GB911223A - Diethylyaminoethyl celluloses - Google Patents
Diethylyaminoethyl cellulosesInfo
- Publication number
- GB911223A GB911223A GB36277/59A GB3627759A GB911223A GB 911223 A GB911223 A GB 911223A GB 36277/59 A GB36277/59 A GB 36277/59A GB 3627759 A GB3627759 A GB 3627759A GB 911223 A GB911223 A GB 911223A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cellulose
- mesh
- water
- amorphous
- particles
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2405—Glucanases
- C12N9/2408—Glucanases acting on alpha -1,4-glucosidic bonds
- C12N9/2411—Amylases
- C12N9/2414—Alpha-amylase (3.2.1.1.)
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01D—HARVESTING; MOWING
- A01D87/00—Loaders for hay or like field crops
- A01D87/0038—Dumpboxes or metering devices for loading or unloading
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/08—Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/16—Organic material
- B01J39/18—Macromolecular compounds
- B01J39/22—Cellulose or wood; Derivatives thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
- B01J41/08—Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
- B01J41/12—Macromolecular compounds
- B01J41/16—Cellulose or wood; Derivatives thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41N—PRINTING PLATES OR FOILS; MATERIALS FOR SURFACES USED IN PRINTING MACHINES FOR PRINTING, INKING, DAMPING, OR THE LIKE; PREPARING SUCH SURFACES FOR USE AND CONSERVING THEM
- B41N3/00—Preparing for use and conserving printing surfaces
- B41N3/08—Damping; Neutralising or similar differentiation treatments for lithographic printing formes; Gumming or finishing solutions, fountain solutions, correction or deletion fluids, or on-press development
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B11/00—Preparation of cellulose ethers
- C08B11/02—Alkyl or cycloalkyl ethers
- C08B11/04—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals
- C08B11/14—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals with nitrogen-containing groups
- C08B11/145—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals with nitrogen-containing groups with basic nitrogen, e.g. aminoalkyl ethers
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D127/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers
- C09D127/02—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
- C09D127/04—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C09D127/06—Homopolymers or copolymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2405—Glucanases
- C12N9/2408—Glucanases acting on alpha -1,4-glucosidic bonds
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/24—Hydrolases (3) acting on glycosyl compounds (3.2)
- C12N9/2402—Hydrolases (3) acting on glycosyl compounds (3.2) hydrolysing O- and S- glycosyl compounds (3.2.1)
- C12N9/2405—Glucanases
- C12N9/2408—Glucanases acting on alpha -1,4-glucosidic bonds
- C12N9/2411—Amylases
- C12N9/2414—Alpha-amylase (3.2.1.1.)
- C12N9/2417—Alpha-amylase (3.2.1.1.) from microbiological source
- C12N9/242—Fungal source
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F11/00—Chemical after-treatment of artificial filaments or the like during manufacture
- D01F11/02—Chemical after-treatment of artificial filaments or the like during manufacture of cellulose, cellulose derivatives, or proteins
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
- D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Molecular Biology (AREA)
- Biochemistry (AREA)
- Medicinal Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Environmental Sciences (AREA)
- Mycology (AREA)
- Polymers & Plastics (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
An ion-exchange material comprises diethylaminoethyl cellulose, the cellulose having an essentially amorphous structure. It is made by reacting amorphous cellulose with an alkali metal hydroxide to form alkali cellulose, which is then reacted with a diethylhaloethylamine. Amorphous cellulose is made by very slow extrusion of viscose into an acid coagulating bath, no tension being applied to the filaments, which suitably are monofils of 1,000-60,000 denier and preferably of 25,000 denier. The monofils may be cut into pieces 1/4 inch in length, and milled to form particles not greater than 10 B.S. mesh, preferably between 16 and 52 B.S. mesh. The cellulose particles may then be treated with caustic soda, followed by diethylchloroethylamine. The material so made may be filled into a glass column as a suspension in water, buffered with 0,1 M sodium dihydrogen phosphate at pH 6,6, and used for purification or concentration of proteinceous material, e.g. a -amylase (see Group IV(b) or of poliomyelitis virus, Vitamin B12 acid (by adsorption) and Vitamin B12 (by adsorption of impurities while the vitamin passes through the column), or for the demineralisation of water.ALSO:Diethylaminoethyl cellulose, in which the cellulose residue has an essentially amorphous structure, is made by reacting amorphous cellulose with an alkali metal hydroxide to form alkali cellulose which is then reacted with a diethylhaloethylamine. Amorphous cellulose is made by very slow extrusion of viscose into an acid coagulating bath, no tension being applied to the filaments, which suitably are monofils of 1,000-60,000 denier and preferably of 25,000 denier. The monofils may be cut into pieces 1/4 inch in length, and milled to form particles not greater than 10 B.S. mesh, preferably between 16 and 52 B.S. mesh. The cellulose particles may then be treated with caustic soda, followed by diethylchloroethylamine. In an example, 1,058 Kg. of amorphous cellulose particles between 16 and 52 B.S. mesh are mixed at 11 DEG C. for one hour with 5,3:1 of 6N NaOH. A solution of 1,058 Kg. of diethylchloroethylamine hydrochloride in 1,6:1 of water is then added, and the whole mixed continuously for 35 minutes at 85 DEG C. The mixture is then cooled to room temperature and acidified with 2,5:1 concentrated hydrochloric acid, filtered, and the residue washed with 12:1 tap water, 5,3:1 N.NaOH and then with tap water until the washings are almost neutral. For the application of the product as an ion-exchange material, (see Group III).ALSO:a -Amylase may be separated, purified and concentrated by means of an ion-exchange material comprising diethylaminoethyl cellulose the cellulose having an essentially amorphous structure. The ion-exchange material is made by reacting amorphous cellulose with an alkali metal hydroxide to form alkali cellulose, which is then reacted with a diethylhaloethylamine. Amorphous cellulose is made by very slow extrusion of viscose into an acid coagulating bath, no tension being applied to the filaments, which suitably are monofils of 1,000-60,000 denier and preferably of 25,000 denier. The monofils may be cut into pieces 1/4 inch in length, and milled to form particles not greater than 10 B.S. mesh, preferably between 16 and 52 B.S. mesh. The cellulose particles may then be treated with caustic soda, followed by diethylchloroethylamine. In an example, 1.058 Kg. of amorphous cellulose particles between 16 and 52 B.S. mesh are mixed at 11 DEG C. for one hour with 5.3 l. of 6N NaOH. A solution of 1.058 Kg. of diethylchloroethylamine hydrochloride in 1.6 l. of water is then added, and the whole mixed continuously for 35 minutes at 85 DEG C. The mixture is then cooled to room temperature and acidified with 2.5 l. concentrated hydrochloric acid, filtered, and the residue washed with 12 l. tap water, 5.3 l. N.NaOH and then with tap water until the washings are almost neutral. The material so made may be filled into a 10 ft. X 2 in. glass column as a suspension in water to give a 7 ft. bed of about 4.2 l. volume. The bed is then buffered with 8.4 l. 0.1 M sodium dihydrogen phosphate at pH 6.6 fed downflow at 8.4 l./hr. In an example, 75 l. of fungal a -amylase broth at a dextrinising activity of 14.0 units/ml., equivalent to 1,050 kilo units total activity, are adjusted to pH 6.6 with acetic acid, passed through a sterilising grade of filter paper and fed downflow through the bed at 4.2 l./hr. followed by 4.2 l. water as displacement wash at 4.2 l./hr. Analysis of the column effluent showed 1.7 kilo units total dextrinising activity, giving 1,048.3 kilo units adsorbed, equivalent to 99.8% efficiency. The adsorbed amylase is recovered by downflow elution with 4.2 l. 0.8 M sodium acetate/0.8 M sodium chloride buffer at pH 4.7 followed by a 4.2 l. displacement water wash, all at 2.1 l./hr. A 7 l. portion of the eluate contained 992.2 kilo units total dextrinising activity, representing 94.6% efficiency and a ten fold concentration of the original broth.ALSO:Poliomyelitis virus may be purified or concentrated by means of an ion-exchange material comprising diethylaminoethyl cellulose, the cellulose having an essentially amorphous structure. The ion-exchange material is made by reacting amorphous cellulose with an alkali metal hydroxide to form alkali cellulose, which is then reacted with a diethylhaloethyl amine. The material so made may be filled into a 10 feet x 2 inches glass column as a suspension in water to give a 7 feet bed of about 4.2 1. volume. The bed is then buffered with 8.4 1. 0.1 M sodium dihydrogen phosphate at pH 6.6 fed downflow at 8.4 1/hr.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL257284D NL257284A (en) | 1959-10-26 | ||
NL127841D NL127841C (en) | 1959-10-26 | ||
GB36277/59A GB911223A (en) | 1959-10-26 | 1959-10-26 | Diethylyaminoethyl celluloses |
DEG30747A DE1215124B (en) | 1959-10-26 | 1960-10-21 | Process for the production of diaethylaminoethyl cellulose ethers which can be used as anion exchangers |
CH1194260A CH395956A (en) | 1959-10-26 | 1960-10-25 | Process for the production of an ion exchanger |
FR842106A FR1271945A (en) | 1959-10-26 | 1960-10-25 | New cellulose derivatives |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB36277/59A GB911223A (en) | 1959-10-26 | 1959-10-26 | Diethylyaminoethyl celluloses |
Publications (1)
Publication Number | Publication Date |
---|---|
GB911223A true GB911223A (en) | 1962-11-21 |
Family
ID=10386639
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB36277/59A Expired GB911223A (en) | 1959-10-26 | 1959-10-26 | Diethylyaminoethyl celluloses |
Country Status (5)
Country | Link |
---|---|
CH (1) | CH395956A (en) |
DE (1) | DE1215124B (en) |
FR (1) | FR1271945A (en) |
GB (1) | GB911223A (en) |
NL (2) | NL127841C (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2073697A5 (en) * | 1969-12-22 | 1971-10-01 | Baxter Laboratories Inc | |
US3785771A (en) * | 1969-08-19 | 1974-01-15 | Du Pont | Method and apparatus for analyzing a liquid containing macromolecules that would interfere with the analysis |
EP0185379A2 (en) * | 1984-12-20 | 1986-06-25 | NABISCO BRANDS, Inc. | A process for the production of purified glucose isomerase |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2422699A1 (en) * | 1978-04-12 | 1979-11-09 | Merieux Inst | Materials for affinity chromatography of biological macromolecules - comprise support coated with polysaccharide coupled to amine |
-
0
- NL NL257284D patent/NL257284A/xx unknown
- NL NL127841D patent/NL127841C/xx active
-
1959
- 1959-10-26 GB GB36277/59A patent/GB911223A/en not_active Expired
-
1960
- 1960-10-21 DE DEG30747A patent/DE1215124B/en active Pending
- 1960-10-25 CH CH1194260A patent/CH395956A/en unknown
- 1960-10-25 FR FR842106A patent/FR1271945A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3785771A (en) * | 1969-08-19 | 1974-01-15 | Du Pont | Method and apparatus for analyzing a liquid containing macromolecules that would interfere with the analysis |
FR2073697A5 (en) * | 1969-12-22 | 1971-10-01 | Baxter Laboratories Inc | |
EP0185379A2 (en) * | 1984-12-20 | 1986-06-25 | NABISCO BRANDS, Inc. | A process for the production of purified glucose isomerase |
EP0185379A3 (en) * | 1984-12-20 | 1988-05-11 | NABISCO BRANDS, Inc. | A process for the production of purified glucose isomerase |
Also Published As
Publication number | Publication date |
---|---|
DE1215124B (en) | 1966-04-28 |
FR1271945A (en) | 1961-09-15 |
CH1194260A4 (en) | 1966-01-14 |
NL257284A (en) | |
CH395956A (en) | 1966-01-14 |
NL127841C (en) |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0026970B1 (en) | Process for recovering interferon | |
EP0447585B2 (en) | Process for manufacturing an intravenously tolerant immunoglobulin-G preparation | |
DE69534749T2 (en) | PREPARATION OF THROMBIN THERAPEUTIC QUALITY LEVEL | |
CN105198762B (en) | Enzymatic lysis method produces the comprehensive recovering process of effective ingredient in 7-amino-cephalosporanic acid crystalline mother solution | |
ES8607748A1 (en) | Treatment process for commercial pellets to improve gas separation kinetics. | |
GB911223A (en) | Diethylyaminoethyl celluloses | |
GB1016150A (en) | Method of amylose purification | |
DE2551966C3 (en) | Method of purifying urokinase | |
Kanfer et al. | Purification of α-and β-galactosidases by affinity chromatography | |
US3723251A (en) | Method for extracting urokinase | |
US3095410A (en) | Deae substituted balsa wood ion-exchange material | |
DE2616761C3 (en) | Process for the production of urokinase | |
US3132994A (en) | Polymyxin purification | |
US3102113A (en) | Unoriented particulate deae-cellulose ion exchange material | |
EP0302503B1 (en) | Method for the separation and purification of t-pa | |
US2643210A (en) | Vitamin b12-active substance elution from montmorillonite absorbent | |
KR910003112A (en) | Method for obtaining, separating and purifying epidermin | |
US4196285A (en) | Antibiotic purification process | |
US2677644A (en) | Purification of vitamin b12 solutions | |
DE1284391B (en) | Adsorption of amylase on starch | |
JPS5982340A (en) | Purification of abscisic acid | |
JPS6031479B2 (en) | Method for producing pure chondroitinase C | |
DE2143815A1 (en) | Process for removing pyrogenic substances from urokinase | |
DE932576C (en) | Process for the purification of impure aqueous solutions which contain vitamin B and variants thereof | |
DE1289809B (en) | Process for the production of urokinase for injection purposes |