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Method of preparing coated pigment particles and the product produced thereby

Assignee: Individual
•
Filing: 1978-03-22
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Granted: 1979-11-06
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Expires: 1998-03-22
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Abstract

Abstract A method of preparing coated pigment particles for dry compounding with a polymeric material such as plastic or rubber, which method comprises the steps of providing particles of a hydrophilic color pigment, mixing the pigment particles with a wax having a given melting point temperature and a brittle condition below a given lower temperature, heating the mixture above a process temperature substantially above the melting temperature and substantially above the boiling point of water to boil away entrapped water, subjecting the mixture to high shear mixing while at the process temperature, cooling the mixture to a temperature below the given lower temperature to produce a solid mass, and, then, breaking the solid mass into flakes.

Inventors

  • 👤 Edward T. Pollard

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 21:59
CPC Classifications
C; C09; C09C; C09C3/00; C09C3/08; C08; C08K; C08K9/00; C08K9/10; C09B; C09B67/00; C09B67/0071; C09B67/0092; C01; C01P; C01P2004/00; C01P2004/20; C01P2004/60; C01P2004/61; C01P2004/62; C01P2004/80; C01P2006/00; C01P2006/60; C01P2006/80; C01P2006/82; C01P2006/90; Y; Y10; Y10T; Y10T428/00; Y10T428/29; Y10T428/2982; Y10T428/2989

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 280 words
A method of preparing colorant flakes comprised of hydrophilic color pigment particles embedded in a wax matrix for dry compounding with a polymeric material, said method comprising the steps of: (a) providing particles of said color pigment dispersed in a presscake having a given moisture content, said particles having a size ranging from about 0.1 micron to about 100 microns; (b) before dehydration of said presscake, mixing said particles with particles of a hydroxystearate wax which has a melting point temperature and is brittle below a selected lower temperature substantially below 212° F. while simultaneously heating the formed admixture to a processing temperature substantially above 212° F., by discharging said pigment particles and wax particles into the nip region of a pair of rotating rolls heated to said processing temperature, to simultaneously boil away any entrapped moisture in said pigment particles and melt the said wax to encapsulate the said pigment particles and form said particle admixture into a molten wax-pigment particle mixture; (c) passing and compressing said mixture while at said processing temperature between said rolls in the nip thereof while they are rotated at differing angular velocities to compress and subject said mixture to high shear forces acting to effect further mixing of said pigment particles with and produce substantially uniform dispersion thereof in the said melted wax while simultaneously expelling residual moisture from said pigment particles; (d) cooling said mixture to a temperature which renders said mixture a brittle, easily breakable solid mass by passing said mixture over and in contact with a surface having a temperature below said selected lower temperature; and, (e) then, scraping said solid mass off said surface to break it into flakes.
Claim 2
Independent Claim 280 words
A method of preparing colorant flakes comprised of hydrophilic color pigment particles embedded in a wax matrix for dry compounding with a polymeric material, said method comprising the steps of: (a) providing particles of said color pigment dispersed in a presscake having a given moisture content, said particles having a size ranging from about 0.1 micron to about 100 microns; (b) before dehydration of said presscake, mixing said particles with particles of a hydroxystearate wax which has a melting point temperature and is brittle below a selected lower temperature substantially below 212° F. while simultaneously heating the formed admixture to a processing temperature substantially above 212° F., by discharging said pigment particles and wax particles into the nip region of a pair of rotating rolls heated to said processing temperature, to simultaneously boil away any entrapped moisture in said pigment particles and melt the said wax to encapsulate the said pigment particles and form said particle admixture into a molten wax-pigment particle mixture; (c) passing and compressing said mixture while at said processing temperature between said rolls in the nip thereof while they are rotated at differing angular velocities to compress and subject said mixture to high shear forces acting to effect further mixing of said pigment particles with and produce substantially uniform dispersion thereof in the said melted wax while simultaneously expelling residual moisture from said pigment particles; (d) cooling said mixture to a temperature which renders said mixture a brittle, easily breakable solid mass by passing said mixture over and in contact with a surface having a temperature below said selected lower temperature; and, (e) then, scraping said solid mass off said surface to break it into flakes.
Claim 3
Dependent Claim 29 words
The method as defined in claim 1 wherein said wax is selected from the class consisting of: glyceryl-tris-12-hydroxystearate, methylhydroxystearate, propylene glycol mono-hydroxystearate, glyceryl mono-hydroxystearate, ethylene glycol mono-hydroxystearate and stearyl-12-hydroxystearate.
Claim 4
Dependent Claim 23 words
A composition formed from pigment particles which are encapsulated in a hydroxystearate wax, said particles being prepared by the process of claim 1.
Claim 5
Independent Claim 54 words
A method of preparing colorant flakes comprised of hydrophilic color pigment particles embedded in a wax matrix for dry compounding with a polymeric material, said method comprising the steps of: (a) providing particles of said hydrophilic color pigment containing absorbed moisture and having a size ranging from about 0.1 micron to about 100 microns;
Claim 6
Independent Claim 54 words
A method of preparing colorant flakes comprised of hydrophilic color pigment particles embedded in a wax matrix for dry compounding with a polymeric material, said method comprising the steps of: (a) providing particles of said hydrophilic color pigment containing absorbed moisture and having a size ranging from about 0.1 micron to about 100 microns;
Claim 7
Dependent Claim 112 words
(b) providing particles of a wax having a melting point temperature substantially below 212° F. and being mechanically fracturable at approximately room temperature; (c) before dehydrating said moisture containing pigment particles, mixing said pigment particles and wax particles and simultaneously heating the formed admixture in the nip region of a pair of rotating heated rolls at a temperature in the range of 250° F. to 450° F. and rotating at different angular velocities to simultaneously boil away any entrapped moisture in said pigment particles while at the same time melt the said particles of wax to encapsulate the said pigment particles and form said particle admixture into a molten wax-pigment particle mixture;
Claim 8
Dependent Claim 112 words
(b) providing particles of a wax having a melting point temperature substantially below 212° F. and being mechanically fracturable at approximately room temperature; (c) before dehydrating said moisture containing pigment particles, mixing said pigment particles and wax particles and simultaneously heating the formed admixture in the nip region of a pair of rotating heated rolls at a temperature in the range of 250° F. to 450° F. and rotating at different angular velocities to simultaneously boil away any entrapped moisture in said pigment particles while at the same time melt the said particles of wax to encapsulate the said pigment particles and form said particle admixture into a molten wax-pigment particle mixture;
Claim 9
Dependent Claim 143 words
(d) subjecting the said heated mixture to high shear mixing and simultaneous heating by passing and compressing said mixture between the said heated rolls in the nip thereof to reduce the moisture content of said mixture below about 4% by weight and form it into a layer adhering to the faster rotating one of said heated rolls; (e) subjecting the said heated layer mixture on said one roll to additional high shear mixing action and cooling said mixture to a solidified mass at about room temperature by passing and compressing said layer mixture between the said one heated roll and a cooling roll at a temperature lower than the said fracturable temperature of said wax and rotating at an angular velocity faster than said one heated roll; and, (f) mechanically fracturing said solidifed mass into flakes by scraping it off said cooling roll.
Claim 10
Dependent Claim 143 words
(d) subjecting the said heated mixture to high shear mixing and simultaneous heating by passing and compressing said mixture between the said heated rolls in the nip thereof to reduce the moisture content of said mixture below about 4% by weight and form it into a layer adhering to the faster rotating one of said heated rolls; (e) subjecting the said heated layer mixture on said one roll to additional high shear mixing action and cooling said mixture to a solidified mass at about room temperature by passing and compressing said layer mixture between the said one heated roll and a cooling roll at a temperature lower than the said fracturable temperature of said wax and rotating at an angular velocity faster than said one heated roll; and, (f) mechanically fracturing said solidifed mass into flakes by scraping it off said cooling roll.
Claim 11
Dependent Claim 13 words
The method as defined in claim 4 wherein said wax is a hydroxystearate.
Claim 12
Dependent Claim 29 words
The method as defined in claim 4 wherein said wax is selected from the class consisting of: glyceryl-tris-12-hydroxystearate, methylhydroxystearate, propylene glycol mono-hydroxystearate, glyceryl mono-hydroxystearate, ethylene glycol mono-hydroxystearate and stearyl-12-hydroxystearate.
Claim 13
Dependent Claim 23 words
A composition formed from pigment particles which are encapsulated in a hydroxystearate wax, said particles being prepared by the process of claim 4.

References Cited (Backward Citations)

US3546150A Cited
US3728143A Cited
US3773535A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-11-05 1983-05-07 1983-11-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-11-05 1987-05-07 1987-11-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-11-05 1991-05-07 1991-11-06 $7700.00 Window Closed / Lapsed

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