USRE28361E - Polymer pigmentation - Google Patents

Polymer pigmentation Download PDF

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USRE28361E
USRE28361E US37178073A USRE28361E US RE28361 E USRE28361 E US RE28361E US 37178073 A US37178073 A US 37178073A US RE28361 E USRE28361 E US RE28361E
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pigment
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/22After-treatment of expandable particles; Forming foamed products
    • C08J9/224Surface treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING, DISPERSING
    • B01F15/00Accessories for mixers ; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F15/00123Controlling; Testing; Measuring
    • B01F15/00331Controlling; Testing; Measuring characterized by the parameter being controlled
    • B01F15/00363Controlling speed during the operation
    • B01F15/00376Controlling the speed of the mixing device during the operation
    • B01F15/00383Controlling the linear speed of the tip of a moving stirrer during the operation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/002Methods
    • B29B7/005Methods for mixing in batches
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/88Adding charges, i.e. additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/203Solid polymers with solid and/or liquid additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/04Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L55/00Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
    • C08L55/02ABS [Acrylonitrile-Butadiene-Styrene] polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/10Polymers of propylene
    • B29K2023/12PP, i.e. polypropylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS
    • B29K2033/00Use of polymers of unsaturated acids or derivatives thereof as moulding material
    • B29K2033/04Polymers of esters
    • B29K2033/08Polymers of acrylic acid esters, e.g. PMA, i.e. polymethylacrylate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS
    • B29K2033/00Use of polymers of unsaturated acids or derivatives thereof as moulding material
    • B29K2033/04Polymers of esters
    • B29K2033/12Polymers of methacrylic acid esters, e.g. PMMA, i.e. polymethylmethacrylate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0032Pigments, colouring agents or opacifiyng agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE, IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/25Solid
    • B29K2105/251Particles, powder, granules
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2982Particulate matter [e.g., sphere, flake, etc.]
    • Y10T428/2991Coated
    • Y10T428/2998Coated including synthetic resin or polymer

Abstract

1. PIGMENTED POLYMER PARTICLES, SAID POLYMER PARTICLES HAVING A PIGMENT ABRASIVELY ADHERED TO THE SURFACES THEREOF BY MIXING THE POLYMER PARTICLES AND DRY POWDERED PIGMENT IN A ROTARY BLADE MIXER HAVING A TIP SPEED EXCEEDING ABOUT 200 INCHES PER SECOND, SAID POLYMER PARTICLES HAVING A SCREEN MESH SIZE OF ABOUT 20 TO 200 U.S. STANDARD SIEVE AND BEING SELECTED FROM THE GROUP CONSISTING OF POLYETHYLENE, POLYPROPYLENE, POLYMERIZED LOWER ALKYL ESTER OF ACRYLIC ACID IN WHICH THE LOWER ALKYL ESTER GROUP HAS ONE TO FOUR CARBON ATOMS, AND POLYMERIZED LOWER ALKYL ESTER OF METHACRYLIC ACID IN WHICH THE LOWER ALKYL ESTER GROUP HAS ONE TO FOUR CARBON ATOMS.

Description

United States Patent Re. 28,361 Reissued Mar. 11, 1975 28,361 POLYMER PlGMENTATlON Granville I. Hahn, Big Spring, Tex., assignor to Cosden Oil & Chemical Company, Big Spring, Tex.

No Drawing. Original No. 3,632,369, dated Jan. 4, 1972,

Ser. No. 884,353, Dec. 11, 1969, which is a continuation-in-part of applications Ser. No. 525,854, Feb. 8, 1966, Ser. No. 576,208, Aug. 31, 1966, both now abandoned, and Ser. No. 594,998, Nov. 17, 1966, now Patent No. 3,484,262. Application for reissue June 20, 1973, Ser. No. 371,780

Int. Cl. Bc 5/00; B44d 1/02 U.S. Cl. 117-16 13 Claims Matter enclosed in heavy brackets appears in the original patent but forms no part of this reissue specification; matter printed in italics indicates the additions made by reissue.

ABSTRACT OF THE DISCLOSURE Particles of polyethylene, polypropylene, polyacrylic lower alkyl ester, and polymethacrylic lower alkyl esters are pigmented by progressively mixing the dry particles with dry pigment in a high speed mixer having a blade tip speed exceeding about 200 inches per second for a short period of a few minutes or less, whereby all of the pigment becomes firmly adhered to the surfaces of the polymer particles.

This invention is a continuation in part of my copending application Ser. No. 525,854, filed Feb. 8, 1966, and now abandoned, Ser. No. 576,208, filed Aug. 31, 1966, now abandoned, and Ser. No. 594,998, filed Nov. 17, 1966, and now U.S. Pat. 3,484,262 issued December 16, 1969, and relates to abrasively adhered dry pigment upon polymer particles.

This invention specifically relates to abrasion-adhered dry pigment upon polymer particles and the method of making such particles.

More particularly, the abrasion-adhered dry particles are usually powder formed by grinding (1) polyethylene pellets; (2) polypropylene pellets; (3) polyacrylic lower alkyl ester pellets; and (4) polymethacrylic lower alkyl ester, the lower alkyl being one to four carbon atoms, usually methyl.

The term particles" as used herein refers preferably to ground pieces, but is broad enough to include ground shapes, beads and powder. The term particles" as used here may have a large screen mesh size ranging upward from about mesh sometimes to as high as about 5 mesh,

U.S. Standard sieve. Preferably the colored particles of the present invention is powder, having a screen mesh size in the range of about 200 to 20 U.S. Standard sieve.

The pigment hereof is any dry powdered coloring or pigmentin'g material insoluble in the polymer particles to be co l ored. Such pigment is usually colored inorganic salts or metallo organic compounds and may be elementary metal powder or metal oxides per se.

According to the present invention I have found that a markedly improved colored polymer particle as defined above is formed by abrasively or intensively mixing the polymer particles with pigment in a dry stage such as by a high-speed rotating blade mixer; for example, a Prodex- Henschel, preferably having a rotational tip speed exceeding about 200 inches per second and ranging upward practically as high as 500 to 1500 inches per second. At such blade speeds the moving surfaces of the blade abrasively rubs the powdered pigment into the surface of the polymer particles, such as beads, powder or rounded pellets, causing a surprisingly firm surface adhesion therebetween. This high intensity abrasive mixing breaks up flocs of colored pigment and transfers the same as very fine pigment particles, evenly distributed over the surface of the beads, powder, or rounded pellets as a relatively strongly-adhered coating on the surfaces and also held in the surface pores or irregularities microscopically occurring upon the particles.

The abrasive, high-intensity mixing procedure hereof docs not need to be applied for unduly long periods of time. For small mixers operating with small quantities, even less than a minute, such as fifteen to thirty seconds, can effect a substantial adhesion of the pigment upon the polymer particles. For lower intensity abrasive forces applied in the dry mixing, the adhesion etiect becomes a ailable in a somewhat more poorly adhered state by abrasively mixing for longer periods of time. The abrasive adhesion method hereof is in substantial contrast to mere dusting and tumbling of powdered pigment upon powder or to application of liquid compositions to effect the pigmentation according to prior proposals.

The present procedure produces a surprisingly unique product in that the pigment becomes relatively firmly adhered to the particle surfaces, rubbing off only with great difficulty, and only substantial abrasive rubbing against wet surfaces allows removal of any empirically significant quantity of the pigment once adhered by this method.

Great advantages attend the present abrasive mixing method. There is greatly reduced dusting of pigment per se. Such dust as appears in the final product is usually substantially the very fine pigmented bead per se. The procedure is available to give a more homogeneous color mixed in the desired proportions as set in the mixing to allow accurate reproduction of the color desired. The procedure allows formation of a masterbatch of color as a commercial product which can be blended back by the molder to the color needed in the molding by simple admixture of colorless beads to reduce the color intensity from the masterbatch. Surprisingly, the pigment upon the abrasively-colored particles hereof does not transfer from the colored surfaces to other particles; for instance, white particles that may have been mixed with a pro-colored batch of particles do not become colored. The colored particles hereof remain stably colortd with a surprising non-transferable color from the pigmented particles to the unpigmented particle, remaining as a heterogeneous salt-and-pepper mix. Some pigments in varying degrees affect the physical properties of the plastic particles and molded products thereof, rendering it in some cases more flexible.

An outstanding advantage of the present method is that in a short period of intensive abrasive mixing of small particles, a finished pigmented product is available for molding. The product is homogeneous and the color is firmly adhered. The pigment is stably adhered and will not rub off. The colored particles are filled into a mold to give asuperior reproducible color to the final molded product without intermediate steps of pelleting, etc., as presently widely practiced.

While, as stated, the larger particles such as pellets can be abrasively coated, the larger pelleted particles have a much reduced surface area and, consequently, cannot secure the pigment in so firm a bond to its surface as smaller'particles; nor do the larger pelleted particles present a large enough surface to allow the pigment to be distributed as evenly thereover. Consequently, the larger pellets give a somewhat poorer distribution of pigment and adhesion of pigment to the surfaces thereof.

The present invention provides in the art a true, much simplified solid-state dry coloring process for dry polymer particles which permits the manufacture of an easily-reproduced colored polymer molding particle, usable often for high quality end products having superior physical properties.

In accordance with the present invention, an improved colored polymer particle product and method is provided for making colored polymer particles. This method includes the abrasive high-intensity mixing of pigment and small solid particles of polymer material. The conditions of mixing are such that the intensity is sufficient to break down agglomerates of pigment, while [abraiding] abrading the pigment and forcing it to adhere to the particles so that substantial dusting will not occur in subsequent handling.

Preferably the intensity of mixing applied by the present method is sufficient to cause the discrete particles of pigment to enter surface regions of the polymer particles. To accomplish this purpose, the intensity of mixing is kept high while the size of pigment utilized is limited to comparatively small pigment, i.e., on the order of about one micron or less.

Mixing is preferably accomplished with a rotating blade-type mixer in which a linear velocity on the outer part of the blades at least as high as 200 inches per second, and usually about 500 to 1,500 inches per second, is achieved.

The product provided by the present invention is particles of polymer material having pigment tightly adhered to its surface portions only, the adherence appearing to involve the entrapment of pigment within surface depressions or indentures in the outer regions of the particle and may be a factor to account for the low dusting, strong pigment adhesion of this product.

The preferred dried, colored particles provided by the present invention are powders of polyethylene, polypropylene, polyacrylic lower alkyl esters and polymethacrylic lower alkyl ester, the lower alkyl being one to four carbon atoms.

While various processes may be utilized for obtaining a suitable polymer for practice of the present invention, a typical process involves grinding pelleted polymer using a conventional knife type grinder. In such process a pelleted polymer is typically one-sixteenth to one-fourth of an inch in size and may be reduced in a series of grinding steps or in one step such that the particle size of the resulting powder is in the range of 200 to 20 US. Slandard sieve. Thereafter the resulting powder is mixed with pigment in the abrasive high intensity mixing conditions described. Other particles or powders may be obtained by means such as the suspension polymerization of monomers wherein the resulting hard bead polymer is approximately 200 to 20 US. Standard sieve. In such a suspension process the monomer may be stirred in water in a heated reaction vessel accompanied by various suspension agents until such time as a hard polymer particle results. Thereafter these polymer particles may be recovered and dried.

The polymer particles are loaded into a high intensity mixer together with a suitable quantity of pigment. The individual pigment particle size is preferably comparatively small, often no larger than on the order of about one micron. It is understood that these particles may exist in agglomerates, wherein several individual particles are clustered together; however, the abrasive mixing reduces and distributes such clusters or fiocs as individual particles evenly over the surfaces of the polymer particles. Accordingly, individual pigment crystals or particles are driven abrasively in the course of the mixing into surface depressions in the polymer spheroid particles and remain firmly adhered therein. In the case of the polymer particles referred to, a certain amount of pore or depression structure adjacent the surface is already present to accommodate, or assist in accommodating the entrance of pigment particles into surface regions of the polymer particles. However, it is observed that the high-intensity mixing of the discrete pigment particles apparently causes the pigment to force its way into surface structure of the polymer particle even in instances when surface depressions are not of suflicient size or number to originally accommodate the pigment.

While it is not desired to be limited by theory, it appears that the high-intensity mixing drives or forces the pigment into the surface of the polymer particle. In some instances, it appears that the site of entrance of the pigment is scratched out or otherwise made by the [abraiding] abradiug action of the pigment itself.

It should be pointed out that the high-intensity mixing step is sufiicient to accomplish two purposes: the agglomerates of pigment characteristic of prior art solidstate coloring methods are broken up; and an adherence of pigment to the bead or similar particle of polymer matcrial is obtained. This degree of adherence will vary over wide limits, and although the words "adhere" or adherence" are seen to be relative, they are taken herein to refer to a sufficient degree of adherence such that pigment will not rub off materially on the hands during the course of handling particles of polymer material which have been abrasively dry or solid-state mixed.

The adherence obtained is less in the case of the comparatively larger pigments which may be mixed in accordance with the present invention, such as ultramarine blue, phthalocyanine green or cadmium orange having particles of the order of about 1 micron up to 2 to 3 microns and better with smaller sized pigments such as white pigment (titanium dioxide), typically about 0.2 percent of a micron and carbon black even smaller.

To illustrate, high-intensity mixing may be conducted on a batch of beads with a cadmium orange pigment. The batch of colored polymer beads so obtained is set aside and a fresh batch of heads is mixed under conditions of high-intensity with rutile titanium dioxide pigment to obtain a white bead. The two batches are then loaded into the high-intensity mixer in which they were originally colored and mixing is conducted in accordance with the same schedule of speed and time. Surprisingly, the product obtained is only a mixture of discrete orange and white polymer beads. There is substantially no transfer of color from the one bead batch to the other bead batch, even after a long period of high-intensity mixing.

To further illustrate, a batch of white polyethylene particles may be prepared by the high-intensity mixing of a polyethylene powder, with titanium dioxide pigment of about 0.2 micron particle size. On mixing, a good whitecolored product is obtained. Therefore, a batch of polyethylene powder of the same nature employed in the white batch is mixed with carbon black pigment of a particle size on the order of about 20 millimicrons. The resulting [produce] product is a well-colored black polyethylene powder batch. The two batches are thereafter combined in the same type high-intensity mixing equipment in which they were originally colored. After mixing together under high-intensity conditions for a period of time substantially greater than was required for the initial coloring, it is observed that there is little or no transfer of the colors between the powders. Accordingly, the end product appears much as salt and pepper which has been shaken well together, with each retaining its own individual color characteristics.

The same experiment was repeated using polypropylene powder. As before, a portion of these powders were pigmented with titanium dioxide and another portion with carbon black. Each portion was well colored and their admixture, despite further agitation, showed no transfer of color from one powder to another.

By way of contrast, phthalocyanine green pigment may be dispersed throughout a batch of similar polymer particles under high-intensity mixing conditions. The end product may be set aside and subsequently mixed with a white, orange or black-colored product obtained by highintensity mixing as described above. It is observed that the phthalocyanine green transfers slightly in the mixing process to the white, orange or black particle, as the case may be.

The character and extent of mixing will vary somewhat, usually ranging from about fifteen seconds to one hour;

typically, fifteen seconds to ten minutes at top speeds from 500 to 1,500 inches per second, in order to be of sufficiently high intensity to abrasively mix the color and powder and fulfill objectives of the present invention.

Whether the pigment be a comparatively small one, as

preferred, or a large one, the product of high-intensity mixing may be fed to a molding device such as an injection molding machine. Molded articles of quite high quality faithfully colored to specifications are obtained.

The colored particles obtained from the high-intensity mixing step may be extruded or otherwise processed as desired to obtain an intermediate or an end product. When contrasted to colored polyethylene products obtained by prior art technology, it is found that the present product has superior characeristics.

Various high-intensity mixers may be used. Typically these involve a rotating shaft which carries a transversely extending blade member or members such as an impeller turbine or the like. Preferably the mixing blade or blades are capable of achieving a linear tip velocity, as stated, of at least about 200 inches per second, and preferably about $00 to 1,500 inches per second. Exemplary of equipment which is satisfactory is the Papenmeier mixer, obtainable from Welding Engineers Inc., Norristown, Pa., as illustrated, and the Prodex-Henschel mixer illustrated in us. Pat. No. 2,945,634, mentioned above.

Preferably the mixer combines the principle of moving the particles being mixed both locally and in gross. That is to say, it is designed to turn over the material well in order that all the material in the mixer will, in due course, be within the region of high shear supplied by the rapidly moving mixer blades. The mixer of US. Pat. No. 2,945,- 634 provides vertical mixing at high shear rates and, accordingly, accomplishes the objectives of both high shear local mixing and good movement in gross.

The mixer blade or rotor may operate at a variety of angular velocities, but it is important that a substantial peripheral speed be developed. For example, such commercial mixer with a pitched blade and having a radius of about /3 foot, may develop a speed on the order of about 720 inches per second at its blade tips, and can accomplish mixing of a batch of particles and small pigment aggregating about 2,000 grams in quantity in around 30 seconds. With some pigment, as little as 15 seconds will suffice, while in other instances a few minutes mixing will be desirable.

The following specific examples are offered by way of further illustration of the practice of the present invention and are not intended to be taken as limiting except to the extent that is specifically expressed in any given example.

EXAMPLE I Polyethylene polymer particles are dry colored in accordance with the present invention by high-intensity mixing of the powder with a light red pigment, specifically [CdS-CdSe-EaSOJ CdS-CdSe-BaSO The polyethylene polymer powder is prepared by grinding polyethylene pellets. The powder size ranges from about 20 mesh to about 200 mesh, with about 100 mesh being average. 11.35 grams of the light red pigment described above are added to a Papenmeier mixer along with the 2,270 grams of the polyethylene polymer particles and are blended therein for about 30 seconds at 1,800 r.p.m. Peripheral speed of the rotor ran on the order of about 720 inches per second. A thermocouple disposed clear of the mixer blades and into the body of the powder indicates a temperature of 80" F. was the maximum achieved during the course of mixing. At the end of the blending period, the powder was examined and found to be strongly adherently colored a light red. The color was uniformly dispersed. Upon examination under the microscope, it was found that the pigment had entered depressions in the surface of the particles and that there is a distinct distribution of color particles on the surface of the powder particles between the various sites of pigment embedded in surface regions of the powder particles. As examined by the naked eye, the powder appears to be quite thoroughly covered with pigment. The pigment-impregnated powder can be rubbed about in the hands, but the pigment does not rub off.

The colored powder of this example is used in various end product molding applications including injection molding, vacuum forming, and sheet extrusion. No intermediate compounding steps are used. A high-quality molded end product is obtained which possesses superior physical and color characteristics.

EXAMPLE II The procedure of example I is repeated with a like quantity of polypropylene powder of the same nature. However, a yellow pigment is used, specifically 11.35 grams of CdS-BaSO The powder is colored the desired yellow, with the pigment well adhered in surface regions of the polymer particles. Microscopic examination at 500 powder indicated that the pigment is actually embedded or entrapped within depressions in the polymer particle surface, as was observed in the prior example.

End products formed from the beads of this examnln are high quality, as was the casein Example I.

EXAMPLE III The procedure of example I is repeated using the same quantity of polyethylene particles, but with 4.5 grams of ultramarine blue and a mixing time of about 2 minutes. The resulting particles are firmly and nontransferably colored blue, possessing about the same good physical and color characteristics as in the preceding example. Microscopic examination at 500 power indicates that at least a part of the pigment is actually embedded in surface irregularities as well as being evenly distributed over regions of the particle surfaces. When mixing time for the ultramarine blue particle mix is reduced to only 30 seconds, the resulting product appears to carry well-dispersed pigment, but application of hard hand rubbing abrasion will rub off some of the pigment. End products formed from the powder of this example are, however, of high, easily reproduced color quality. This is true even if the comparatively short mixing time of 30 seconds is employed instead of the two minutes first referred to in this example. The result of the shorter mixing time is not found to he in product quality, but rather only in the tendency of the resulting colored powder to evidence slight dusting.

EXAMPLE IV The procedure of example I is repeated except that 2 grams of phthalocyanine green pigment are substituted for the pigment therein used and a 10 minute mixing time is employed. The particles obtained are well colored with a similar slight dusting as in example III. Even after 10 minutes of high-intensity mixing, a small amount of the pigment rubs off on the hands.

EXAMPLE [IV] V The procedure of example I is repeated, except that 11.5 grams of a finely pulverized mica carrying titanium dioxide on its surface, as the pigment, is used. The end products obtained by this example are of a metallic pearl color and possess good physical and color characteristics.

EXAMPLE VI The procedure of example I is repeated except that to the polymer particles is addecl45.4 grams of rutile titanium dioxide pigment. The pigment is found to be quite well adhered to the polymer particles. Microscopic examination at 500 power revealed that the pigment is embedded or entrapped in depressions in the polymer surace. Good results are achieved on molding end products vithout intermediate compounding steps.

EXAMPLE VII Example I is repeated but, for the pigment therein emllOyCd, there is substituted 2.4 grams of a yellow pigment specifically [CdS-CdS-BaSo] CdS-Ba-S'o 4.2 grams if light red pigment (specifically CdS-CdSe-BaSOJ, and 2.4 grams of carbon black. The three pigments and polyner particles are mixed to obtain well colored brown polyner having the pigment firmly adhered to the polymer. )n molding, high quality product of desired brown color formed from this powder.

EXAMPLES VIIIXIV The foregoing examples are repeated except that polynethyl methacrylate is utilized as the polymer material. t is found that comparable results are obtained in all nstances.

EXAMPLE XV EXAMPLE XVI Example I is repeated, using 4.5 grams of carbon black pigment size ranging from about 0.007 to 0.045 [mi- :rons] micron). The polymer particles have the pigment vell adhered and form high-quality end products of a uality black color.

EXAMPLE XVII High-density polyethylene is extruded as in example (VIH, below, and similar spheroidal particles are obained. 0.05 percent of ultramarine blue is added to the |olyethylene particles and abrasively adhered. The pigment is firmly attached as in example XVIII.

EXAMPLE XVIII Low-density polyethylene is extruded through a conentional extruder and the emerging strands are cut hot lirectly at the die face such as to obtain pellets that are pheroidal in appearance and about one-sixteenth to oneighth inch in size. These particles are colored by abraive agitation using 0.05 percent of ultramarine blue. The esulting particles have the ultramarine blue firmly atached and only by severe rubbing can the pigment be emoved.

EXAMPLE XIX Polypropylene is extruded such as to obtain a one- :ixteenth-hot-cut particle of approximately one-sixteenth nch size. To these particles are added 0.05 percent of a ight red pigment, specifically CdS-CdSeBaS0,,. The paricles are mixed, using abrasive agitation such that the ight red pigment firmly adheres as in example I.

EXAMPLE XX Poly methyl methacrylate particles averaging 30 mesh .n size are mixed with a yellow pigment, specifically ZdS-BaSO such as to obtain a 0.1 percent concentra- '.ion of pigment. The mixture is then subjected to abrailVB agitation as in example I. On completion, the color .s found to have adhered firmly to the beads and cannot be removed except by severe rubbing.

From the foregoing description and examples, it will be appreciated that a process for making high-quality, colored polyethylene particles has been provided. Moreover, it will be understood that quality polymer end products may be made from such particles. Further, a stable color adherent particle of polymer material that will not dust nor rub off easily has been disclosed.

Having described the invention in connection with certain specific embodiments thereof, it is to be understood that further modifications may now suggest themselves to those skilled in the art, and it is intended to cover such modifications as fall within the scope and the claims appended hereto.

What is claimed is:

1. Pigmented polymer particles, said polymer particles having a pigment abrasively adhered to the surfaces thereof by mixing the polymer particles and dry powdered pigment in a rotary blade mixer having a tip speed exceeding about 200 inches per second, said polymer particles having a screen mesh size of about 20 to 200 U.S. Standard sieve and being selected from the group consisting of polyethylene, polypropylene, polymerized lower alkyl ester of acrylic acid in which the lower alkyl ester group has one to four carbon atoms, and polymerized lower alkyl ester of methacrylic acid in which the lower alkyl ester group has one to four carbon atoms.

2. Pigmented polymer particles as defined in claim 1 wherein the particles are rounded polyethylene pellets.

3. Pigmented polymer particles as defined in claim 1 wherein the particles are rounded polypropylene pellets.

4. Pigmented polymer particles as defined in claim 1 wherein the particles are rounded polymerized lower alkyl ester of acrylic acid pellets, the lower alkyl ester group having one to four carbon atoms.

5. Pigmented polymer particles as defined in claim 1 wherein the particles are rounded polymethylacrylate pellets.

6. Pigmented polymer particles as defined in claim 1 wherein the particles are rounded polymerized lower alkyl ester of methacrylic acid pellets, the lower alkyl having one to four carbon atoms.

7. Pigmented polymer particles as defined in claim 1 wherein the particles are rounded polymethy-l methacrylate pellets.

8. Pigmented polymer particles as defined in claim 1 wherein the pigment is a dry powdered pigment substance insoluble in said polymer.

9. Pigmented polymer particles as defined in claim 1 wherein the pigment is carbon black.

10. Pigmented polymer particles as defined in claim 1 wherein the pigment is titanium dioxide.

11. Pigmented polymer powder comprising dry powdered particles of polymer having a screen mesh size up to about 200 U.S. Standard sieve and dry powdered pigment abrasively adhered together by mixing the dry powdered polymer and dry powdered pigment in a high speed rotary blade mixer having a tip speed exceeding about 200 inches per second for a time period in the range of 15 seconds up to about 10 minutes.

12. Pigmented polymer powder comprising dry powdered particles of polymer having a screen mesh size up to about 200 U.S. Standard sieve and dry powdered pigment abrasively adhered together by mixing the dry powdered polymer and dry powdered pigment in a high speed rotary blade mixer having a tip speed exceeding about 200 inches per second.

13. The powdered pigmented polymer product as defined in claim 12 wherein the polymer is selected from the group consisting of polyethylene, polypropylene, polymerized lower alkyl ester of acrylic acid in which the lower alkyl ester group has I to 4 carbon atoms, and polymerized lower alkyl ester of methacrylic acid in which the lower alkyl ester group has I to 4 carbon atoms.

(References on following page) patent.

References Cited The following references, cited by the Examiner, are of record in the patented file of this patent or the original UNITED STATES PATENTS Sommer 117-100 Sommer 117-100 Louis 117-100 Beck et a1 241-98 Simpson 260-40 Dyer 260-455 Zweigle 260-25 Nagle 117-100 Eichorn 117-100 Bernot 117-100 Jordan 117-100 Hahn 117-100 Carton 260-41 R Ballentine et a1 117-109 Kessler 117-109 Carton 260-41 R 5/1963 Erchak 117-100 9/1963 Shannon 117-100 10/1964 McMillan 117-100 5/1965 Resnick 117-100 7/1965 Seymour 117-100 2/1966 Sapiego 117-100 4/1966 Beaulieu 117-100 12/1966 Raymond 117-100 1/1967 Ferrigno 117-100 1/1968 Bonitz 117-100 2/1968 Voris 117-100 FOREIGN PATENTS 7/1970 Australia 117-100 WILLIAM D. MARTIN, Primary Examiner D. C. KONOPACKI, Assistant Examiner US. Cl. X.R.

117-100 C, 138.8 E, 138.8 F

Claims (1)

1. PIGMENTED POLYMER PARTICLES, SAID POLYMER PARTICLES HAVING A PIGMENT ABRASIVELY ADHERED TO THE SURFACES THEREOF BY MIXING THE POLYMER PARTICLES AND DRY POWDERED PIGMENT IN A ROTARY BLADE MIXER HAVING A TIP SPEED EXCEEDING ABOUT 200 INCHES PER SECOND, SAID POLYMER PARTICLES HAVING A SCREEN MESH SIZE OF ABOUT 20 TO 200 U.S. STANDARD SIEVE AND BEING SELECTED FROM THE GROUP CONSISTING OF POLYETHYLENE, POLYPROPYLENE, POLYMERIZED LOWER ALKYL ESTER OF ACRYLIC ACID IN WHICH THE LOWER ALKYL ESTER GROUP HAS ONE TO FOUR CARBON ATOMS, AND POLYMERIZED LOWER ALKYL ESTER OF METHACRYLIC ACID IN WHICH THE LOWER ALKYL ESTER GROUP HAS ONE TO FOUR CARBON ATOMS.
USRE28361E 1966-02-08 1973-06-20 Polymer pigmentation Expired USRE28361E (en)

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US5319001A (en) * 1988-12-02 1994-06-07 Courtaulds Coating (Holdings) United Colored powder coating compositions
US5470893A (en) * 1990-06-01 1995-11-28 Courtaulds Coatings (Holdings) Limited Powder coating compositions
US5527877A (en) * 1992-11-23 1996-06-18 Dtm Corporation Sinterable semi-crystalline powder and near-fully dense article formed therewith
US5536576A (en) * 1993-05-21 1996-07-16 Iwao Hishida Colored, thermoplastic resin pellets
US5648450A (en) * 1992-11-23 1997-07-15 Dtm Corporation Sinterable semi-crystalline powder and near-fully dense article formed therein
US5856378A (en) * 1988-12-02 1999-01-05 Courtaulds Coatings (Holdings) Limited Powder coating compositions
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US6576732B1 (en) 2000-11-28 2003-06-10 Conocophillips Co. Drag-reducing polymers and drag-reducing polymer suspensions and solutions
US6649670B1 (en) 2002-12-17 2003-11-18 Baker Hughes Incorporated Continuous neat polymerization and ambient grinding methods of polyolefin drag reducing agents
US6765053B2 (en) 2000-11-28 2004-07-20 Conocophillips Company Drag-reducing polymer suspensions
US20050182155A1 (en) * 2004-02-13 2005-08-18 O'dell William G. Novel powder coloring system
US6946500B2 (en) 2002-12-17 2005-09-20 Baker Hughes Incorporated Non-cryogenic process for grinding polyolefin drag reducing agents
USRE39354E1 (en) 1992-11-23 2006-10-17 3D Systems, Inc. Sinterable semi-crystalline powder and near-fully dense article formed therewith
US20090158963A1 (en) * 2005-10-21 2009-06-25 Valspar Sourcing, Inc. Novel Powder Coloring System
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US6649670B1 (en) 2002-12-17 2003-11-18 Baker Hughes Incorporated Continuous neat polymerization and ambient grinding methods of polyolefin drag reducing agents
US20050182155A1 (en) * 2004-02-13 2005-08-18 O'dell William G. Novel powder coloring system
US7867555B2 (en) 2004-02-13 2011-01-11 Valspar Sourcing Inc. Dispersion-coated powder coloring system
US20090158963A1 (en) * 2005-10-21 2009-06-25 Valspar Sourcing, Inc. Novel Powder Coloring System
US9156996B2 (en) * 2005-10-21 2015-10-13 Valspar Sourcing, Inc. Powder coloring system
US9528007B2 (en) 2005-10-21 2016-12-27 Valspar Sourcing, Inc. Powder coloring system
US20110064940A1 (en) * 2009-09-14 2011-03-17 The Regents Of The University Of Michigan Dispersion method for particles in nanocomposites and method of forming nanocomposites
US9902819B2 (en) * 2009-09-14 2018-02-27 The Regents Of The University Of Michigan Dispersion method for particles in nanocomposites and method of forming nanocomposites

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