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GB1071170A - Method of manufacturing minute capsules - Google Patents

Method of manufacturing minute capsules

Info

Publication number
GB1071170A
GB1071170A GB4819165A GB4819165A GB1071170A GB 1071170 A GB1071170 A GB 1071170A GB 4819165 A GB4819165 A GB 4819165A GB 4819165 A GB4819165 A GB 4819165A GB 1071170 A GB1071170 A GB 1071170A
Authority
GB
United Kingdom
Prior art keywords
wall
forming polymer
liquid vehicle
solution
coacervate
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
GB4819165A
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.)
NCR Voyix Corp
National Cash Register Co
Original Assignee
NCR Corp
National Cash Register Co
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 NCR Corp, National Cash Register Co filed Critical NCR Corp
Publication of GB1071170A publication Critical patent/GB1071170A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/06Making microcapsules or microballoons by phase separation
    • B01J13/10Complex coacervation, i.e. interaction of oppositely charged particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M5/00Duplicating or marking methods; Sheet materials for use therein
    • B41M5/124Duplicating or marking methods; Sheet materials for use therein using pressure to make a masked colour visible, e.g. to make a coloured support visible, to create an opaque or transparent pattern, or to form colour by uniting colour-forming components
    • B41M5/165Duplicating or marking methods; Sheet materials for use therein using pressure to make a masked colour visible, e.g. to make a coloured support visible, to create an opaque or transparent pattern, or to form colour by uniting colour-forming components characterised by the use of microcapsules; Special solvents for incorporating the ingredients

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

In a process for the production of coated capsules by coacervation, the core material and a coacervate solution of the wall-forming polymer are dispersed as minute entities in an agitated liquid vehicle, the solubility of the wall-forming polymer decreasing with increasing temperature, and the system is heated above the gel point of the wall-forming polymer to harden the walls deposited about the entities of core material. In order to produce phase separation to effect an emergence of a coacervate phase of the wall-forming polymer a complementary polymer may be added to the system. Separation of the capsules from the liquid vehicle is carried out at the elevated temperature, unless agents are added to the system to accelerate the hardening process, in which case separation can be carried out after recooling. In the one form a coacervate solution of the wall-forming polymer is formed separately from the liquid vehicle in which it is insoluble, and the system is made up by combining the component phases and agitating and heating as required. Incomplete systems, lacking one or more component, may be stored for future use. In cases where the liquid vehicle is used as the solvent for the wall-forming polymer coacervation may be induced by, in conjunction with the property of decreasing solubility at elevated temperature, changing conditions such as microion concentration. Examples of wall-forming polymers having the requisite solubility properties are methyl cellulose, polyvinylmethyl ether, and ethylhydroxyethyl cellulose. Suitable complementary polymers to assist in formation of a coacervate solution of methyl cellulose include dextran, hydroxypropyldextran, polyvinyl alcohol or polyvinylpyrrolidone. The method is particularly suited to the coating of core materials which are insoluble in the liquid vehicle, including chloroform, chlorinated biphenyl, kerosene, acetylated monoglyceride, lemon oil, menthol, aspirin, resins, pigments and dies. In particular examples described, aqueous dextran solution is used to facilitate coacervation of methyl cellulose aqueous wall-forming solution when various materials are coated, agitation and heating to 50-60 DEG C. producing the required particle size and encapsulation. An example of a wall-hardening agent is a mixture of aqueous sorbitol solution; mono-and di-glycerides of fat forming fatty acids, and an aqueous solution of tannic acid.ALSO:In a process for the production of coated capsules of, for example, aspirin, by coacervation, the core material and a coacervate solution of the wall-forming polymer are dispersed as minute entities in an agitated liquid vehicle, the solubility of the wall-forming polymer decreasing with increasing temperature, and the system is heated above the gel point of the wall-forming polymer to harden the walls deposited about the entities of core material. In order to produce phase separation to effect an emergence of a coacervate phase of the wall-forming polymer a complementary polymer may be added to the system. Separation of the capsules from the liquid vehicle is carried out at the elevated temperature, unless agents are added to the system to accelerate the hardening process, in which case separation can be carried out after recooling. In the one form a coacervate solution of the wall-forming polymer is formed separately from the liquid vehicle in which it is insoluble, and the system is made up by combining the component phases and agitating and heating as required. Incomplete systems, lacking one or more component, may be stored for future use. In cases where the liquid vehicle is used as the solvent for the wall-forming polymer coacervation may be induced by, in conjunction with the property of decreasing solubility at elevated temperature, changing conditions such as microion concentration. Examples of wallforming polymers having the requisite solubility properties are methyl cellulose, polyvinylmethyl ether, and ethylhydroxyethyl cellulose. Suitable complementary polymers to assist in formation of a coacervate solution of methyl cellulose include dextran, hydroxypropyldextran, polyvinyl alcohol or polyvinylpyrrolidone. The method is particularly suited to the coating of core materials which are insoluble in the liquid vehicle.
GB4819165A 1964-11-23 1965-11-12 Method of manufacturing minute capsules Expired GB1071170A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US41334864A 1964-11-23 1964-11-23

Publications (1)

Publication Number Publication Date
GB1071170A true GB1071170A (en) 1967-06-07

Family

ID=23636893

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4819165A Expired GB1071170A (en) 1964-11-23 1965-11-12 Method of manufacturing minute capsules

Country Status (10)

Country Link
AT (1) AT262937B (en)
BE (1) BE672621A (en)
CH (1) CH458294A (en)
DE (1) DE1283191B (en)
DK (1) DK109893C (en)
FR (1) FR1453745A (en)
GB (1) GB1071170A (en)
NL (1) NL6515181A (en)
NO (1) NO123781B (en)
SE (1) SE303733B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0232512A3 (en) * 1985-12-13 1989-06-14 E.I. Du Pont De Nemours And Company Encapsulated pigment in silver halide wash-off film
WO2003105786A3 (en) * 2002-06-14 2004-06-03 Firmenich & Cie Non-crystalline perfume or flavour delivery system

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5515681A (en) * 1978-07-21 1980-02-02 Kuraray Co Ltd Production of microcapsule

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0232512A3 (en) * 1985-12-13 1989-06-14 E.I. Du Pont De Nemours And Company Encapsulated pigment in silver halide wash-off film
WO2003105786A3 (en) * 2002-06-14 2004-06-03 Firmenich & Cie Non-crystalline perfume or flavour delivery system
CN1327823C (en) * 2002-06-14 2007-07-25 弗门尼舍有限公司 Non-crystalline perfume or flavour delivery system

Also Published As

Publication number Publication date
CH458294A (en) 1968-06-30
BE672621A (en) 1966-04-01
SE303733B (en) 1968-09-09
FR1453745A (en) 1966-06-03
AT262937B (en) 1968-07-10
DK109893C (en) 1968-07-29
NL6515181A (en) 1966-05-24
NO123781B (en) 1972-01-17
DE1283191B (en) 1968-11-21

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