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公开(公告)号:BR9101408A
公开(公告)日:1991-11-26
申请号:BR9101408
申请日:1991-04-09
Applicant: STANDARD OIL CO OHIO
Inventor: VALUS RONALD JAMES , VELIKOFF ALEXANDER EVAN , ESHRAGHI REZA , DAVIS JAMES CRITSER
Abstract: A process for the selective separation of at least one component eg propylene of a gaseous feedstream comprises passing the feedstream containing the component through a separation unit (50), the separation unit (50) containing a porous membrane (53), eg in the form of a hollow fiber, the membrane (53) having a feed side and a permeate side, and a pore size of from about 10 Angstroms to about 200 Angstroms. Disposed in the pores of the porous membrane (53) is a facilitator liquid comprising a carrier eg silver nitrate dissolved in a suitable solvent. The process includes the steps of (a) dissolving the component in the facilitator liquid on the feed side of the porous membrane (53) at the feed gas/membrane interface; (b) forming a component-carrier complex; (c) diffusing the complex to the permeate side of the porous membrane (53): and (d) releasing the component from the carrier.
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2.
公开(公告)号:CA2038239A1
公开(公告)日:1991-10-10
申请号:CA2038239
申请日:1991-03-14
Applicant: STANDARD OIL CO OHIO
Inventor: VALUS RONALD J , ESHRAGHI REZA , VELIKOFF ALEXANDER E , DAVIS JAMES C
Abstract: The subject invention relates to a process for the selective separation of at least one component of a gaseous feedstream comprising passing the feedstream containing the component through a separation unit, the separation unit containing a porous membrane having a feed side and a permeate side, and a pore size of from about 10Angstroms to about 200Angstroms, and having disposed in the pores of the porous membrane a facilitator liquid comprising a carrier dissolved in a suitable solvent, including: a) dissolving the component in the facilitator liquid on the feed side of the porous membrane at the feed gas/membrane interface; b) forming a component-carrier complex; c) diffusing the complex to the permeate side of the porous membrane; and d) releasing the component from the carrier. The invention further relates to a membrane for the selective separation of at least one component of a gaseous feedstream comprising a porous membrane, having pores of from about 10Angstroms to about 200Angstroms, the pores containing a facilitator liquid having an affinity for the component to be selectively separated, the membrane being capable of operating at a transmembrane pressure of about 100psig to about 300psig. The subject invention also relates to use of the aboveidentified process and membrane for the separation of vapor phase olefins from olefin-containing feed streams.
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公开(公告)号:AT131406T
公开(公告)日:1995-12-15
申请号:AT91302766
申请日:1991-03-28
Applicant: STANDARD OIL CO OHIO
Inventor: DAVIS JAMES CRITSER , VALUS RONALD JAMES , ESHRAGHI REZA , VELIKOFF ALXANDER EVAN
Abstract: A process for the selective separation of at least one component eg propylene of a gaseous feedstream comprises passing the feedstream containing the component through a separation unit (50), the separation unit (50) containing a porous membrane (53), eg in the form of a hollow fiber, the membrane (53) having a feed side and a permeate side, and a pore size of from about 10 Angstroms to about 200 Angstroms. Disposed in the pores of the porous membrane (53) is a facilitator liquid comprising a carrier eg silver nitrate dissolved in a suitable solvent. The process includes the steps of (a) dissolving the component in the facilitator liquid on the feed side of the porous membrane (53) at the feed gas/membrane interface; (b) forming a component-carrier complex; (c) diffusing the complex to the permeate side of the porous membrane (53): and (d) releasing the component from the carrier.
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公开(公告)号:PT97289A
公开(公告)日:1992-01-31
申请号:PT9728991
申请日:1991-04-08
Applicant: STANDARD OIL CO OHIO
Inventor: VALUS RONALD JAMES , VELIKOFF ALEXANDER EVAN , ESHRAGHI REZA , DAVIS JAMES CRITSER
Abstract: A process for the selective separation of at least one component eg propylene of a gaseous feedstream comprises passing the feedstream containing the component through a separation unit (50), the separation unit (50) containing a porous membrane (53), eg in the form of a hollow fiber, the membrane (53) having a feed side and a permeate side, and a pore size of from about 10 Angstroms to about 200 Angstroms. Disposed in the pores of the porous membrane (53) is a facilitator liquid comprising a carrier eg silver nitrate dissolved in a suitable solvent. The process includes the steps of (a) dissolving the component in the facilitator liquid on the feed side of the porous membrane (53) at the feed gas/membrane interface; (b) forming a component-carrier complex; (c) diffusing the complex to the permeate side of the porous membrane (53): and (d) releasing the component from the carrier.
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5.
公开(公告)号:ZA9102193B
公开(公告)日:1992-01-29
申请号:ZA9102193
申请日:1991-03-22
Applicant: STANDARD OIL CO OHIO
Inventor: VALUS RONALD JAMES , RONALD JAMES VALUS , ESHRAGHI REZA , REZA ESHRAGHI , VELIKOFF ALEXANDER EVAN , ALEXANDER EVAN VELIKOFF , DAVIS JAMES CRITZER , JAMES CRITZER DAVIS
CPC classification number: B01D53/22 , B01D63/02 , B01D2313/22 , B01D2313/38
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公开(公告)号:DE69115329T2
公开(公告)日:1996-05-02
申请号:DE69115329
申请日:1991-03-28
Applicant: STANDARD OIL CO OHIO
Inventor: DAVIS JAMES CRITSER , VALUS RONALD JAMES , ESHRAGHI REZA , VELIKOFF ALXANDER EVAN
Abstract: A process for the selective separation of at least one component eg propylene of a gaseous feedstream comprises passing the feedstream containing the component through a separation unit (50), the separation unit (50) containing a porous membrane (53), eg in the form of a hollow fiber, the membrane (53) having a feed side and a permeate side, and a pore size of from about 10 Angstroms to about 200 Angstroms. Disposed in the pores of the porous membrane (53) is a facilitator liquid comprising a carrier eg silver nitrate dissolved in a suitable solvent. The process includes the steps of (a) dissolving the component in the facilitator liquid on the feed side of the porous membrane (53) at the feed gas/membrane interface; (b) forming a component-carrier complex; (c) diffusing the complex to the permeate side of the porous membrane (53): and (d) releasing the component from the carrier.
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公开(公告)号:DE69115329D1
公开(公告)日:1996-01-25
申请号:DE69115329
申请日:1991-03-28
Applicant: STANDARD OIL CO OHIO
Inventor: DAVIS JAMES CRITSER , VALUS RONALD JAMES , ESHRAGHI REZA , VELIKOFF ALXANDER EVAN
Abstract: A process for the selective separation of at least one component eg propylene of a gaseous feedstream comprises passing the feedstream containing the component through a separation unit (50), the separation unit (50) containing a porous membrane (53), eg in the form of a hollow fiber, the membrane (53) having a feed side and a permeate side, and a pore size of from about 10 Angstroms to about 200 Angstroms. Disposed in the pores of the porous membrane (53) is a facilitator liquid comprising a carrier eg silver nitrate dissolved in a suitable solvent. The process includes the steps of (a) dissolving the component in the facilitator liquid on the feed side of the porous membrane (53) at the feed gas/membrane interface; (b) forming a component-carrier complex; (c) diffusing the complex to the permeate side of the porous membrane (53): and (d) releasing the component from the carrier.
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8.
公开(公告)号:ZA912193B
公开(公告)日:1992-01-29
申请号:ZA912193
申请日:1991-03-22
Applicant: STANDARD OIL CO OHIO
Inventor: VALUS RONALD JAMES , RONALD JAMES VALUS , ESHRAGHI REZA , REZA ESHRAGHI , VELIKOFF ALEXANDER EVAN , ALEXANDER EVAN VELIKOFF , DAVIS JAMES CRITZER , JAMES CRITZER DAVIS
Abstract: A process for the selective separation of at least one component eg propylene of a gaseous feedstream comprises passing the feedstream containing the component through a separation unit (50), the separation unit (50) containing a porous membrane (53), eg in the form of a hollow fiber, the membrane (53) having a feed side and a permeate side, and a pore size of from about 10 Angstroms to about 200 Angstroms. Disposed in the pores of the porous membrane (53) is a facilitator liquid comprising a carrier eg silver nitrate dissolved in a suitable solvent. The process includes the steps of (a) dissolving the component in the facilitator liquid on the feed side of the porous membrane (53) at the feed gas/membrane interface; (b) forming a component-carrier complex; (c) diffusing the complex to the permeate side of the porous membrane (53): and (d) releasing the component from the carrier.
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