IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0546713
(2004-02-16)
|
등록번호 |
US-7438746
(2008-10-21)
|
우선권정보 |
JP-2003-047647(2003-02-25) |
국제출원번호 |
PCT/JP04/001673
(2004-02-16)
|
§371/§102 date |
20050824
(20050824)
|
국제공개번호 |
WO04/076030
(2004-09-10)
|
발명자
/ 주소 |
- Sumida,Toshihiko
- Sasano,Hiroaki
- Miyake,Masanori
|
출원인 / 주소 |
- Sumitomo Seika Chemicals, Co., Ltd.
|
대리인 / 주소 |
Hamre, Schumann, Mueller & Larson, P.C.
|
인용정보 |
피인용 횟수 :
0 인용 특허 :
4 |
초록
▼
The invention provides an off-gas feeding method that supplies the off-gas discharged from a plurality of adsorption towers (A, B, C) to an off-gas consumption unit (1), when performing a pressure swing adsorption process of repeating a cycle including a plurality of steps, to enrich and separate th
The invention provides an off-gas feeding method that supplies the off-gas discharged from a plurality of adsorption towers (A, B, C) to an off-gas consumption unit (1), when performing a pressure swing adsorption process of repeating a cycle including a plurality of steps, to enrich and separate the target gas out of a gas mixture in the adsorption towers (A, B, C) loaded with an adsorbent. The method allows at least one of the plurality of adsorption towers (A, B, C) to discharge the off-gas, in all the steps included in the cycle, so as to continue to supply the off-gas to the off-gas consumption unit (1) without interruption.
대표청구항
▼
The invention claimed is: 1. An off-gas feeding method for supplying off-gas discharged from a plurality of adsorption towers to an off-gas consumption unit, while performing a pressure swing adsorption process of repeating a cycle including a plurality of steps, to enrich and separate target gas o
The invention claimed is: 1. An off-gas feeding method for supplying off-gas discharged from a plurality of adsorption towers to an off-gas consumption unit, while performing a pressure swing adsorption process of repeating a cycle including a plurality of steps, to enrich and separate target gas out of a gas mixture in the adsorption towers loaded with an adsorbent, comprising: causing at least one of the adsorption towers to discharge the off-gas, in all the steps included in the cycle, so as to continue to supply the off-gas to the off-gas consumption unit without interruption; wherein each of the adsorption towers repeats the cycle which includes: an adsorption step of adsorbing an unnecessary gas component in the gas mixture with the adsorbent so as to discharge a product gas containing a higher concentration of the target gas, a first depressurizing step of reducing the pressure in the adsorption tower to a first intermediate pressure, a second depressurizing step of reducing the pressure in the adsorption tower to a second intermediate pressure, a desorption step of desorbing and discharging the unnecessary gas component from the adsorbent, a scavenging step of introducing scavenging gas into the adsorption tower so as to discharge residual gas in the tower, and a pressurizing step of increasing the pressure in the adsorption tower; and wherein the residual gas discharged through a product gas outlet of the adsorption tower performing the second depressurizing step is introduced to another adsorption tower performing the pressurizing step, and the off-gas is supplied to the off-gas consumption unit through a gas mixture inlet of the adsorption tower performing the second depressurizing step. 2. The method according to claim 1, further comprising controlling a flow rate of the off-gas supplied to the off-gas consumption unit. 3. The method according to claim 2, wherein the step of controlling the flow rate of the off-gas supplied to the off-gas consumption unit includes adjusting an opening extent of a flow control valve located in a gas flow path connecting the respective adsorption towers to the off-gas consumption unit. 4. The method according to claim 1, wherein the adsorption towers supply the off-gas to the off-gas consumption unit during the second depressurizing step, the desorption step and the scavenging step. 5. The method according to claim 4, further comprising controlling a flow rate of the off-gas supplied to the off-gas consumption unit by a flow control valve located in a gas flow path connecting the adsorption towers to the off-gas consumption unit, wherein an opening extent of the flow control valve is set to be largest in the scavenging step and smallest in the second depressurizing step while gradually increasing in the desorption step. 6. An off-gas feeding method for supplying off-gas discharged from a plurality of adsorption towers to an off-gas consumption unit, while performing a pressure swing adsorption process of repeating a cycle including a plurality of steps, to enrich and separate target gas out of a gas mixture in the adsorption towers loaded with an adsorbent, comprising: causing at least one of the adsorption towers to discharge the off-gas, in all the steps included in the cycle, so as to continue to supply the off-gas to the off-gas consumption unit without interruption; wherein each of the adsorption towers repeats the cycle which includes: an adsorption step of adsorbing an unnecessary gas component in the gas mixture with the adsorbent so as to discharge a product gas containing a higher concentration of the target gas, a first depressurizing step of reducing the pressure in the adsorption tower to a first intermediate pressure, a second depressurizing step of reducing the pressure in the adsorption tower to a second intermediate pressure, a desorption step of desorbing and discharging the unnecessary gas component from the adsorbent, a scavenging step of introducing scavenging gas into the adsorption tower so as to discharge residual gas in the tower, a first pressurizing step of increasing the pressure in the adsorption tower, a waiting step of closing both of the gas mixture inlet and the product gas outlet of the adsorption tower, and a second pressurizing step of further increasing the pressure in the adsorption tower; wherein the residual gas discharged through a product gas outlet of the adsorption tower performing the second depressurizing step is introduced to another adsorption tower performing the first pressurizing step, and the off-gas is supplied to the off-gas consumption unit through a gas mixture inlet of the adsorption tower performing the second depressurizing step. 7. The method according to claim 1, further comprising utilizing the off-gas consumption unit as a combustion unit of a reformer that produces the gas mixture. 8. The method according to claim 1, wherein the target gas is hydrogen gas, and the gas mixture contains hydrogen gas and a flammable gas component other than hydrogen gas. 9. The method according to claim 6, further comprising utilizing the off-gas consumption unit as a combustion unit of a reformer that produces the gas mixture. 10. The method according to claim 6, wherein the target gas is hydrogen gas, and the gas mixture contains hydrogen gas and a flammable gas component other than hydrogen gas.
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