최소 단어 이상 선택하여야 합니다.
최대 10 단어까지만 선택 가능합니다.
다음과 같은 기능을 한번의 로그인으로 사용 할 수 있습니다.
NTIS 바로가기다음과 같은 기능을 한번의 로그인으로 사용 할 수 있습니다.
DataON 바로가기다음과 같은 기능을 한번의 로그인으로 사용 할 수 있습니다.
Edison 바로가기다음과 같은 기능을 한번의 로그인으로 사용 할 수 있습니다.
Kafe 바로가기국가/구분 | United States(US) Patent 등록 |
---|---|
국제특허분류(IPC7판) |
|
출원번호 | US-0332272 (2014-07-15) |
등록번호 | US-8894858 (2014-11-25) |
우선권정보 | AU-2005904552 (2005-08-22) |
발명자 / 주소 |
|
출원인 / 주소 |
|
인용정보 | 피인용 횟수 : 0 인용 특허 : 472 |
A method of filtering a feed liquid in a membrane filtration assembly is provided comprising introducing feed liquid to be treated into a filtration chamber of a membrane filtration system including a membrane module having one or more permeable hollow membranes, the module being located in the filt
A method of filtering a feed liquid in a membrane filtration assembly is provided comprising introducing feed liquid to be treated into a filtration chamber of a membrane filtration system including a membrane module having one or more permeable hollow membranes, the module being located in the filtration chamber, and the filtration chamber having an open upper end located above an upper header of the membrane module and a closed lower end, and feed tank surrounding the filtration chamber. The feed tank may be configured to provide the feed liquid through the open upper end of the filtration chamber, and the feed liquid may be applied to the surface of the membranes within the membrane module and withdrawn from the lumens of the membranes as filtrate.
1. A method of treating a feed liquid, the method comprising: introducing the feed liquid to be treated into a filtration chamber of a membrane filtration system including: a membrane module having one or more permeable hollow membranes extending between an upper header and a lower header of the mem
1. A method of treating a feed liquid, the method comprising: introducing the feed liquid to be treated into a filtration chamber of a membrane filtration system including: a membrane module having one or more permeable hollow membranes extending between an upper header and a lower header of the membrane module, the membrane module being located in the filtration chamber, the filtration chamber having an open upper end located above the upper header of the membrane module and a closed lower end, anda feed tank surrounding the filtration chamber and configured to provide the feed liquid through the open upper end of the filtration chamber;applying the feed liquid to surfaces of the one or more membranes within the membrane module;producing a pressure differential across membrane walls of the one or more membranes;filtering the feed liquid through the membrane walls into lumens of the one or more membranes as filtrate; andwithdrawing the filtrate from the lumens of the one or more membranes. 2. The method of claim 1, further comprising providing feed liquid into the filtration chamber by raising the level of the feed liquid within the feed tank to a level above the open upper end of the filtration chamber. 3. The method of claim 1, further comprising flowing gas bubbles past the surfaces of the one or more membranes to aerate the membranes within the membrane module. 4. The method of claim 3, further comprising preventing liquid flow from the filtration chamber during aeration of the one or more membranes. 5. The method of claim 3, further comprising lowering a level of the feed liquid within the feed tank to below a level below the open upper end of the filtration chamber before aerating the one or more membranes. 6. The method of claim 1, further comprising flowing feed liquid past the surfaces of the one or more membranes to backwash the membranes within the membrane module. 7. The method of claim 6, further comprising preventing liquid flow from the filtration chamber during the backwashing of the one or more membranes. 8. The method of claim 6, further comprising lowering the level of the feed liquid within the feed tank to a level below the open upper end of the filtration chamber before backwashing the one or more membranes. 9. The method of claim 6, further comprising flowing the feed liquid out of the membrane module through at least one opening in at least one of the upper and lower headers. 10. The method of claim 6, further comprising raising a level of the feed liquid within the feed tank to a level above the open upper end of the filtration chamber to cause the feed liquid to flow into the filtration chamber before and/or during the backwashing of the one or more membranes. 11. The method of claim 1, further comprising performing a filtrate liquid backwash operation including: suspending filtering the feed liquid through the membrane walls;flowing filtrate into the lumens and through the membrane walls to remove an accumulation of solids from the one or more membranes and form a backwash liquid containing removed accumulated solids; andremoving the backwash liquid containing the removed accumulated solids from the filtration chamber. 12. The method of claim 11, further comprising: lowering a level of the feed liquid within the feed tank to a level below the open upper end of the filtration chamber before performing a backwashing operation on the one or more membranes; andarranging a rate of flow of filtrate backwash liquid into the filtrate chamber and a rate of removal of filtrate backwash liquid from the filtration chamber such that no filtrate backwash liquid flows from the filtration chamber into the feed tank. 13. The method of claim 1, further comprising removing liquid from the filtration chamber following at least one of aerating the one or more membranes and backwashing the one or more membranes. 14. A method of filtering a feed liquid, the method comprising: introducing the feed liquid into a filtration chamber of a membrane filtration system including: a membrane module having one or more permeable hollow membranes extending between an upper header and a lower header of the membrane module, the membrane module being located in the filtration chamber, the filtration chamber having an open upper end located above the upper header of the membrane module and a closed lower end and a feed tank surrounding the filtration chamber and configured to provide the feed liquid through the open upper end of the filtration chamber;allowing a gas to flow into and out of the filtration chamber through a valve at the upper open end of the filtration chamber;providing the feed liquid to the filtration chamber such that the valve at the upper open end in the filtration chamber closes and prevents liquid flow out of the filtration chamber;applying the feed liquid to surfaces of the one or more membranes within the membrane module;pressurizing the filtration chamber and producing a pressure differential across walls of the one or more membranes by continuing to provide the feed liquid to the filtration chamber;filtering the feed liquid through walls of the one or more membranes into lumens of the membranes as filtrate; andwithdrawing the filtrate from the membrane lumens of the one or more membranes. 15. The method of claim 14, further comprising: opening the valve to depressurize the filtration chamber; andflowing gas bubbles past the surfaces of the membranes to aerate the one or more membranes within the membrane module. 16. The method of claim 14, further comprising performing a feed liquid backwash operation including: opening the valve to depressurize the filtration chamber; andflowing the feed liquid past the surfaces of the one or more membranes to backwash the one or more membranes within the membrane module. 17. The method of claim 16, further comprising: opening the valve before a feed liquid backwashing operation begins by lowering a level of the feed liquid within the feed tank to a level below the open upper end of the filtration chamber; andpreventing liquid flow from the filtration chamber into the feed tank during the feed liquid backwashing operation. 18. The method of claim 14, further comprising performing a feed liquid backwash operation including: opening the valve of the filtration chamber to depressurize the filtration chamber and cause the feed liquid to flow into the filtration chamber lowering a level of the feed liquid within the feed tank while maintaining the level of the feed liquid above the open upper end of the filtration chamber; andflowing the feed liquid within the filtration chamber past the surfaces of the one or more membranes to backwash the one or more membranes within the membrane module. 19. The method of to claim 18, further comprising flowing the feed liquid out of the membrane module through at least one opening in at least one of the upper and lower headers. 20. The method of claim 14, further comprising performing a filtrate liquid backwash operation including: suspending filtering the feed liquid through the walls of the one or more membranes;flowing filtrate into the lumens of the membranes and through the walls of the membranes to remove an accumulation of solids from the one or more membranes and form a backwash liquid containing removed accumulated solids; andremoving the backwash liquid containing the removed accumulated solids from the filtration chamber. 21. The method of claim 20, further comprising: lowering the level of the feed liquid within the feed tank before the filtrate liquid backwash operation to open the valve and depressurize the filtration chamber; andarranging a rate of flow of filtrate backwash liquid into the filtration chamber and a rate of removal of filtrate backwash liquid from the filtration chamber such that no filtrate liquid flows from the filtration chamber into the feed tank. 22. The method of claim 14, further comprising removing liquid from the filtration chamber following at least one of an aeration operation and a backwash operation.
Copyright KISTI. All Rights Reserved.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.