US4087376A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Capsule manufacture
Assignee: WTA Inc
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Filing: 1976-12-30
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Granted: 1978-05-02
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Expires: 1996-12-30
Abstract
Abstract A process is disclosed for performing encapsulation, en masse, by an in situ polymerization reaction to yield capsule wall material. The polymerization includes a reaction between urea and formaldehyde or polycondensation of monomeric or low molecular weight polymers of dimethylol urea or methylated dimethylol urea in an aqueous vehicle and the reaction is conducted in the presence of negatively-charged, carboxyl-substituted, linear aliphatic hydrocarbon polyelectrolyte material dissolved in the vehicle. Liquid-liquid phase separation is accomplished and maintained by increase in the molecular weight of the resulting condensation polymer without further dilution of the manufacturing vehicle. The negatively-charged polyelectrolyte material is required and has an apparent effect of controlling or modifying the polymerization reaction. The disclosed encapsulation process permits manufacture of microcapsules in concentrations of capsule to capsule manufacturing vehicle higher than previously possible.
Inventors
- 👤 Peter L. Foris
- 👤 Robert W. Brown
- 👤 Paul S. Phillips, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 01:26
CPC Classifications
B; B01; B01J; B01J13/00; B01J13/02; B01J13/06; B01J13/14; B01J13/18; Y; Y10; Y10S; Y10S428/00; Y10S428/914; Y10T; Y10T428/00; Y10T428/29; Y10T428/2982; Y10T428/2984; Y10T428/2985; Y10T428/2987; Y10T428/2989
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
172 words
A process for manufacturing minute capsules, en masse in an aqueous manufacturing vehicle, comprising the steps of: (a) establishing an agitating aqueous system including monomeric dimethylol urea or methylated dimethylol urea, or a low molecular weight polymer thereof, about 0.75 to about 15 percent by weight, based on the weight of aqueous manufacturing vehicle, of a system modifier material selected from the group consisting of poly(ethylene-co-maleic anhydride), poly(methyl vinyl ether-co-maleic anhydride), poly(acrylic acid), poly(propylene-co-maleic anhydride), poly(isobutylene-co-maleic anhydride), poly(butadiene-co-maleic anhydride), and poly(vinyl acetate-co-maleic anhydride) and particles of an intended capsule core material substantially insoluble in the system, in which agitating system the modifier material is present prior to the addition of said particles, and (b) polycondensing said dimethylol urea or methylated dimethylol urea to form a condensation polymer resulting in (i) liquid-liquid phase separation of the resulting condensation polymer above a molecular weight to be soluble in the system and (ii) continued polycondensation of the separated polymerization product to give solid capsule wall material individually surrounding particles of the dispersed intended capsule core.
Claim 2
Dependent Claim
172 words
A process for manufacturing minute capsules, en masse in an aqueous manufacturing vehicle, comprising the steps of: (a) establishing an agitating aqueous system including monomeric dimethylol urea or methylated dimethylol urea, or a low molecular weight polymer thereof, about 0.75 to about 15 percent by weight, based on the weight of aqueous manufacturing vehicle, of a system modifier material selected from the group consisting of poly(ethylene-co-maleic anhydride), poly(methyl vinyl ether-co-maleic anhydride), poly(acrylic acid), poly(propylene-co-maleic anhydride), poly(isobutylene-co-maleic anhydride), poly(butadiene-co-maleic anhydride), and poly(vinyl acetate-co-maleic anhydride) and particles of an intended capsule core material substantially insoluble in the system, in which agitating system the modifier material is present prior to the addition of said particles, and (b) polycondensing said dimethylol urea or methylated dimethylol urea to form a condensation polymer resulting in (i) liquid-liquid phase separation of the resulting condensation polymer above a molecular weight to be soluble in the system and (ii) continued polycondensation of the separated polymerization product to give solid capsule wall material individually surrounding particles of the dispersed intended capsule core.
Claim 3
Dependent Claim
18 words
The process of claim 1, wherein the polycondensation reaction is effected while continuing to agitate the aqueous system.
Claim 4
Dependent Claim
45 words
The process of claim 1, wherein the poly(ethylene-co-maleic anhydride) has a molecular weight of greater than about 1000, the poly(vinyl methyl ether-co-maleic anhydride) has a molecular weight of greater than about 250,000 and the poly(acrylic acid) has a molecular weight of greater than about 20,000.
Claim 5
Dependent Claim
20 words
The process of claim 1, wherein the aqueous manufacturing vehicle is less than 60 percent, by volume, of the system.
Claim 6
Dependent Claim
20 words
The process of claim 1, wherein the aqueous manufacturing vehicle is less than 50 percent, by volume, of the system.
Claim 7
Dependent Claim
24 words
The process of claim 1, wherein the aqueous system includes an additive compound selected from the group consisting of resorcinol, orcinol and gallic acid.
Claim 8
Dependent Claim
36 words
The process of claim 6, wherein said additive compound is present in the system in an amount of 5 to 30 percent, by weight, of the combined urea in the dimethylol urea or methylated dimethylol urea.
Claim 9
Dependent Claim
22 words
The process of claim 1, wherein the pH of the aqueous manufacturing vehicle is maintained between 3 and 7 through step (b).
Claim 10
Dependent Claim
29 words
The process of claim 1, wherein the dimethylol urea or methylated dimethylol urea is added to an agitating aqueous system comprising said modifier material and said capsule core material.
Claim 11
Dependent Claim
164 words
A process for manufacturing minute capsules, en masse, in an aqueous manufacturing vehicle, comprising the steps of: (a) establishing an agitating single-phase aqueous solution system including monomeric dimethylol urea or methylated dimethylol urea, or a low molecular weight polymer thereof, and about 0.75 to about 15 percent by weight, based on the weight of aqueous manfacturing vehicle, of a system modifier material selected from the group consisting of poly(ethylene-co-maleic anhydride), poly(methyl vinyl ether-co-maleic anhydride), poly(acrylic acid), poly(propylene-co-maleic anhydride), poly(isobutylene-co-maleic anhydride), poly-(butadiene-co-maleic anhydride) and poly(vinyl acetate-co-maleic anhydride), (b) dispersing into the solution system particles of an intended capsule core material substantially insoluble in the system, and (c) polycondensing said dimethylol urea or methylated dimethylol urea to form a condensation polymer resulting in (i) liquid-liquid phase separation of the resulting condensation polymer above a molecular weight to be soluble in the system and (ii) continued polycondensation of the separated polymerization product to give solid capsule wall material individually surrounding particles of the dispersed intended capsule core.
Claim 12
Dependent Claim
164 words
A process for manufacturing minute capsules, en masse, in an aqueous manufacturing vehicle, comprising the steps of: (a) establishing an agitating single-phase aqueous solution system including monomeric dimethylol urea or methylated dimethylol urea, or a low molecular weight polymer thereof, and about 0.75 to about 15 percent by weight, based on the weight of aqueous manfacturing vehicle, of a system modifier material selected from the group consisting of poly(ethylene-co-maleic anhydride), poly(methyl vinyl ether-co-maleic anhydride), poly(acrylic acid), poly(propylene-co-maleic anhydride), poly(isobutylene-co-maleic anhydride), poly-(butadiene-co-maleic anhydride) and poly(vinyl acetate-co-maleic anhydride), (b) dispersing into the solution system particles of an intended capsule core material substantially insoluble in the system, and (c) polycondensing said dimethylol urea or methylated dimethylol urea to form a condensation polymer resulting in (i) liquid-liquid phase separation of the resulting condensation polymer above a molecular weight to be soluble in the system and (ii) continued polycondensation of the separated polymerization product to give solid capsule wall material individually surrounding particles of the dispersed intended capsule core.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-05-01 | 1981-10-31 | 1982-05-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-05-01 | 1985-10-31 | 1986-05-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-05-01 | 1989-10-31 | 1990-05-02 | $7700.00 | Window Closed / Lapsed |