Pigment encapsulated latex aqueous colorant dispersions

Claim 2

A process for producing a colorant comprising a stable aqueous suspension of submicron sized particles of polymer encapsulated active ingredient, wherein a polymer matrix surrounds a core of solid active ingredient, said process comprising the steps of: A. Mixing together an organic solvent, a polymer soluble in said solvent but substantially insoluble in water and an active ingredient which substantially is insoluble in water to form a homogeneous mixture, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said active ingredient has dispersed in said solvent without appreciable agglomeration; and B. Adding said solvent/polymer/active ingredient mixture to water, in a concentration range of 1.0% to 50.0%, by weight, and dispersing until an emulsion results wherein solvent/polymer/active ingredient comprises a discontinuous phase, having a size less than 4 microns with water as the continuous phase, werein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm.; and C. Removing substantially all of said solvent to define an aqueous suspension of said particles.

Claim 3

The process according to claim 1, wherein, in said mixing step, the polymer is soluble to less than 5 percent, in water, and the solvent is soluble to less than 20% in water.

Claim 4

The process according to claim 2, wherein, in said mixing step, the active ingredient comprises solid primary elements having an element average diameter range of between 0.01 to 1.0 microns, and at least one primary element is encapsulated as a core within each polymer matrix wherein, further, the concentration ratio, by weight, of polymer to encapsulated material for each submicron sized particle is between 0.1 and 10.0, and each particle density is controlled by the pigment to polymer ratio.

Claim 5

The process according to claim 2, wherein said dispersing step further comprises the addition of a surfactant, in the range between 0.1 percent and 20 percent, by weight, of active ingredient material, and the concentration ratio, by weight, of polymer to encapsulated active material for each particle is between 0.1 and 10.0.

Claim 6

The process according to claim 2, wherein, in said mixing step, the concentration, by weight, of active material to solvent is between 1.0 percent and 20 percent, said polymer has a viscosity of less than 200 centipoise when dissolved in said solvent and said dispersing step is done ultrasonically, until substantially each droplet of discontinuous phase comprises a submicron sized polymer matrix encapsulating active material as a solid core.

Claim 7

The process of claim 2 wherein said polymer is a system of epoxy resin and a curing agent, said dispersing step conditions are created by a surfactant that is cationic, and said curing agent migrates through the aqueous suspension to cure the surface of each dispersed polymer particle.

Claim 8

The process of claim 6 wherein said solvent removal step further comprises applying heat to cure said polymer and remove some or all of the water of said aqueous suspension.

Claim 9

The process according to claim 2 wherein, in said mixing step, said polymer is selected from the group consisting of polyvinyl butyral, vinyl acetal polymers, butyrals, styrene/maleic anhydride copolymers, and alkylated vinylpyrrolidone copolymers.

Claim 10

The process according to claim 2 wherein, in said mixing step, the polymer has a viscosity of less than 200 centipoise when dissolved in a solvent which is selected from the group consisting of ethyl acetate, methyl isobutyl ketone, methylene chloride, and tetrachlorethylene.

Claim 11

The process according to claim 4, wherein said surfactant is selected from the group consisting of quaternary ammonium salts, ethoxylated alkyl phenols, ethoxylated alcohols, ethoxylated fatty esters, sulfosuccinate derivatives, alkyl aryl sulfonates, sorbitan derivatives and lecithin.

Claim 12

A process for producing a writing fluid comprising a low viscosity aqueous suspension of submicron sized particles of polymer encapsulated pigment, wherein a polymer matrix surrounds a solid core of pigment, said process comprising the steps of: A. Mixing together an organic solvent, a film-forming polymer soluble in said solvent but substantially insoluble in water and a pigment comprising submicron sized primary particles, which substantially are insoluble in water, to form a homogeneous mixture, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said pigment has been dispersed homogeneously as primary particles in said solvent without appreciable agglomeration; and B. Adding said solvent/polymer/pigment mixture to water, in a concentration range of 1.0% to 50.0%, by weight, and dispersing until an emulsion results wherein solvent/polymer/pigment droplets with an average diameter less than 2 microns comprise a discontinuous phase in water as the continuous phase, wherein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm., and substantially each droplet of discontinuous phase has one or more primary pigment particles therein; and C. Removing substantially all of said solvent to define an aqueous suspension of submicron-sized particles of pigment with smooth outer polymer surfaces.

Claim 13

A process for producing a writing fluid comprising a low viscosity aqueous suspension of submicron sized particles of polymer encapsulated pigment, wherein a polymer matrix surrounds a solid core of pigment, said process comprising the steps of: A. Mixing together an organic solvent, a film-forming polymer soluble in said solvent but substantially insoluble in water and a pigment comprising submicron sized primary particles, which substantially are insoluble in water, to form a homogeneous mixture, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said pigment has been dispersed homogeneously as primary particles in said solvent without appreciable agglomeration; and B. Adding said solvent/polymer/pigment mixture to water, in a concentration range of 1.0% to 50.0%, by weight, and dispersing until an emulsion results wherein solvent/polymer/pigment droplets with an average diameter less than 2 microns comprise a discontinuous phase in water as the continuous phase, wherein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm., and substantially each droplet of discontinuous phase has one or more primary pigment particles therein; and C. Removing substantially all of said solvent to define an aqueous suspension of submicron-sized particles of pigment with smooth outer polymer surfaces.

Claim 14

The process according to claim 11, wherein, in said mixing step, the polymer is soluble to less than 5 percent, in water, the solvent is soluble to less than 20% in water, and the amounts of polymer/pigment in said mixing step have a combined average density of approximately 1.0 gram/c.c.; wherein further the concentrations of polymer and pigment are chosen so that substantially all of said pigment remains in the discontinuous liquid phase, during said dispersing step.

Claim 15

The process according to claim 12, wherein, in said mixing step, the pigment comprises solid primary elements having an element average diameter range of between 0.01 and 1.0 microns, substantially one primary element is encapsulated as a core within each polymer matrix wherein, further, the concentration ratio, by weight, of polymer to encapsulated pigment for each resulting particle is between 0.1 and 10.0, and each particle further has a density in the range of 0.9 to 1.1 grams/c.c.

Claim 16

The process according to claim 12, wherein said dispersing step further comprises the addition of a surfactant, in the range between 0.1 percent and 20 percent, by weight, of active ingredient material, and the concentration ratio, by weight, of polymer to encapsulated pigment for each resulting particle is between 0.1 and 10.0.

Claim 17

The process according to claim 12, wherein, in said mixing step, the concentration, by weight, of pigment to solvent is between 1.0 percent and 20 percent, said polymer has a viscosity of less than 200 centipoise when dissolved in said solvent and said dispersing step is done ultrasonically, until substantially each discontinuous phase droplet average diameter is below 2 microns in size and comprises a solvent/polymer matrix encapsulating pigment as a solid core.

Claim 18

The process according to claim 14 wherein, in said mixing step, said film-forming polymer is of a concentration and molecular weight to have a viscosity of less than 200 centipoise when dissolved in a solvent selected from the group consisting of ethyl acetate, methyl isobutyl ketone and methylene chloride.

Claim 19

The process according to claim 16, wherein, said surfactant is selected from the group consisting of quaternary ammonium salts, ethoxylated alkyl phenols, ethoxylated alcohols, ethoxylated fatty esters, sulfosuccinate derivatives, alkyl aryl sulfonates, and sorbitan derivatives.

Claim 20

A writing fluid made according to the process of claim 17.

Claim 21

A process for creating a textile colorant which comprises creating a polymer matrix that surrounds a core of solid colorant, said process comprising the steps of: A. Mixing together an organic solvent, a polymer soluble in said solvent but substantially insoluble in water and colorant primary particles, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said colorant has been dispersed as primary particles in said solvent without appreciable agglomeration; and B. Adding said solvent/polymer/colorant mixture to water, in a concentration range of 1.0% to 50.0% by weight, and dispersing until an emulsion results wherein solvent/polymer/colorant comprises a discontinuous droplet phase in water as the continuous phase, wherein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm. and is continued until a stable emulsion of droplets less than 2 microns average diameter results; and C. Removing substantially all of said solvent to define encapsulated colorant particles that are adapted to be formed as a film upon a textile surface and then set by application of heat sufficient to raise the polymer encapsulation above its glass transition temperature.

Claim 22

A process for creating a textile colorant which comprises creating a polymer matrix that surrounds a core of solid colorant, said process comprising the steps of: A. Mixing together an organic solvent, a polymer soluble in said solvent but substantially insoluble in water and colorant primary particles, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said colorant has been dispersed as primary particles in said solvent without appreciable agglomeration; and B. Adding said solvent/polymer/colorant mixture to water, in a concentration range of 1.0% to 50.0% by weight, and dispersing until an emulsion results wherein solvent/polymer/colorant comprises a discontinuous droplet phase in water as the continuous phase, wherein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm. and is continued until a stable emulsion of droplets less than 2 microns average diameter results; and C. Removing substantially all of said solvent to define encapsulated colorant particles that are adapted to be formed as a film upon a textile surface and then set by application of heat sufficient to raise the polymer encapsulation above its glass transition temperature.

Claim 23

The process according to claim 19, wherein, in said mixing step, the polymer is soluble to less than 5 percent, in water, the solvent is soluble to less than 20% in water, and the amounts of polymer/colorant in said mixing step having a combined average density of approximately 1.0 gram/c.c., and said carrier fluid comprises water remaining after said solvent removal step.

Claim 24

The process according to claim 19, wherein, in said mixing step, the colorant comprises solid primary elements having an element average diameter range of between 0.01 and 1.0 microns and said dispersing is done with sufficient energy to disperse substantially one primary element as a core within a submicron sized polymer/solvent matrix wherein, further, the concentration ratio, by weight, of polymer to colorant for each resulting submicron sized encapsulated particle is between 0.1 and 10.0, and each particle density is controlled by the pigment to polymer ratio employed.

Claim 25

The process according to claim 19, wherein said polymer is thermoplastic and less than 5 percent soluble in water, and said dispersing step further comprises the addition of a surfactant, in the range between 0.1 percent and 20 percent, by weight, of colorant, and the concentration ratio, by weight, of polymer to encapsulated colorant for each submicron sized particle is between 0.1 and 10.0.

Claim 26

The process according to claim 19, wherein, in said mixing step, the concentration, by weight, of colorant to solvent is between 1.0 percent and 20 percent, said polymer has a viscosity of less than 200 centipoise when dissolved in said solvent and said dispersing step is done ultrasonically, until substantially each discontinuous phase droplet is less than 2 microns in average diameter and comprises a solvent/polymer matrix encapsulating colorant as a solid core.

Claim 27

The process according to claim 19 wherein said polymer is a thermosetting system of epoxy resin which requires a curing agent, said dispersing step comprises adding a cationic surfactant, and said curing agent is added in a continuous aqueous phase, in order to contact the dispersed polymer particle surfaces, whereby upon applying heat to particles that have been applied to a textile surface, the particles will thermoset upon said textile surface.

Claim 28

The process according to claim 24 wherein a cationic surfactant is used in said dispersing step and a water soluble curing agent is applied to said particles from a separate bath, after said particles have been applied to a substrate.

Claim 29

A textile colorant made by the process of claim 23.

Claim 30

A textile colorant made by the process of claim 24.

Claim 31

A process for encapsulating submicron sized pigment particles for use in cosmetics, wherein a polymer matrix surrounds a solid pigment particle and the resulting particles are in an aqueous suspension, said process comprising the steps of: A. Mixing together an organic solvent, a polymer soluble in said solvent but substantially insoluble in water and a pigment which substantially is insoluble in water to form a homogeneous mixture, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said active ingredient has dispersed homogeneously in said solvent, without appreciable agglomeration; and B. Adding said solvent/polymer/pigment mixture, in a concentration range of 1.0% to 50.0%, by weight, to water which contains a nonionic surfactant and dispersing until an emulsion results wherein solvent/polymer/pigment droplets with an average diameter less than 5 microns comprise a discontinuous phase in water as the continuous phase, wherein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm.; and C. Removing substantially all of said solvents to define an aqueous mixture comprising encapsulated pigment in suspension; and D. Concentrating the encapsulated colorant to a desired concentration for admixture with a cosmetic carrier fluid.

Claim 32

A process for encapsulating submicron sized pigment particles for use in cosmetics, wherein a polymer matrix surrounds a solid pigment particle and the resulting particles are in an aqueous suspension, said process comprising the steps of: A. Mixing together an organic solvent, a polymer soluble in said solvent but substantially insoluble in water and a pigment which substantially is insoluble in water to form a homogeneous mixture, wherein said solvent is characterized by a vapor pressure higher than water and said mixing is continued until said active ingredient has dispersed homogeneously in said solvent, without appreciable agglomeration; and B. Adding said solvent/polymer/pigment mixture, in a concentration range of 1.0% to 50.0%, by weight, to water which contains a nonionic surfactant and dispersing until an emulsion results wherein solvent/polymer/pigment droplets with an average diameter less than 5 microns comprise a discontinuous phase in water as the continuous phase, wherein said dispersing step is done under conditions where interfacial tension between the organic solvent and the water is less than approximately 10 dynes/cm.; and C. Removing substantially all of said solvents to define an aqueous mixture comprising encapsulated pigment in suspension; and D. Concentrating the encapsulated colorant to a desired concentration for admixture with a cosmetic carrier fluid.

Claim 33

The process according to claim 28 wherein said pigment comprises a metal oxide with an average primary particle size that is submicron, said polymer is soluble to less than 5 percent, in water, and said solvent is soluble to less than 20 percent in water.

Claim 34

The process according to claim 29 wherein said solvent is selected from the group consisting of methylene chloride and ethyl acetate, and said pigment is selected from the group consisting of oxides of iron, and pigments approved for cosmetic use.

Claim 35

The process according to claim 30 wherein said cosmetic carrier comprises the aqueous phase resulting from said solvent removal step, said polymer is non-film forming, said solvent is selected from the group consisting of methylene chloride and ethyl acetate, and said aqueous mixture comprises a dispersion of submicron polymer particles containing one or more primary pigment particles and non-pigmented polymer particles.

Claim 36

The process according to claim 29 wherein said polymer is film-forming, said solvent is selected from the group consisting of ethyl acetate and methylene chloride, and said aqueous mixture comprises a dispersion of submicron polymer particles containing one or more primary pigment particles, unencapsulated pigment and non-pigmented polymer particles.

Claim 37

A cosmetic made according to the process of claim 31.

Claim 38

A cosmetic made according to the process of claim 32.