Patent Application
20240198717
The present invention relates to an in-line process for manufacturing paints, more particularly, an in-line mixing process adapted to manufacture a variety of paints continuously or semi-continuously.
Paints sold in retail outlets are typically produced in bulk by a batch process that includes grinding pigment and extender particles to form a solid dispersion, then combining this dispersion in a so-called letdown stage with binder, thickeners, and other additives. The batch process produces paint bases of different concentrations of pigment and extender that are transported to the retail outlet where colorant is added to the paint to meet the demands of the consumer. This base system model of paint production requires substantial inventory and is further disadvantaged by using a fixed amount of TiO2 where the flexibility to adjust TiO2 levels would be desirable. For example, where a colorant requires lower amounts TiO2 than present in the untinted paint to achieve the desired tint, excess colorant would need to be added to balance the excess TiO2. The unnecessary costs associated with the use of excess TiO2 and colorant as well as the additional time required to prepare the final paint are examples of inefficiencies in the base system model that need to be addressed.
An alternative to the base system model is a point-of-sale model where cans of paint are made by concurrent dispensing of binder, pigment, and extender components from separate holding tanks into a paint container, then mixing the contents of the container. (See US 2003/0110101, para [0027] and [0028].) Although this point-of-sale model is an improvement on the base system model, it is still a labor and cost intensive batch process that relies on both the speed of dispensing the materials into a container and the time it takes to mix the materials in the container and to stabilize the viscosity of the final paint.
Accordingly, it would be advantageous to make cans of paint by a more efficient and versatile process.
The present invention addresses a need in the art by providing a process for preparing a container of paint comprising the steps of:
The present invention is a process for preparing a container of paint comprising the steps of:
The process of the present invention provides an efficient and rapid way of making a wide variety of paints.
In a second embodiment of the process of the present invention, the latex from pre-paint storage tank (2) and an aqueous dispersion of a matting agent from storage tank (3) are fed through valves (10) and (9) respectively into mixing chamber (5) and mixed to form an aqueous dispersion of the latex and the matting agent. Pre-paint storage tank (3) further contains a rheology modifier for the matting agent, typically an alkali swellable emulsion (ASE), such as a polyacrylic acid, or a hydrophobically modified alkali swellable emulsion (HASE) or a hydroxyethyl cellulose (HEC). In this embodiment, the ICI builder is advantageously added to mixing chamber (5) from one of additive storage tanks (4).
In a third embodiment of the process of the present invention pre-paints from pre-paint storage tanks (1), (2), and (3) are fed to mixing chamber (5) through valves (11), (10), and (9) and blended to form an aqueous dispersion of opacifying pigment, latex, and matting agent. It is also possible to pre-mix the pre-paints from storage tanks (1) and (2) to form an aqueous dispersion of the opacifying pigment and latex and feed the pre-paint from storage tank (3) further downstream through valve (13) into mixing chamber (5) to form an aqueous dispersion of the opacifying pigment, latex, and matting agent.
In each of the aforementioned embodiments one or more additives such as surfactants, dispersants, defoamers, coalescents, additional thickeners, organic opacifying pigments, block additives, photoinitiators, and solvents may be fed from any or all of additive storage tanks (4) into mixing chamber (5) through any or all of valves (12), (14), and (15). Alternatively, it may be desirable to include one or more of a defoamer, a surfactant, and a coalescent in any of the pre-paints. In a preferred embodiment, a defoamer, a surfactant, and a coalescent in the latex pre-paint.
Colorants are a special class of additives that require special care. For tinted paints, one or more aqueous solutions or dispersions of colorants from colorant addition system (7) is fed into mixing chamber (5) through valve (17), the final paint is formed and then directed into paint container (8). A paint with no opacifying pigment (the second embodiment) requires one or more colorants to form a deep base paint.
Suitable opacifying pigment include inorganic opacifying pigments having a refractive index of greater than 1.90. TiO2 and ZnO are examples of inorganic opacifying pigments, with TiO2 being preferred. Other opacifying pigments include organic opacifying pigments such as opaque polymers. Although an organic opacifying pigment may be used as a substitute for an inorganic opacifying pigment, it is more desirable to use the organic opacifying pigment as a supplement to augment the efficiency of the inorganic opacifying pigment. The organic opacifying pigment can be added to the mixing chamber from a separate additives tank. ROPAQUE™ ULTRA Opaque Polymers and AQACell HIDE 6299 Opaque Polymers are commercial examples of opaque polymers.
The aqueous dispersion of polymer particles (the latex) preferably have a z-average particle size by dynamic light scattering in the range of from 50 nm to 600 nm. Examples of suitable polymeric dispersions include acrylic, styrene-acrylic, urethane, alkyd, vinyl ester (e.g., vinyl acetate and vinyl versatate), and vinyl acetate-ethylene (VAE) polymeric dispersions, and combinations thereof. Acrylic and styrene-acrylic polymeric dispersions typically have a z-average particle size in the range of from 70 nm to 300 nm, while vinyl ester latexes generally have a z-average particle size in the range of from 200 nm to 550 nm as measured using dynamic light scattering. If it is desirable to feed more than one kind of latex into the mixing chamber, the latexes are preferably added from separate latex pre-paint storage tanks.
The latex pre-paint storage tank preferably contains an acrylic latex. As used herein, an “acrylic latex” comprises at least 30 weight percent, preferably at least 50 weight percent, and more preferably at least 80 weight percent structural units of an acrylate and/or methacrylate monomer. Acrylic latexes preferably comprise aqueous dispersions of polymer particles functionalized with methyl methacrylate and one or more acrylates selected from the group consisting of methyl acrylate, ethyl acrylate, n-butyl acrylate, 2-ethylhexyl acrylate, and 2-propylheptyl acrylate. As used herein, the term “structural unit” of a recited monomer refers to the remnant of the monomer after polymerization. For example, a structural unit of n-butyl acrylate is as illustrated:
Structural Unit of n-Butyl Acrylate
where the dotted lines represent the points of attachment of the structural unit to the polymer backbone.
Acrylic latexes also preferably comprise structural units of an acid monomer including carboxylic acid, sulfur acid, and phosphorus acid monomers, as well as salts thereof, and combinations thereof. Examples of suitable carboxylic acid monomers include methacrylic acid, acrylic acid, and itaconic acid and salts thereof; examples of suitable sulfur acid monomers include sulfoethyl methacrylate, sulfopropyl methacrylate, styrene sulfonic acid and salts thereof, vinyl sulfonic acid and salts thereof, and 2-acrylamido-2-methyl propanesulfonic acid and salts thereof; examples of suitable phosphorus acid monomers include phosphonates and dihydrogen phosphate esters of an alcohol in which the alcohol contains or is substituted with a polymerizable vinyl or olefinic group. Preferred dihydrogen phosphate esters are phosphates of hydroxyalkyl acrylates or methacrylates, including 2-phosphoethyl methacrylate (PEM) and salts thereof.
A preferred acrylic latex comprises structural units of a carboxylic acid monomer and a phosphorus acid monomer, preferably PEM. The acrylic polymer particles may have an acorn morphology (as described in U.S. Pat. No. 9,920,194 B2), or a spherical morphology, or a blend of spherical and acorn morphologies. The acrylic polymer particles with an acorn morphology may comprise a protuberating phosphorus acid functionalized core, more particularly a protuberating PEM functionalized core.
The matting agent fed from the matting agent pre-paint storage tank may be an organic matting agent or an inorganic matting agent. Examples of organic matting agents are aqueous dispersions of polymeric microspheres having a median weight average particle size (D50) in the range of from 0.7 μm, preferably from 1 μm, and more preferably from 2 μm, and most preferably from 4 μm, to 30 μm, preferably to 20 μm, and more preferably to 13 μm, as measured using a Disc Centrifuge Photosedimentometer (DCP). These organic polymeric microspheres are characterized by being non-film-forming and preferably having a crosslinked low Tg core, that is, a crosslinked core having a Tg, as calculated by the Fox equation, of not greater than 25° C., more preferably not greater than 15° C., and more preferably not greater than 10° C.
The crosslinked core of the organic polymeric microspheres preferably comprises structural units of one or more monoethylenically unsaturated monomers whose homopolymers have a Tg of not greater than 20° C. (low Tg monomers) such as methyl acrylate, ethyl acrylate, n-butyl acrylate, and 2ethylhexyl acrylate. Preferably, the crosslinked low Tg core comprises, based on the weight of the core, from 50, more preferably from 70, more preferably from 80, and most preferably from 90 weight percent, to preferably 99, and more preferably to 97.5 weight percent structural units of a low Tg monoethylenically unsaturated monomer. n-Butyl acrylate, and 2ethylhexyl acrylate are preferred low Tg monoethylenically unsaturated monomers used to prepare the low Tg core.
The crosslinked core further comprises structural units of a multiethylenically unsaturated monomer, examples of which include allyl methacrylate, allyl acrylate, divinyl benzene, trimethylolpropane trimethacrylate, trimethylolpropane triacrylate, butylene glycol (1,3) dimethacrylate, butylene glycol (1,3) diacrylate, ethylene glycol dimethacrylate, and ethylene glycol diacrylate. The concentration of structural units of the multiethylenically unsaturated monomer in the crosslinked microspheres is preferably in the range of from 1, more preferably from 2 weight percent, to 9, more preferably to 8, and most preferably to 6 weight percent, based on the weight of the core.
The crosslinked polymeric core is preferably clad with high a Tg shell, that is, a shell having a Tg of at least 50° C., more preferably at least 70° C., and most preferably at least 90° C. The shell preferably comprises structural units of monomers whose homopolymers have a Tg greater than 70° C. (high Tg monomers), such as methyl methacrylate, styrene, isobornyl methacrylate, cyclohexyl methacrylate, and t-butyl methacrylate. The high Tg shell preferably comprises at least 90 weight percent structural units of methyl methacrylate.
Examples of inorganic matting agents include talc, clay, mica, and sericite; CaCO3; nepheline syenite; feldspar; wollastonite; kaolinite; dicalcium phosphate; and diatomaceous earth. Although it is possible to feed a blend of a variety of matting agents into the mixer from a single storage tank, it is preferable to feed different matting agents from separate tanks.
The opacifying pigment, latex, and matting agent pre-paint storage tanks each further comprise a rheology modifier. The concentration and type of rheology modifier included in each pre-paint storage tank is readily predetermined to achieve the desired Brookfield, KU, and ICI viscosity of the final paint. Examples of suitable rheology modifiers include hydrophobically modified ethylene oxide urethane polymers (HEURs); hydrophobically modified alkali swellable emulsion (HASEs); alkali swellable emulsions (ASEs); and hydroxyethyl cellulosics (HECs), and hydrophobically modified hydroxyethyl cellulosic (HMHECs); and combinations thereof.
Preferably, the latex pre-paint storage tank and the opacifying pigment pre-paint storage tank each comprise a HEUR and the matting agent pre-paint storage tank comprises an ASE or a HASE, or an HEC.
The process of the present invention provides a way of making a wide variety of paints quickly with minimal cleanup between runs. Significantly, no further mixing is required after the in-line mixed pre-paints are dispensed into the paint container.
The following pre-paint storage vessels were prepared:
In the following examples, BA refers to butyl acrylate, MMA refers to methyl methacrylate.
In the following examples, Latex 2 is a BA/MMA/PEM latex with spherical morphology having a solids content of 46% by weight and a calculated Tg by the Fox equation of 14° C. Latex 3 is a BA/MMA/PEM latex with acorn morphology having a solids content of 49% by weight and a calculated Tg by the Fox equation of 10° C.
Latex and TiO2 pre-paints stored in separate storage vessels were concurrently pumped through a static in-line mixer ( 3/16″ o.d., Model 3/16-12, Koflo Corporation) fitted with a Y-shaped connector and a 3/16″ inner diameter plastic tubing (Masterflex pump tubing model 96410-15, MasterFlex). The latex pre-paint (39.6% vol solids) contained a pre-mixed blend of water (143.4 g), RHOPLEX™ VSR-1050 Acrylic Latex (660.3 g, a Trademark of The Dow Chemical Company or its Affiliates), DC8590 Defoamer (0.17 g), CF-10 Surfactant (0.4 g), Texanol Coalescent (16.5 g), and RM-8w (1.9 g); and the TiO2 pre-paint vessel 2 contained 4311 TiO2 (800 g) and RM2020-NPR (27.2 g). Peristaltic pumps (model 7524-50 MasterFlex L/S digital economy drive pump with a dual easy load (model 7518-10) connected) were used to pump the pre-paints through the in-line mixer. The flow rate of the peristaltic pump displacing the binder pre-paint was set to 18-20 m/min and the flow rate of the peristaltic pump displacing the titanium dioxide pre-paint was set to 4 m/min. The amounts of pre-paints displaced from the vessels were determined gravimetrically. The final paint flowing out of the Y-shaped connector containing the in-line mixer was collected in a plastic paint container. The paint was collected over 8-10 min. PVC, volume solids, KUo, KUf, gloss, and contrast ratio were measured.
The procedure as described in Example 1 was used except that the latex pre-paint vessel contained a pre-mixed blend of water (35.2 g), Latex 2 (777.0 g), DC8590 Defoamer (0.17 g), CF-10 Surfactant (0.4 g), Texanol Coalescent (17.9 g), and RM-8w (1.9 g), 39.6% vol solids. The volume solids of the latex pre-paint was 39.6%; PVC, volume solids, KUo, KUf, gloss, and contrast ratio were measured.
The procedure as described in Example 1 was used except that the latex pre-paint vessel contained a pre-mixed blend of water (71.9 g), Latex 3 Polymer (743.9 g,), DC8590 Defoamer (0.17 g), CF-10 Surfactant (0.4 g), Texanol Coalescent (17.9 g), and RM8w (1.5 g). The volume solids of the latex pre-paint was 39.6%; PVC, volume solids, KUo, KUf, gloss, and contrast ratio were measured.
A low gloss paint was prepared by placing an additional Y-shaped connector containing an in-line mixer to a matting agent pre-paint storage vessel downstream of the Y-shaped connector connecting the Latex 3 and TiO2 pre-paint storage vessels. The matting agent was a dispersion of acrylic microspheres having a D50 particle size of 0.85 μm prepared substantially as described in U.S. Pat. No. 9,410,053 B2, Sample D, column 14, lines 1-48. Immediately after the latex and TiO2 pre-paints were mixed in a first in-line mixer, the TiO2/latex blend was contacted with the flow of organic microspheres in a Y-shaped connector and tubing containing an in-line mixer. The flow rate from the latex pre-paint storage vessel was 16 mL/min, and the flow rates from the TiO2 and matting agent pre-paint storage vessels were both 3 mL/min. The final paint flowing out of the upstream Y-shaped connector containing the in-line mixer was collected in a plastic paint container. The paint was collected over 8-10 minutes. The volume solids of the latex pre-paint was 39.0%; PVC, volume solids, KUo, KUf, gloss, and contrast ratio were measured.
A low gloss paint was prepared as described in Example 4 except that the matting agent was a dispersion of microspheres (8.5 μm, 34.2% solids) prepared in accordance with the procedure as described in U.S. Pat. No. 10,676,580, Example 4, except that 4.2 g of oligomer seed was used instead of 12.8 g of oligomer seed. PVC, volume solids, KUo, KUf, gloss, and contrast ratio were measured.
Table 1 show the TiO2 PVC, Matting Agent PVC (MA PVC), volume solids (VS), initial KU (KUo), KU after 1 d (KUf), ΔKU, 60/85° gloss, and contrast ratios for each sample.
A wide variety of paints can be prepared by the process of the present invention by simply adjusting the flow rates from the pre-paint storage tanks. The fully blended paints are prepared before the paint is dispensed into the paint container. As such, no additional stirring or shaking of the contents in the paint can is needed.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2022/029610 | 5/17/2022 | WO |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 63188616 | May 2021 | US |
| Child | 18556495 | US |
