Method and device for vacuum pressure swing adsorption with temporary storage
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B01D-053/047
B01D-053/053
C01B-013/02
출원번호
US-0879033
(2011-10-05)
등록번호
US-8961653
(2015-02-24)
우선권정보
DE-10 2010 048 774 (2010-10-16)
국제출원번호
PCT/EP2011/004969
(2011-10-05)
§371/§102 date
20130425
(20130425)
국제공개번호
WO2012/048814
(2012-04-19)
발명자
/ 주소
Grahl, Matthias
출원인 / 주소
Linde Aktiengesellschaft
대리인 / 주소
Millen, White, Zelano & Branigan, P.C.
인용정보
피인용 횟수 :
0인용 특허 :
5
초록▼
Adsorptive decomposition of a gas mixture is performed by vacuum pressure swing adsorption. The gas mixture is condensed to the adsorption pressure by means of at least one condenser prior to being fed into the vacuum pressure swing adsorption process. Regeneration of the adsorber(s) is carried out
Adsorptive decomposition of a gas mixture is performed by vacuum pressure swing adsorption. The gas mixture is condensed to the adsorption pressure by means of at least one condenser prior to being fed into the vacuum pressure swing adsorption process. Regeneration of the adsorber(s) is carried out by means of at least one vacuum pump. The condensed gas mixture (1, 5, 6) is at least periodically and/or at least partially temporarily stored (S1) and/or fed to a consumer at those times when no gas mixture is being fed to the vacuum pressure swing adsorption process; and/or at least one of the vacuum pumps (P) that is not required for the regeneration is used at least occasionally for another application at those times when no regeneration of the adsorber or an adsorber (A, A′) is being carried out.
대표청구항▼
1. A method for the adsorptive decomposition of a gas mixture by means of a vacuum pressure swing adsorption process, wherein a gas mixture to be decomposed adsorptively is compressed to the adsorption pressure by means of at least one compressor before being delivered to the vacuum pressure swing a
1. A method for the adsorptive decomposition of a gas mixture by means of a vacuum pressure swing adsorption process, wherein a gas mixture to be decomposed adsorptively is compressed to the adsorption pressure by means of at least one compressor before being delivered to the vacuum pressure swing adsorption process, and the regeneration of adsorber or adsorbers utilized in said vacuum pressure swing adsorption process occurs by means of at least one vacuum pump, and wherein at those times at which no gas mixture is delivered to the vacuum pressure swing adsorption process, the compressed gas mixture (1, 5, 6) is at least temporarily and/or at least partially intermediately stored (S1) and/or delivered to a consumer, and/orat those times at which no regeneration of the adsorber (A, A′) or of an adsorber (A, A′) by means of the vacuum pump (V) or at least one of the vacuum pumps (V) takes place, the vacuum pump (P) or at least one of the vacuum pumps (P) not required for regeneration is employed at least temporarily for another intended use. 2. The method as claimed in claim 1, wherein said gas mixture to be decomposed adsorptively is air. 3. The method as claimed in claim 1, wherein compression of said gas mixture to be decomposed adsorptively takes place by means of a single-stage compressor unit (C). 4. The method as claimed in claim 1, wherein regeneration of the adsorber or adsorbers (A, A′) takes place by means of a single-stage vacuum pump unit (V). 5. The method as claimed in claim 1, wherein said compressed gas mixture (S1) at least temporarily and/or at least partially intermediately stored is delivered to the adsorber (A, A′) or to an adsorber (A, A′) which is in the adsorption phase. 6. The method as claimed in claim 1, wherein the vacuum pump (V) used for regenerating the adsorber or adsorbers (A, A′) is connected at least temporarily to a storage tank (S3) to be evacuated, and the storage tank (S3) to be evacuated is connected at least temporarily to the adsorber (A, A′) or to an adsorber (A, A′) which is in the desorption phase. 7. A device for carrying out a method according to claim 1, said device comprising: at least one compressor, at least one adsorber and at least one vacuum pump, whereinat least one first storage tank (S1) is provided and is connected to the compressor or to at least one of the compressors (C) in such a way that, at those times at which no gas mixture is delivered to the vacuum pressure swing adsorption process, the compressed gas mixture (1, 5, 6) is routed at least temporarily and/or at least partially into the first storage tank (S1) or at least one of the first storage tanks (S1), and/orat least one second storage tank (S3) is provided and this is connected to the vacuum pump or to at least one of the vacuum pumps (V) in such a way that, at those times at which no regeneration of the adsorber (A, A′) or of an adsorber (A, A′) by means of the or at least one of the vacuum pumps (V) takes place, the vacuum pump (P) or at least one of the vacuum pumps (P) not required for regeneration evacuates at least temporarily the second storage tank (S3) or at least one of the second storage tanks (S3). 8. The device as claimed in claim 7, wherein the compressor or compressors (C) are of a single-stage design. 9. The method as claimed in claim 1, wherein at those times at which no gas mixture is delivered to the vacuum pressure swing adsorption process, the compressed gas mixture (1, 5, 6) is at least temporarily and/or at least partially intermediately stored (S1) and/or delivered to a consumer. 10. The method as claimed in claim 1, wherein at those times at which no regeneration of the adsorber (A, A′) or of an adsorber (A, A′) by means of the vacuum pump (V) or at least one of the vacuum pumps (V) takes place, the vacuum pump (P) or at least one of the vacuum pumps (P) not required for regeneration is employed at least temporarily for another intended use. 11. The method as claimed in claim 9, wherein at those times at which no regeneration of the adsorber (A, A′) or of an adsorber (A, A′) by means of the vacuum pump (V) or at least one of the vacuum pumps (V) takes place, the vacuum pump (P) or at least one of the vacuum pumps (P) not required for regeneration is employed at least temporarily for another intended use. 12. The method as claimed in claim 9, wherein at those times at which no gas mixture is delivered to the vacuum pressure swing adsorption process, the compressed gas mixture (1, 5, 6) is at least temporarily stored (S1). 13. The method as claimed in claim 9, wherein at those times at which no gas mixture is delivered to the vacuum pressure swing adsorption process, the compressed gas mixture (1, 5, 6) is at least temporarily delivered to a consumer. 14. The method as claimed in claim 1, wherein compression of said gas mixture to be decomposed adsorptively takes place by means of a multistage compressor unit (C). 15. The method as claimed in claim 1, wherein regeneration of the adsorber or adsorbers (A, A′) takes place by means of a multistage vacuum pump unit (V). 16. The method as claimed in claim 1, wherein said compressed gas mixture (S1) at least temporarily and/or at least partially intermediately stored is delivered to the adsorber (A, A′) or to an adsorber (A, A′) which is in the adsorption phase, delivery taking place when an adjustable pressure value in the storage device (S1) used for intermediate storage is overshot. 17. The method as claimed in claim 1, wherein the vacuum pump (V) used for regenerating the adsorber or adsorbers (A, A′) is connected at least temporarily to a storage tank (S3) to be evacuated, and the storage tank (S3) to be evacuated is connected at least temporarily to the adsorber (A, A′) or to an adsorber (A, A′) which is in the desorption phase, this connection taking place when an adjustable pressure value in the storage tank (S3) is undershot. 18. The device as claimed in claim 7, wherein the compressor or compressors (C) are of a multistage design. 19. The device as claimed in claim 7, wherein the vacuum pumps (V) are of a single-stage design. 20. The device as claimed in claim 7, wherein the vacuum pumps (V) are of a multistage design.
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