EP0749371A1 - Mikrokapseldispersion - Google Patents
MikrokapseldispersionInfo
- Publication number
- EP0749371A1 EP0749371A1 EP95909752A EP95909752A EP0749371A1 EP 0749371 A1 EP0749371 A1 EP 0749371A1 EP 95909752 A EP95909752 A EP 95909752A EP 95909752 A EP95909752 A EP 95909752A EP 0749371 A1 EP0749371 A1 EP 0749371A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- oil
- room temperature
- solid
- weight
- liquid
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41M—PRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
- B41M5/00—Duplicating or marking methods; Sheet materials for use therein
- B41M5/124—Duplicating 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
- B41M5/165—Duplicating 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
- B41M5/1655—Solvents
Definitions
- the present invention relates to a microcapsule dispersion for producing pressure-sensitive recording papers, in which the core solvent contained in the microcapsules is a dye precursor or a
- Microcapsule dispersions of the type mentioned at the outset and their use have been known for a long time.
- Essentially two different types of capsule wall-forming materials are used, namely water-soluble capsule wall-forming materials, such as. B. pig skin gelatin, gum arabic and water-insoluble, such as. B. polyisocyanate as one of the components used for the production of polyurea capsules.
- the microcapsule dispersions are also spacers, for. B. starch granules or cellulose fibers and a suitable binder for fixing the microcapsules on the paper surface.
- a large number of proposals are known from the known prior art which relate to suitable solvents or oils and their mixtures for taking up the color precursor compounds. For the sake of simplicity, this microcapsule component is referred to below as the core solvent.
- diphenylalkanes alkyl-substituted diphenylalkanes, diphenylalkenes and / or alkyl-substituted diphenylalkenes are known as liquid core solvents for dye precursors.
- the addition of these diluents is intended to change the physical properties, such as the viscosity and the vapor pressure, with the aim of better manageability or for process reasons.
- DE-A-26 40 197 relates to a preparation for dissolving dye formers for pressure-sensitive copying systems in which the color acceptors consist of acidic resins.
- a mixture of partially hydrogenated terphenyl and alkylbenzene components which is liquid at room temperature is used, optionally with up to about 3 parts of diluent for each part of solvent can be moved.
- Liquid mineral oils or vegetable oils, but also coconut oil solid at room temperature, are mentioned as diluents.
- EP-A-0 262 569 provides as the core solvent a composition which consists of at least 80% by weight of vegetable, animal or paraffin oil, a dye precursor based on a triphenylmethane leuco dye being used and the wall material of the microcapsules being water-soluble or prior to microcapsule formation is water dispersible.
- EP-A-0 520 639 also provides a core solvent which contains a vegetable oil for a microcapsule to be used for the production of pressure-sensitive recording paper.
- a core solvent which contains a vegetable oil for a microcapsule to be used for the production of pressure-sensitive recording paper.
- an ester component of a non-aromatic monocarboxylic acid with a saturated or unsaturated straight or branched hydrocarbon chain with at least 3 carbon atoms in the chain is also provided in this composition.
- EP-A-0 573 210 proposes a core solvent which does not contain the aforementioned ester component, the as Vegetable oil provided for the core solvent has a softening range of approximately 20 to 25 degrees and consists at least for the most part of a vegetable oil that is solid or semi-solid in this temperature range.
- this proposal is not free from disadvantages.
- polyisocyanate as a component to be used for the production of polyurea capsules, is soluble or at least excellently dispersible in vegetable oils which are solid or semi-solid at room temperature, and is therefore at the same time suitable for the organic solvents previously required to dissolve this component, such as. B. isopropylnaphthalene, can be dispensed with.
- solid or semi-solid core solvent mixtures in a temperature range close to room temperature can lead to production disturbances in the production of capsules from polyurea.
- the object of the invention is to provide a
- microcapsule dispersion which, because of the core solvent components used, enables problem-free capsule production. At the same time, only oils of vegetal origin should be used predominantly.
- Another task is to provide a microcapsule with high tightness, for which purpose polyurea is to be used as the capsule wall material which has proven itself in this regard.
- the invention therefore provides a microcapsule dispersion which can be used for the production of pressure-sensitive recording papers and in which the core solvent contained in the microcapsules is a dye precursor or a
- - rest a vegetable oil which is solid or semi-solid at room temperature
- the core solvent is liquid at room temperature
- the capsule wall material consists of polyurea.
- room temperature used in the description and in the claims means that the core solvent is liquid above 20 ° C.
- liquid means: flowable.
- paraffin oil specified in the description and claims of the present application are naphthenic or paraffin-based mineral oil products, e.g. B. white oil and spindle oil to understand. Chlorine paraffin, which has already been proposed several times as the core solvent, is not encompassed by the present invention.
- liquid paraffin oil In order to establish a liquid state in the core solvent, smaller quantities of paraffin oil are sufficient than of liquid vegetable oil.
- liquid paraffin oil is used as the sole additive to a core solvent, which consists of solid or semi-solid vegetable oil Amounts of at least 10% by weight are required, preferably not more than 20% by weight. When using liquid vegetable oils, the minimum amount added is more than 25% by weight and can be up to 60% by weight. Mixtures of liquid paraffin oil with liquid vegetable oil on the one hand and solid or semi-solid vegetable oil on the other hand are also possible; an amount of paraffin oil below 10% by weight can also be used here, but then higher amounts of liquid vegetable oil than this sole use of liquid paraffin oil would have to be added.
- the core solvent consists of 80 to 90% by weight of a vegetable oil which is solid or semi-solid at room temperature, the rest: a paraffin oil which is liquid at room temperature.
- a preferred core solvent mixture consisting of only vegetable oils consists of 60 to 70% by weight of a vegetable oil that is solid or semi-solid at room temperature, while the rest consists of a vegetable oil that is liquid at room temperature.
- coconut oil, palm oil and palm kernel oil or mixtures of these oils are preferred as solid or semi-solid vegetable oils. Rapeseed oil, sunflower oil, cottonseed oil, olive oil, corn oil, safflower oil or a mixture of these oils are preferred as vegetable oils which are liquid at room temperature.
- a color precursor mixture which contains 2-phenyl-4- (4-diethylaminophenyl) -4- (4-methoxyphenyl) -6-methyl-7-dimethylamino-4H-benz.3.1-oxazine as color former.
- Such a color former mixture has good solubility in the core solvent mixtures provided according to the invention, while on the other hand a high efficiency of the microcapsule dispersion according to the invention is also ensured.
- the core solvent contained in the microcapsules does not solidify at temperatures of more than 18 ° C.
- a microcapsule dispersion In a mixture of 90 parts by weight of coconut oil (Cocopur from Rau) and 10 parts by weight of paraffin oil (white oil P 1020 from Parafluid) is a dye precursor mixture consisting of 60 parts by weight. Share 2-phenyl-4- (4-diethylaminophenyl) -4- (4-methoxyphenyl) -6-methyl-7-dimethylamino-4H-benz .3.1-oxazine (baymicron SN 2601 from BAYER, see also claim 7 of the EP A-0 573 210), 20 parts by weight of a fluorine-based dye precursor and 20 parts by weight of CVL so that a
- Dye concentration of 6% is present in the core solvent.
- 71 g of diisocyanate are added to 447 g of the color image mixture produced, and 992 g of a 1% strength polyvinyl alcohol solution (as an emulsifying aid) in demineralized water are subsequently added.
- the mixture produced is transferred to the storage vessel of a pilot encapsulation plant.
- the dispersion head of the dispersion unit which is connected to a cooling device by a pipeline, is then filled and the dispersion is initiated. After the water-cooled cooling device has been passed through, part of the liquid leaves the dispersing unit via a throttle disc and is guided to a separate stirring vessel, while another part of the liquid is fed again to the dispersing head in the circuit.
- a 5.4% solution of diethylenetriamine (DET) in demineralized water and, if necessary, defoamer are added to the separate stirred vessel.
- the temperature set in the separate mixing vessel is 25 ° C.
- Capsules with an average size of 5.1 ⁇ m are formed. 8.6% of the capsules were> 10 ⁇ m in size.
- Dye precursor mixture as stated above, but with an oil mixture in which the white oil content was 20 parts by weight, a microcapsule dispersion was produced under the same process conditions, giving an average grain size of 5.9 ⁇ m and 15.8% of the microcapsules were> 10 ⁇ m.
- the dye precursor mixture described for Examples 1 and 2 was used and a dye concentration of 6% was set in the core solvents given below.
- the microcapsules were produced as indicated for Examples 1 and 2, and the microcapsules produced were used to produce CFB sheets on a wood-free, mass-coated coating base paper of 42 g / m 2 , which already had a CF layer on one side was provided, in which the color acceptors consisted of acidic clays, applied to the side opposite the CF layer while setting a coat weight of 6 g / m 2 .
- the coating color also contained ground cellulose as a spacer and butadiene styrene latex as a binder.
- the microcapsule dispersion was applied using a doctor blade. Composition of the core solvents:
- This test is used to check capsule stability when exposed to different pressures.
- Test result role test
- CFB sheets according to comparative example and examples 3 and 4 are stored for 12 days at 70 ° C. and 75% relative atmospheric humidity in the dark.
- the aged samples are combined with a standard CF sheet and labeled.
- the image intensity is then determined in comparison to an unaged sample. The result is shown in the table below.
- the child aging described under 3 of the present test report essentially corresponds to the "accelerated aging" given on page 7, lines 15 ff.
- EP-A-0 573 210 With the difference that according to EP-A -0 573 210 the CF discoloration of the CFB sheet and not the loss of writing power is assessed.
Landscapes
- Color Printing (AREA)
- Manufacturing Of Micro-Capsules (AREA)
- Heat Sensitive Colour Forming Recording (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SI9530201T SI0749371T1 (en) | 1994-03-09 | 1995-02-21 | Dispersion of microcapsules |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4407813 | 1994-03-09 | ||
DE4407813A DE4407813C1 (de) | 1994-03-09 | 1994-03-09 | Mikrokapseldispersion |
PCT/EP1995/000613 WO1995024318A1 (de) | 1994-03-09 | 1995-02-21 | Mikrokapseldispersion |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0749371A1 true EP0749371A1 (de) | 1996-12-27 |
EP0749371B1 EP0749371B1 (de) | 1998-12-02 |
Family
ID=6512238
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP95909752A Expired - Lifetime EP0749371B1 (de) | 1994-03-09 | 1995-02-21 | Mikrokapseldispersion |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0749371B1 (de) |
CZ (1) | CZ285796B6 (de) |
DE (2) | DE4407813C1 (de) |
ES (1) | ES2127512T3 (de) |
WO (1) | WO1995024318A1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE50306215D1 (de) | 2002-09-20 | 2007-02-15 | Koehler August Papierfab | Verfahren zum einkapseln gel ster farbreaktionspartner von f arbreaktionssystemen, die danach erh ltlichen kapseln sowie deren verwendung in farbreaktionspapieren |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE790321A (fr) * | 1971-10-20 | 1973-04-19 | Monsanto Co | Solvants pour colorants de materiaux d'enregistrement sensiblesa la pression |
US3968301A (en) * | 1972-02-11 | 1976-07-06 | Monsanto Company | Pressure-sensitive record material and dye solvents therefor |
DE3039117A1 (de) * | 1980-10-16 | 1982-05-13 | Bayer Ag, 5090 Leverkusen | Verfahren zur herstellung von mikrokapseln |
JPS61188184A (ja) * | 1985-02-14 | 1986-08-21 | Kanzaki Paper Mfg Co Ltd | 感圧複写紙 |
JPS63262281A (ja) * | 1987-04-20 | 1988-10-28 | Fuji Photo Film Co Ltd | 感圧複写用マイクロカプセルシ−ト |
DE4212827A1 (de) * | 1991-04-19 | 1992-10-22 | Kanzaki Paper Mfg Co Ltd | Mikrokapsel-tintenzusammensetzung |
DE69321765T3 (de) * | 1992-06-04 | 2006-08-24 | Arjo Wiggins Ltd., Basingstoke | Druckempfindliches Aufzeichnungsmaterial |
-
1994
- 1994-03-09 DE DE4407813A patent/DE4407813C1/de not_active Expired - Fee Related
-
1995
- 1995-02-21 ES ES95909752T patent/ES2127512T3/es not_active Expired - Lifetime
- 1995-02-21 EP EP95909752A patent/EP0749371B1/de not_active Expired - Lifetime
- 1995-02-21 CZ CZ962582A patent/CZ285796B6/cs not_active IP Right Cessation
- 1995-02-21 WO PCT/EP1995/000613 patent/WO1995024318A1/de active IP Right Grant
- 1995-02-21 DE DE59504421T patent/DE59504421D1/de not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
See references of WO9524318A1 * |
Also Published As
Publication number | Publication date |
---|---|
DE4407813C1 (de) | 1995-10-26 |
WO1995024318A1 (de) | 1995-09-14 |
CZ285796B6 (cs) | 1999-11-17 |
CZ258296A3 (en) | 1997-03-12 |
EP0749371B1 (de) | 1998-12-02 |
ES2127512T3 (es) | 1999-04-16 |
DE59504421D1 (de) | 1999-01-14 |
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