용 특허 :
13
초록▼
A pressure swing adsorption (PSA) system and a PSA process including a PSA cycle schedule are disclosed. The PSA cycle schedule includes an unlimited number of equalization steps, no idle steps, no dead time and a minimum number of three PSA adsorbent beds assisted with two or more equalization tank
A pressure swing adsorption (PSA) system and a PSA process including a PSA cycle schedule are disclosed. The PSA cycle schedule includes an unlimited number of equalization steps, no idle steps, no dead time and a minimum number of three PSA adsorbent beds assisted with two or more equalization tanks. The PSA system, process and cycle schedule include the following sequence of cycle steps: a feed step, two or more down equalization steps either between beds or between a bed and a tank, an optional forced cocurrent depressurization step coupled with a forced intermediary light end pressurization step, a countercurrent depressurization step, a light reflux step, two or more up equalization steps between beds or between a bed and a tank, an optional forced intermediary light end pressurization step coupled with the forced cocurrent depressurization step, and a light product pressurization step.
대표청구항▼
1. A pressure swing adsorption (PSA) system comprising: as few as three PSA beds configured with N-tanks to perform a continuous feed PSA cycle schedule with an even number (N) of light end equalization steps allowing for bed-to-tank-to-bed equalization steps and no bed-to-bed equalization steps, wh
1. A pressure swing adsorption (PSA) system comprising: as few as three PSA beds configured with N-tanks to perform a continuous feed PSA cycle schedule with an even number (N) of light end equalization steps allowing for bed-to-tank-to-bed equalization steps and no bed-to-bed equalization steps, wherein N>2, wherein at all times during the process, each of the three beds are actively separating gases with no idle steps and no dead time, and wherein the system is capable of performing the process with only three PSA beds. 2. The system of claim 1, wherein the PSA cycle schedule for the three PSA beds comprises: a feed step, an even number of two or more down equalization steps between a bed and a tank, a countercurrent depressurization step, a light reflux step, an even number of two or more up equalization steps between a tank and a bed, and a light product pressurization step. 3. The system of claim 1, wherein all the N equalization steps are in sequence with no other cycle steps in between the N equalization steps. 4. The system of claim 2, wherein the PSA cycle schedule for the three PSA beds further comprises: a forced cocurrent depressurization step coupled with a forced intermediary light end pressurization step before the countercurrent depressurization step, or a forced intermediary light end pressurization step coupled with the forced cocurrent depressurization step before the light product pressurization step. 5. The system of claim 4, further comprising: a compressor or a vacuum pump for assisting the forced cocurrent depressurization and forced intermediate light end pressurization steps. 6. The system of claim 2, further comprising: a fourth bed for extending a duration of the countercurrent depressurization and light reflux steps without affecting a duration of the feed step. 7. A pressure swing adsorption (PSA) system comprising: three PSA beds configured with N-tanks to perform a continuous feed PSA cycle schedule with an odd number (N+1) of light end equalization steps and one bed-to-bed equalization step, wherein N+1≧3, and wherein at all times during the process, each of the three beds are actively separating gases with no idle steps and no dead time. 8. The system of claim 7, wherein the PSA cycle schedule for the three PSA beds comprises: a feed step, an odd number of three or more down equalization steps with one between two beds and the rest of the three or more down equalization steps between a bed and a tank, a countercurrent depressurization step, a light reflux step, an odd number of three or more up equalization steps with one between two beds and the rest of the three or more up equalization steps between a tank and a bed, and a light product pressurization step. 9. The system of claim 7, wherein the one bed-to-bed equalization step occurs directly in the middle of the N equalization steps with an equal number of equalization steps on either side of the one bed-to-bed equalization step. 10. The system of claim 8, wherein the PSA cycle schedule for the three PSA beds further comprises: a forced cocurrent depressurization step coupled with a forced intermediary light end pressurization step before the countercurrent depressurization step, or a forced intermediary light end pressurization step coupled with the forced cocurrent depressurization step before the light product pressurization step. 11. The system of claim 10, further comprising: a compressor or a vacuum pump for assisting the forced cocurrent depressurization and forced intermediate light end pressurization steps. 12. The system of claim 8, further comprising: a fourth bed for extending a duration of the countercurrent depressurization and light reflux steps without affecting a duration of the feed step. 13. A pressure swing adsorption (PSA) process comprising: providing a PSA apparatus having as few as three PSA beds and two or more equalization tanks; andequalizing a pressure of each of the three PSA beds in two or more equalization steps, wherein at all times during the process, each of the three beds are actively separating gases with no idles steps or no dead time, and wherein the apparatus is capable of performing the process with only three PSA beds. 14. The process of claim 13, further comprising: providing the three PSA beds with N-tanks to perform a continuous feed PSA cycle schedule with an even number (N) of light end equalization steps and no bed-to-bed equalization steps, wherein N≧2. 15. The process of claim 14, further comprising: a feed step, an even number of two or more down equalization steps between a bed and a tank, a countercurrent depressurization step, a light reflux step, an even number of two or more up equalization steps between a tank and a bed, and a light product pressurization step. 16. The process of claim 15, further comprising: a forced cocurrent depressurization step coupled with a forced intermediary light end pressurization step before the countercurrent depressurization step, or a forced intermediary light end pressurization step coupled with the forced cocurrent depressurization step before the light product pressurization step. 17. The process of claim 13, further comprising: providing the three PSA beds with N-tanks to perform a continuous feed PSA cycle schedule with an odd number (N+1) of light end equalization steps and one bed-to-bed equalization step, wherein N+1≧3. 18. The process of claim 17, further comprising: a feed step, an odd number of three or more down equalization steps with one between two beds and the rest of the three or more down equalization steps between a bed and a tank, a countercurrent depressurization step, a light reflux step, an odd number of three or more up equalization steps with one between two beds and the rest of the three or more up equalization steps between a tank and a bed, and a light product pressurization step. 19. The process of claim 18, further comprising: a forced cocurrent depressurization step coupled with a forced intermediary light end pressurization step before the countercurrent depressurization step, or a forced intermediary light end pressurization step coupled with the forced cocurrent depressurization step before the light product pressurization step. 20. The process of claim 15, further comprising: providing a fourth bed for extending a duration of the countercurrent depressurization and light reflux steps without affecting a duration of the feed step.
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이 특허에 인용된 특허 (13)
Reinhold ; III Herbert E. (Annapolis MD) D\Amico Joseph S. (Linthicum MD) Knaebel Kent S. (Plain City OH), Natural gas enrichment process.
Krishnamurthy Ramachandran (Cranbury NJ) Lerner Steve L. (Berkeley Heights NJ) MacLean Donald L. (Annandale NJ), PSA multicomponent separation utilizing tank equalization.
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