GB1054774A - - Google Patents
Info
- Publication number
- GB1054774A GB1054774A GB1054774DA GB1054774A GB 1054774 A GB1054774 A GB 1054774A GB 1054774D A GB1054774D A GB 1054774DA GB 1054774 A GB1054774 A GB 1054774A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tubes
- porous
- membrane
- cellulose acetate
- impregnated
- Prior art date
- 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.)
- Active
Links
Classifications
-
- 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
- B01D63/06—Tubular membrane modules
- B01D63/062—Tubular membrane modules with membranes on a surface of a support tube
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
1,054,774. Liquid diffusion apparatus. G. G. HAVENS. July 2, 1966 [July 10, l962], No. 26132/63. Headings B1X and B2K. A solvent separation apparatus includes a plurality of elongate rigid porous tubes having a semipermeable membrane on either the inner or outer surface thereof, the tubes being operative to pass water at a higher rate than dissolved salts and means for circulating a solution at a pressure exceeding the osmotic pressure difference across the membrane. Saline water is maintained at 1000 to 1500 p.s.i. by pump 12, the water being circulated by way of tubes 14, tank 18 and pump 20. A salinity monitor automatically bleeds off brine at valve 22 when the salt concentration is high. Tierods 44 through end supports 36 hold the porous tubes against gasket 40 in the pressure vessel 24. The tubes are made from a glass fibre screen, mesh or fabric impregnated with a phenolic resin thereby giving a porous tube upon curing. The tubes are manufactured by winding with a bias ribbons of resin impregnated fabric on a mandrel coated with a parting agent. The wound mandrel is wrapped in cellulose acetate, cured at 180‹C for 2 hrs. and the cellulose acetate removed. A solution of cellulose acetate, acetone and aqueous magnesium perchlorate is used to coat the porous tubes which is subsequently treated at room temperature, 0‹, 30 to 50‹ and finally 80‹C. The porous tubes may be modified by interposing a layer of unimpregnated fibre e.g. a spiral wrapping of glass fibre roving, between the impregnated tube and the semi-permeable membrane. A further modification is the use of a pattern of grooves to promote the formation of conical pores or gaseous inclusions which aid diffusion speeds. An alternative embodiment (Fig. 5, not shown) incorporates a series of cylindrical tubes closed at one end within a pressure vessel, the vessel containing saline water while the membrane is on the outside of the tubes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US20877662A | 1962-07-10 | 1962-07-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1054774A true GB1054774A (en) |
Family
ID=22776013
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1054774D Active GB1054774A (en) | 1962-07-10 |
Country Status (6)
Country | Link |
---|---|
BE (1) | BE634211A (en) |
DE (1) | DE1442421A1 (en) |
FR (1) | FR1395552A (en) |
GB (1) | GB1054774A (en) |
NL (2) | NL295120A (en) |
SE (1) | SE321207B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2035371A1 (en) * | 1969-07-16 | 1971-01-28 | United Kingdom Atomic Energy Authority, London | Method and device for the manufacture of a membrane arrangement |
GB2223690A (en) * | 1988-10-17 | 1990-04-18 | Roger Stanley White | Filter tubes |
US5840186A (en) * | 1994-09-15 | 1998-11-24 | British Nuclear Fuels Plc | Liquid filtration apparatus |
GB2469582A (en) * | 2009-04-18 | 2010-10-20 | Fairey Filtration Systems Ltd | Filter material |
US20220161203A1 (en) * | 2019-04-10 | 2022-05-26 | Berghof Membrane Technology GmbH | Tubular membrane comprising longitudinal ridges, device provided therewith and method for producing such membrane |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3341024A (en) * | 1965-10-04 | 1967-09-12 | Lowe Edison | Apparatus for molecular filtration and methods for its fabrication |
US3369667A (en) * | 1966-03-08 | 1968-02-20 | Universal Water Corp | Reverse osmosis apparatus having feed recirculation means |
US3544358A (en) * | 1966-07-18 | 1970-12-01 | Universal Water Corp | Production of semipermeable membranes directly on the surfaces of permeable support bodies |
US3430770A (en) * | 1966-11-21 | 1969-03-04 | Universal Water Corp | Reverse osmosis apparatus |
GB1168722A (en) * | 1967-02-22 | 1969-10-29 | Atomic Energy Authority Uk | Improvements in or relating to Reverse Osmosis. |
US3581900A (en) * | 1967-10-25 | 1971-06-01 | Aqua Chem Inc | Reverse osmosis liquid purification |
JPS57209603A (en) * | 1981-06-26 | 1982-12-23 | Nikoraebitsuchi Chi Reonitsudo | Membrane element and apparatus for separating mixture of gas and liquid phases |
DE102010035336A1 (en) | 2010-08-24 | 2012-03-01 | Bvp Gmbh | Method for capturing, storing, analyzing and verifying movement dynamics e.g. touching dynamics of people, involves amplifying, storing and evaluating measured values of pressure-dependent spacing of write plate to base plate |
-
0
- BE BE634211D patent/BE634211A/xx unknown
- NL NL134680D patent/NL134680C/xx active
- NL NL295120D patent/NL295120A/xx unknown
- GB GB1054774D patent/GB1054774A/en active Active
-
1963
- 1963-06-18 DE DE19631442421 patent/DE1442421A1/en active Pending
- 1963-06-25 FR FR939241A patent/FR1395552A/en not_active Expired
- 1963-07-01 SE SE728263A patent/SE321207B/xx unknown
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2035371A1 (en) * | 1969-07-16 | 1971-01-28 | United Kingdom Atomic Energy Authority, London | Method and device for the manufacture of a membrane arrangement |
GB2223690A (en) * | 1988-10-17 | 1990-04-18 | Roger Stanley White | Filter tubes |
GB2223690B (en) * | 1988-10-17 | 1991-05-01 | Roger Stanley White | Filtration systems |
US5840186A (en) * | 1994-09-15 | 1998-11-24 | British Nuclear Fuels Plc | Liquid filtration apparatus |
GB2469582A (en) * | 2009-04-18 | 2010-10-20 | Fairey Filtration Systems Ltd | Filter material |
GB2469582B (en) * | 2009-04-18 | 2013-12-25 | Mantec Technical Ceramics Ltd | Filter |
US20220161203A1 (en) * | 2019-04-10 | 2022-05-26 | Berghof Membrane Technology GmbH | Tubular membrane comprising longitudinal ridges, device provided therewith and method for producing such membrane |
Also Published As
Publication number | Publication date |
---|---|
NL134680C (en) | |
BE634211A (en) | |
NL295120A (en) | |
SE321207B (en) | 1970-03-02 |
FR1395552A (en) | 1965-04-16 |
DE1442421A1 (en) | 1969-11-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1054774A (en) | ||
JPS59218161A (en) | Hollow fiber membrane type artificial lung and production thereof | |
US3457170A (en) | Solvent separation process and apparatus | |
US3422008A (en) | Wound hollow fiber permeability apparatus and process of making the same | |
US3651616A (en) | Process for effecting absorption or removal of gas from a liquid | |
US3850203A (en) | Porous tube device for bilateral osmotic processes | |
FR2212166A1 (en) | Sepn processes using hollow fibres - spirally wound on core to form cartridge of small cylindrical membranes | |
GB1325672A (en) | Method of producing a membrane assembly and an apparatus for use therein | |
GB1415752A (en) | Membrane on a hollow cord | |
US4681713A (en) | Method of making a hollow fiber membrane for dialysis | |
EP0012630B1 (en) | Process for producing a cellulose acetate-type permselective membrane, permselective membrane thus produced, and use of such membrane in artificial kidney | |
GB2035197A (en) | Process for the production of semipermeable hollow fiber membranes | |
US2197805A (en) | Dialyzing diaphragms and process of making the same | |
JPH035847B2 (en) | ||
US3721596A (en) | Fluid separation and method and apparatus for forming same | |
US5968358A (en) | Method for washing hollow fiber membrane | |
JPH055529B2 (en) | ||
JPS5457475A (en) | Manufacture of selective permeable-membrane | |
JPS55155704A (en) | Hollow semipermeable membrane and its production | |
JPS5580514A (en) | Production of hollow fiber | |
JPS6054712A (en) | Hollow yarn membrane separation module | |
JPS55132605A (en) | Preparation of semi-permeable membrane | |
JPS60249970A (en) | Production of hollow fiber membrane type artificial lung | |
JPS5580515A (en) | Production of hollow fiber | |
GB1299977A (en) | Improvements in and relating to the formation of membranes |