GB1290001A

GB1290001A – – Google Patents

GB1290001A – – Google Patents

Info

Publication number
GB1290001A

GB1290001A

GB1290001DA
GB1290001A
GB 1290001 A
GB1290001 A
GB 1290001A

GB 1290001D A
GB1290001D A
GB 1290001DA
GB 1290001 A
GB1290001 A
GB 1290001A
Authority
GB
United Kingdom
Prior art keywords
compartments
liquid
vapour
tubes
feed
Prior art date
1968-12-24
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)

Expired

Application number

Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1968-12-24
Filing date
1969-12-01
Publication date
1972-09-20

1969-12-01
Application filed
filed
Critical

1972-09-20
Publication of GB1290001A
publication
Critical
patent/GB1290001A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

Classifications

A—HUMAN NECESSITIES

A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES

A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF

A23F5/00—Coffee; Coffee substitutes; Preparations thereof

A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee

A23F5/28—Drying or concentrating coffee extract

A23F5/285—Drying or concentrating coffee extract by evaporation, e.g. drying in thin layers, foam drying

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01D—SEPARATION

B01D63/00—Apparatus in general for separation processes using semi-permeable membranes

B01D63/08—Flat membrane modules

B01D63/082—Flat membrane modules comprising a stack of flat membranes

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01D—SEPARATION

B01D63/00—Apparatus in general for separation processes using semi-permeable membranes

B01D63/08—Flat membrane modules

B01D63/082—Flat membrane modules comprising a stack of flat membranes

B01D63/0822—Plate-and-frame devices

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01D—SEPARATION

B01D2313/00—Details relating to membrane modules or apparatus

B01D2313/08—Flow guidance means within the module or the apparatus

B01D2313/086—Meandering flow path over the membrane

B—PERFORMING OPERATIONS; TRANSPORTING

B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL

B01D—SEPARATION

B01D2313/00—Details relating to membrane modules or apparatus

B01D2313/14—Specific spacers

Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC

Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y10S159/00—Concentrating evaporators

Y10S159/27—Micropores

Abstract

1290001 Evaporators; concentration of solutions IONICS Inc 1 Dec 1969 [24 Dec 1968] 58575/69 Headings BIB and B1X A volatile component is removed from a liquid mixture by diffusion of vapour therefrom through selective membranes 10 in an apparatus comprising a pack of feed compartments 8, heating compartments 7 and vapour compartments 9 formed by frame members and heat transfer sheets 11, the arrangement being such that two liquid flow compartments are disposed on either side of each vapour compartment, and conduits formed by aligned holes in the membranes, sheets and the gaskets of the frame members supply the feed stream 60, the heating medium (steam or hot water) 62 to their respective compartments while a third conduit 61 serves for applying partial vacuum to the vapour compartments by pumps 26. The liquid enters and leaves the compartments 8 via channels 50..56. The liquid leaves each compartment 8 in a direction away from the immediately adjacent selective membrane 10. In the apparatus shown, feed liquid and heating medium are pumped through tubes 20 and 21 respectively into vacuum spacers 14. These streams then flow in parallel through their respective compartments 8 and 7. The concentrated liquid is withdrawn from the apparatus through tubes 23; and heating medium is withdrawn through tubes 24. In a modified apparatus (Fig. 1, not shown), the feed liquid flows in series through the compartments 8. It is stated that, instead of applying partial vacuum to compartments 9, sweep gas may be passed through them. The apparatus may be used for the concentration of aqueous extracts of coffee, and fruit and vegetable juices. For such aqueous liquors, the membrane-material should be strongly hydrophilic to allow permeation of water and impede the evaporation of organic constituents. The membrane may be made of an organic polymer or a cellulose ester.

GB1290001D
1968-12-24
1969-12-01

Expired

GB1290001A
(en)

Applications Claiming Priority (2)

Application Number
Priority Date
Filing Date
Title

US78663468A

1968-12-24
1968-12-24

US3066170A

1970-04-22
1970-04-22

Publications (1)

Publication Number
Publication Date

GB1290001A
true

GB1290001A
(en)

1972-09-20

Family
ID=26706303
Family Applications (3)

Application Number
Title
Priority Date
Filing Date

GB1290002D
Expired

GB1290002A
(en)

1968-12-24
1969-12-01

GB1290001D
Expired

GB1290001A
(en)

1968-12-24
1969-12-01

GB1290003D
Expired

GB1290003A
(en)

1968-12-24
1969-12-01

Family Applications Before (1)

Application Number
Title
Priority Date
Filing Date

GB1290002D
Expired

GB1290002A
(en)

1968-12-24
1969-12-01

Family Applications After (1)

Application Number
Title
Priority Date
Filing Date

GB1290003D
Expired

GB1290003A
(en)

1968-12-24
1969-12-01

Country Status (5)

Country
Link

US
(2)

US3520803A
(en)

DE
(1)

DE1964635A1
(en)

FR
(1)

FR2026998A1
(en)

GB
(3)

GB1290002A
(en)

NL
(1)

NL6918953A
(en)

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Priority date
Publication date
Assignee
Title

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1970-07-02
1972-08-15
Gen Electric
Blood component exchange device

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1971-02-05
1972-05-09
Pactide Corp
Compact multistage distillation apparatus having stacked microporous membranes and impermeable films

FR2141417B2
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1971-02-25
1973-06-29
Rhone Poulenc Sa

FR2127155A5
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*

1971-02-25
1972-10-13
Rhone Poulenc Sa
Plate-type ultra-filter – with semi-permeable membranes

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1971-02-25
1981-06-02
Rhone Poulenc, S.A.
Separation apparatus

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1971-06-09
1973-05-29
Gulf Research Development Co
Membrane gas extractor

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1971-07-06
1974-09-10
Cutter Lab
Membrane diffusion apparatus

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1971-08-27
1974-03-19
Gen Electric
Microporous/non-porous composite membranes

BE788610A
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1971-09-09
1973-03-08
Rhone Poulenc Sa

MEMBRANE SEPARATOR APPARATUS USED IN GAS PERMEATION AND PERVAPORATION

GB1292421A
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*

1972-02-02
1972-10-11
Sam Ellison Smith
Improvements in or relating to a method for fabricating a seamless plastic surface and a template therefor

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1972-04-27
1974-10-01
Gen Electric
Integral blood heat and component exchange device and two flow path membrane blood gas exchanger

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1973-02-08
1978-06-06
Josef Hoeltzenbein
Plate dialyzer

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1974-04-22
1977-04-05
Baxter Laboratories, Inc.
Staged membrane diffusion device and membrane support

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1975-07-28
1978-05-16
General Electric Company
Apparatus for the separation of hydrogen sulfide from gas mixture including carbon dioxide

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*

1975-10-31
1976-11-23
The United States Of America As Represented By The Secretary Of The Interior
Thin cell electromembrane separator

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1978-01-26
1981-09-24
Sartorius GmbH, 3400 Göttingen

Device for mass transfer between fluids with the interposition of a membrane

AT352757B
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1978-02-24
1979-10-10
Edwin Hiesinger

FILTRATION DEVICE

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1979-02-01
1981-03-17
C. R. Bard, Inc.
Membrane oxygenator

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1979-02-14
1981-05-05
International Power Technology, Inc.
Method and apparatus for distillation

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1980-01-22
1982-07-20
A.T. Ramot Plastics Ltd.
Membrane separation cell

EP0054020A1
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1980-03-19
1982-06-23
Gambro AG
A device for the diffusion of substances between two fluids via semipermeable membranes

US4422936A
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*

1981-03-17
1983-12-27
Gambro Ag
Device for the diffusion of substances between two fluids via semipermeable membranes

DE3131642C2
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1981-08-11
1986-01-16
Emil 4802 Halle Schneck

Heat exchanger for mash

DE3304956A1
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*

1983-02-12
1984-08-16
Gkss – Forschungszentrum Geesthacht Gmbh, 2054 Geesthacht

DEVICE FOR SEPARATING SOLUTIONS BY PERVAPORATION

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*

1983-08-31
1987-04-28
Cell Environmental Systems, Ltd.
Cell culture system

EP0154845A3
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1984-02-24
1986-06-18
Sartorius GmbH.
Flat filter element for the filtration of fluids

SE452451B
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1984-06-07
1987-11-30
Svenska Utvecklings Ab

MEMBRANE STILLATION DEVICE

DE3441190A1
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*

1984-11-10
1986-05-15
Metallgesellschaft Ag, 6000 Frankfurt

DEVICE FOR SEPARATING LIQUID MIXTURES BY PERVAPORATION

DE3529175A1
(en)

*

1985-08-14
1987-02-19
Gft Ingenieurbuero

DEVICE FOR SEPARATING MIXED MEANS OF THE PERVAPORATION METHOD

US5868930A
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*

1986-11-26
1999-02-09
Kopf; Henry B.
Filtration cassette article and filter comprising same

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1986-11-26
1997-01-14
Kopf; Henry B.
Filtration cassette article, and filter comprising same

JPH01124467A
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*

1987-06-25
1989-05-17
Terumo Corp
Blood component separator

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*

1987-10-02
1989-11-21
Kopf Henry B
Filter plate, filter plate element, and filter comprising same

US4867876A
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*

1987-10-02
1989-09-19
Kopf Henry B
Filter plate, filter plate element, and filter comprising same

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*

1987-10-02
1993-08-03
Kopf Henry B
Filter element and support

US5049268A
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*

1987-10-02
1991-09-17
Kopf Henry B
Filter plate, filter plate element, and filter comprising same

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1987-10-02
1994-08-30
Kopf Henry B
Filtration cassette article, and filter comprising same

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1987-10-02
1990-09-11
Kopf Henry B
Filter plate, filter plate element and filter comprising same

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*

1989-02-27
1990-10-09
Exxon Research And Engineering Company
Multi-stage pervaporation process run at progressively higher vacuum, higher temperature or both at each successive retentate stage

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*

1989-05-19
1993-02-02
Sweetana Stephanie A
Apparatus for in vitro determination of substances across membranes, biological tissues, or cell cultures

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*

1989-09-15
1992-04-14
Exxon Research And Engineering Company
Flat stack permeator

US5002667A
(en)

*

1990-10-30
1991-03-26
National Research Council Of Canada
Fluid fractionating, stacked permeable membrane envelope assembly, and a fluid distributing and permeable membrane sealing collar

CH685331A5
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*

1992-05-27
1995-06-15
Krebs & Co Ag
Module to perform the pervaporation of fluids.

DE4225060C1
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*

1992-07-29
1993-09-23
Deutsche Carbone Ag, 6680 Neunkirchen, De

US5591636A
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*

1993-10-18
1997-01-07
Precision Instrument Design
Membrane holder

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*

1993-10-18
1997-02-04
Precision Instrument Design
Device and method for circulating fluid over a membrane

US6129973A
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1994-07-29
2000-10-10
Battelle Memorial Institute
Microchannel laminated mass exchanger and method of making

DE4446270C1
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*

1994-12-23
1996-02-29
Hewlett Packard Gmbh
Liquid chromatography de-gasifier

GB9600211D0
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*

1996-01-05
1996-03-06
Jem Smoke Machine Company Limi
Improvements in or relating to a vaporiser

US6152995A
(en)

1999-03-22
2000-11-28
Idatech Llc
Hydrogen-permeable metal membrane and method for producing the same

US7195663B2
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1996-10-30
2007-03-27
Idatech, Llc
Hydrogen purification membranes, components and fuel processing systems containing the same

US6494937B1
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2001-09-27
2002-12-17
Idatech, Llc
Hydrogen purification devices, components and fuel processing systems containing the same

US6537352B2
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1996-10-30
2003-03-25
Idatech, Llc
Hydrogen purification membranes, components and fuel processing systems containing the same

US6783741B2
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*

1996-10-30
2004-08-31
Idatech, Llc
Fuel processing system

US6319306B1
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*

2000-03-23
2001-11-20
Idatech, Llc
Hydrogen-selective metal membrane modules and method of forming the same

US6171374B1
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*

1998-05-29
2001-01-09
Ballard Power Systems Inc.
Plate and frame fluid exchanging assembly with unitary plates and seals

US6146883A
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*

1998-09-14
2000-11-14
Navicyte, Inc.
Packing device for transporting confluent cell monolayers

US6602325B1
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1999-10-21
2003-08-05
Ati Properties, Inc.
Fluid separation assembly

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1999-10-21
2002-07-16
Ati Properties, Inc.
Fluid separation assembly and fluid separation module

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1998-11-10
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Fluid separation assembly and fluid separation module

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1998-11-10
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Hydrogen separation membrane

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1999-03-22
2004-07-27
Idatech, Llc
Hydrogen-selective metal membranes, membrane modules, purification assemblies and methods of forming the same

US6596057B2
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1999-03-22
2003-07-22
Idatech, Llc
Hydrogen-selective metal membranes, membrane modules, purification assemblies and methods of forming the same

US20010045061A1
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2000-03-13
2001-11-29
Ida Tech, L.L.C.
Fuel processor and systems and devices containing the same

US6875247B2
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2000-06-06
2005-04-05
Battelle Memorial Institute
Conditions for fluid separations in microchannels, capillary-driven fluid separations, and laminated devices capable of separating fluids

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2000-06-06
2003-12-23
Battelle Memorial Institute
Microsystem capillary separations

US6569227B2
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2001-09-27
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Idatech, Llc
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2001-03-08
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Hydrogen purification devices, components and fuel processing systems containing the same

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2001-04-13
2002-10-17
Andreas Deuschle
Spacer for membrane stacks

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2001-10-26
2007-05-07
에스케이 주식회사
Hydrogen purification module

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2001-12-12
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윤석원
Plate-type module for performing pervaporation

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2002-02-15
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Denco, Inc.
Spin-hemodialysis assembly and method

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2003-02-19
2004-09-02
Mcmaster University
Composite materials comprising supported porous gels

DE10324300B4
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*

2003-05-21
2006-06-14
Thomas Dr. Weimer

Thermodynamic machine and method for absorbing heat

US7303681B2
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*

2003-11-18
2007-12-04
Exxonmobil Research And Engineering Company
Dynamic membrane wafer assembly and method

US7318898B2
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2003-11-18
2008-01-15
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Polymeric membrane wafer assembly and method

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2003-11-18
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エクソンモービル リサーチ アンド エンジニアリング カンパニー

Method and system for separating components for mixing

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*

2003-11-18
2006-08-16
ExxonMobil Research and Engineering Company
Method and apparatus for separating aromatic hydrocarbons in a non-adiabatic membrane system

WO2005097304A1
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*

2004-04-08
2005-10-20
Mcmaster University
Membrane stacks

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2004-06-07
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Mcmaster University
Stable composite material comprising supported porous gels

US7959780B2
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2004-07-26
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Textured ion exchange membranes

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2005-09-16
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Self-regulating feedstock delivery systems and hydrogen-generating fuel processing assemblies and fuel cell systems incorporating the same

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Disposable tangential flow filtration device holder

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Cassette-style filtration apparatus

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* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US2778096A
(en)

*

1957-01-22

weema

US2249063A
(en)

*

1938-05-12
1941-07-15
Texas Gulf Sulphur Co
Filter leaf

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*

1963-06-05
1967-09-19
American Mach & Foundry
Ion exchange membrane fabrication

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*

1966-08-09
1968-08-20
Ionics
Membrane separation apparatus and process

1968

1968-12-24
US
US786634A
patent/US3520803A/en
not_active
Expired – Lifetime

1969

1969-12-01
GB
GB1290002D
patent/GB1290002A/en
not_active
Expired

1969-12-01
GB
GB1290001D
patent/GB1290001A/en
not_active
Expired

1969-12-01
GB
GB1290003D
patent/GB1290003A/en
not_active
Expired

1969-12-04
FR
FR6941947A
patent/FR2026998A1/fr
not_active
Withdrawn

1969-12-17
NL
NL6918953A
patent/NL6918953A/xx
unknown

1969-12-23
DE
DE19691964635
patent/DE1964635A1/en
active
Pending

1970

1970-04-22
US
US30661A
patent/US3695444A/en
not_active
Expired – Lifetime

Also Published As

Publication number
Publication date

GB1290002A
(en)

1972-09-20

GB1290003A
(en)

1972-09-20

US3520803A
(en)

1970-07-21

DE1964635A1
(en)

1970-07-09

FR2026998A1
(en)

1970-09-25

NL6918953A
(en)

1970-06-26

US3695444A
(en)

1972-10-03

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1973-05-09
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Application of which complete specification have been accepted and published, but patent is not sealed

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