Invention Grant
US09321011B2 Ethanol/water vapor permeation membrane separation process with heat and energy recovery via temperature and flow control
有权
乙醇/水蒸汽渗透膜分离过程,通过温度和流量控制进行热能和能量回收
- Patent Title: Ethanol/water vapor permeation membrane separation process with heat and energy recovery via temperature and flow control
- Patent Title (中): 乙醇/水蒸汽渗透膜分离过程,通过温度和流量控制进行热能和能量回收
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Application No.: US13809445Application Date: 2011-07-29
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Publication No.: US09321011B2Publication Date: 2016-04-26
- Inventor: Takafumi Kiuchi , Ryohta Hidaka , Yoichi Ishibashi , Yasuki Kansha , Atsushi Tsutsumi
- Applicant: Takafumi Kiuchi , Ryohta Hidaka , Yoichi Ishibashi , Yasuki Kansha , Atsushi Tsutsumi
- Applicant Address: JP Tokyo JP Tokyo
- Assignee: NIPPON STEEL & SUMKIN ENGINEERING CO., LTD.,THE UNIVERSITY OF TOKYO
- Current Assignee: NIPPON STEEL & SUMKIN ENGINEERING CO., LTD.,THE UNIVERSITY OF TOKYO
- Current Assignee Address: JP Tokyo JP Tokyo
- Agency: Wenderoth, Lind & Ponack, L.L.P.
- Priority: JP2010-176499 20100805
- International Application: PCT/JP2011/004306 WO 20110729
- International Announcement: WO2012/017628 WO 20120209
- Main IPC: B01D61/36
- IPC: B01D61/36

Abstract:
[Problem] To provide a membrane separation apparatus and a membrane separation method capable of reducing energy consumption,[Solution] A membrane separation apparatus (10) includes: a membrane separator (20) supplied with a fluid (X) containing a component (A) and a component (B) and separating the fluid (X) into a fluid (Y) having a higher concentration of the component (A) than the fluid (X) and a fluid (Z) having a lower concentration of the component (A) than the fluid (X) by using a separation membrane; a first compressor (21) adiabatically compressing the fluid (Y); a first heat exchanger (11) to which the fluid (Y) adiabatically compressed by the first compressor (21) is introduced as a heat source; and a second heat exchanger (12) to which the fluid (Z) is introduced as a heat source. The fluid (X) is divided and conveyed by first and second supply lines (31, 32), the divided fluids (X) are heated by the first and second heat exchangers (11, 12), respectively, then merged and supplied to the membrane separator (20).
Public/Granted literature
- US20130153498A1 MEMBRANE SEPARATION APPARATUS AND MEMBRANE SEPARATION METHOD Public/Granted day:2013-06-20
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