GB1106664A - Improvements in and relating to membranes - Google Patents

Improvements in and relating to membranes

Info

Publication number
GB1106664A
GB1106664A GB23445/65A GB2344565A GB1106664A GB 1106664 A GB1106664 A GB 1106664A GB 23445/65 A GB23445/65 A GB 23445/65A GB 2344565 A GB2344565 A GB 2344565A GB 1106664 A GB1106664 A GB 1106664A
Authority
GB
United Kingdom
Prior art keywords
alginate
substrate
membrane
gel
solution
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.)
Expired
Application number
GB23445/65A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sartorius Membranfilter GmbH
Original Assignee
Sartorius Membranfilter GmbH
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.)
Filing date
Publication date
Application filed by Sartorius Membranfilter GmbH filed Critical Sartorius Membranfilter GmbH
Publication of GB1106664A publication Critical patent/GB1106664A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • B01D67/0009Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0039Inorganic membrane manufacture
    • B01D67/0046Inorganic membrane manufacture by slurry techniques, e.g. die or slip-casting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12Composite membranes; Ultra-thin membranes
    • B01D69/125In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/08Polysaccharides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/006Heteroglycans, i.e. polysaccharides having more than one sugar residue in the main chain in either alternating or less regular sequence; Gellans; Succinoglycans; Arabinogalactans; Tragacanth or gum tragacanth or traganth from Astragalus; Gum Karaya from Sterculia urens; Gum Ghatti from Anogeissus latifolia; Derivatives thereof
    • C08B37/0084Guluromannuronans, e.g. alginic acid, i.e. D-mannuronic acid and D-guluronic acid units linked with alternating alpha- and beta-1,4-glycosidic bonds; Derivatives thereof, e.g. alginates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2323/00Details relating to membrane preparation
    • B01D2323/12Specific ratios of components used
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N2796/00Viruses not covered by groups C12N2710/00 - C12N2795/00

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Materials Engineering (AREA)
  • Biochemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Molecular Biology (AREA)
  • General Health & Medical Sciences (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Materials For Medical Uses (AREA)
  • Cosmetics (AREA)

Abstract

Alginate membranes are prepared by applying a layer of an aqueous solution of an alkyl ammonium alginate to a porous substrate saturated with a solution containing polyvalent cations that form an alginate gel by reaction with the alginate solution, the alginate solution before application to the substrate being mixed with a softener, and after the gel-forming process the gel and the substrate are dried. A hygroscopic liquid which is difficultly volatile is preferably used as softener, e.g. glycerol. When the membrane is washed through e.g. in the case of filtrations, the softener is washed out by water. The partly shrunk alginate membrane on drying is detached from its connection with the substrate and the membrane together with the filter residue from the substrate removed. The membrane may be floated off the substrate. In examples, a sheet of porous filter substrate is saturated with an aqueous solution of AlCl36H2O, or La(NO3)3. 6H2O. A solution of sodium alginate and glycerine is spread over the saturated substrate, whereupon an alginate gel is formed, and the whole is air dried at ambient temperature. The alginate membranes can be used in pressure apparatus.ALSO:Alginate membranes for use as ion-exchange membranes are prepared by applying a layer of an aqueous solution of an alkyl ammonium alginate to a porous substrate, for example a paper or membrane filter saturated with a solution containing polyvalent cations that form an alginate gel by reaction with the alginate solution, the alginate solution before application to the substrate being mixed with a softener, and, after the gel-forming process, the gel and the substrate are dried by being subjected to a drying process. A hygroscopic liquid which is difficultly volatile is preferably used as softener, e.g. glycerol. When the membrane is washed through, e.g. in the case of filtrations, the softener is washed out by water. The partly shrunk alginate membrane on drying is detached from its connection with the substrate and the membrane together with the filter residue from the substrate removed. The membrane may be floated off the substrate. In Example 1, a sheet of porous filter substrate is saturated with an aqueous solution of AlCl3 6H2O. A solution of sodium alginate and glycerine is spread over the saturated substrate, whereupon an alginate gel is formed, and the whole is air dried at ambient temperature. In Example 2, La (NO3)3 6H2O is used instead of AlCl3 6H2O. The alginate membranes can be used in pressure apparatus.
GB23445/65A 1964-06-05 1965-06-02 Improvements in and relating to membranes Expired GB1106664A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1964M0061265 DE1470890A1 (en) 1964-06-05 1964-06-05 Process for the production of alginate membranes

Publications (1)

Publication Number Publication Date
GB1106664A true GB1106664A (en) 1968-03-20

Family

ID=7310076

Family Applications (1)

Application Number Title Priority Date Filing Date
GB23445/65A Expired GB1106664A (en) 1964-06-05 1965-06-02 Improvements in and relating to membranes

Country Status (3)

Country Link
DE (1) DE1470890A1 (en)
FR (1) FR1456501A (en)
GB (1) GB1106664A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003086360A1 (en) * 2002-04-15 2003-10-23 Beisel Guenther Agent for producing a sensation of satiety and for weight loss

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2592383B1 (en) * 1985-12-26 1990-01-19 Adeline Andre PROCESS FOR THE PREPARATION OF A FLEXIBLE FILM OF CALCIUM ALGINATE
US5043069A (en) * 1989-10-18 1991-08-27 E. I. Du Pont De Nemours And Company Filtration device having hardened gum formed-in-place membranes

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003086360A1 (en) * 2002-04-15 2003-10-23 Beisel Guenther Agent for producing a sensation of satiety and for weight loss

Also Published As

Publication number Publication date
DE1470890A1 (en) 1969-02-20
FR1456501A (en) 1966-10-28

Similar Documents

Publication Publication Date Title
FR2286962A1 (en) PRESSURE TANK
SE410815B (en) PROCEDURE FOR EXPANSION OF TOBACCO
ATE11228T1 (en) USE OF POLYVINYL ALCOHOL WATER PERMEABLE FILMS.
GB1106664A (en) Improvements in and relating to membranes
ES336141A1 (en) Procedure for the production of films based on polyvinyl alcohol. (Machine-translation by Google Translate, not legally binding)
NL7507330A (en) PROCESS FOR PREPARING COLORLESS TRIETHYLENE TETRAMINE AND TETRAETHYLENE PENTAMINE.
SE7313965L (en)
FI823797A0 (en) KATJONBYTARMEMBRANER FOER ELEKTROLYSCELL OCH FOERFARANDEN FOER FRAMSTAELLNING OCH REPARERING AV DESAMMA
ES447235A1 (en) High temperature and high pressure steamer
DE2043393B2 (en) DEVICE FOR REMOVING FOREIGN BODIES OF CERTAIN COLOR FROM LIQUID, COLORLESS OR NEARLY COLORLESS SUBSTANCE CONTAINING DIFFERENT COLOR FOREIGN BODIES
FR2278004A1 (en) PRESSURE TANK
CH540207A (en) Process for pyrolysis of a liquid or gaseous medium, application of this process and device for carrying out the process
DK150114C (en) MEMBRANE PRESSURE CUMULATOR FOR LIQUIDS
SE416978B (en) PROCEDURE FOR WETTING THE FIBER PLATE
JPS56144705A (en) Desorption of polyvinyl alcohol polymer adsorbed on silica
SU663937A1 (en) Valve for gas inlet to reservoir with liquid
JPS53136890A (en) Ionic electrode
JPS5387982A (en) Regulating method for membrane performance of semi-permeable membrane
JPS5241174A (en) Concentrating process by dehydration with osmotic pressure of solute
FR2225775A1 (en) Prepg cine film for re-use as e.g. header strip - by removing gelatin coating and applying cellulose ink
KR880000100A (en) Method for preparing Peony Licorice gel (or sol)
ES257400A1 (en) A procedure for obtaining stable gelified particles (Machine-translation by Google Translate, not legally binding)
ATA258176A (en) DEVICE FOR EXOTHERMAL ABSORPTION OF GASES IN LIQUIDS, ESPECIALLY AMMONIA IN WATER
NL7500766A (en) METHOD AND LIQUID PREPARATION FOR DRYING WATER-MOISTENED SURFACES.
ES450221A1 (en) A procedure to manufacture an adhesive material sensitive to pressure (Machine-translation by Google Translate, not legally binding)