Cottonseed oil based liquid color composition and plastics coloring method using the same

Information

  • Patent Grant
  • 10767031
  • Patent Number
    10,767,031
  • Date Filed
    Tuesday, January 30, 2018
    6 years ago
  • Date Issued
    Tuesday, September 8, 2020
    4 years ago
Abstract
A method of fabricating plastic products having a preselected color, comprising preparing a dispersion of pigment of the preselected color in cottonseed oil; supplying a preselected plastic resin for the product to be fabricated to a process machine having a rotating screw; furnishing the dispersion to the process machine at a position adjacent to threaded portion of the rotating screw; and blending the dispersion and the resin by rotating the screw.
Description
STATEMENT REGARDING FEDERAL FINANCING RESPECTING THIS INVENTION

Not applicable.


INCORPORATION BY REFERENCE

Applicant hereby incorporates by reference the disclosures of U.S. Pat. Nos. 3,468,904 A and 3,488,204 A as well as U.S. Pat. Nos. 4,921,132 A, 7,201,290 B2, 8,042,578 B2, 8,627,852 B2, 8,757,217 B2, 9,188,118 B2, and 9,708,462 B2 and United States patent publications U.S. 2002/0122103 A1, 2002/0189667 A1, 2003/0071868 A1, U.S. 2005/0126638 A1, U.S. 2010/0322644 A1, U.S. 2010/0322644 A1, U.S. 2016/0040661A1 and U.S. 2017/0152366 A1.


BACKGROUND OF THE INVENTION
Field of the Invention

This invention involves use of cottonseed oil as the primary ingredient or a secondary ingredient of a liquid carrier when manufacturing liquid color for the plastics industry and when fabricating plastic articles of a desired color.


Description of the Prior Art

Plastic products are most often colored.


Color pigments begin in powder form. Because powder is messy and difficult to handle, it is almost always pre-dispersed into some “carrier” that is easier to handle.


Typically color pigment is pre-dispersed into pellets of plastic resin, with the pellets containing typically 50% pigment, by weight. In the United States, these pellets are referred to as “concentrate” and in Europe as “masterbatch”.


As used herein the term “process machine” embraces extruders and injection molding presses.







DESCRIPTION OF THE INVENTION

A better method to make the pigment easier to handle is to pre-disperse the pigment into a liquid carrier. This is one of the methods to which this invention is directed.


The liquid carrier for the pigment must be compatible with the plastic resin to which it is to be added. Different resins may require different carriers. When selecting a liquid carrier, certain characteristics are desirable while other characteristics must be avoided.


Surfactants, or “soap-like” carriers, can cause “slip” during the molding or extrusion process, which must be avoided.


The liquid carrier must not break down at the high temperatures required in the molding or extrusion process that melt the plastic resin.


Carrier liquid that imparts an odor to the final part cannot be used when molding or extruding products to be used to contain food, such as plastic water bottles.


Cost and availability of the carrier liquid are always factors.


Heretofore, no single liquid carrier solves all these problems. However this invention is based on the discovery that cottonseed oil is superior to other carriers in meeting a number of these requirements and solving many of the aforementioned problems. Cottonseed oil is not known to have previously been used as a carrier for pigment in making liquid color for use in plastics molding or extrusion.


Cottonseed oil has a relatively high flash point, and a high smoke point, well above 400° F. Most other liquid carriers smoke below 400° F.


Cottonseed oil has very little odor. Cottonseed oil is known to be used as a cooking oil that does not impart flavor to the food being cooked. This is a benefit when molding or extruding plastic products used for food packaging.


Cottonseed oil is high in antioxidants, providing an advantage in preserving products packaged in plastic that has been molded or extruded using a cottonseed oil carrier for the liquid color providing the color for the product packaging.


Cottonseed oil is high in vitamin “E”, an antioxidant, which is often required as an additive when using other carriers.


Cottonseed oil is available in bulk qualities, and is competitively priced.


In one of its aspects, this invention provides a method of fabricating a plastic article of pre-selected color where the method includes preparing a blend, where the blend preferably comprises solid plastic resin pellets and liquid color of a hue and in an amount to impart the pre-selected color to the article to be fabricated, where the liquid color preferably includes cottonseed oil, and thereafter forming the blend preferably under pressure and heat into the plastic article. The method may preferably be accomplished either by injection molding or by extrusion. In practice of this aspect of the invention, the liquid color preferably comprises at least one dispersion of a single pigment in cottonseed oil. Even more preferably, the liquid color may comprise a plurality of dispersions, each of a single pigment in cottonseed oil.


The method may further include the liquid color preferably comprising at least one additive to facilitate fabrication of the plastic article, where the additive may be selected from the group preferably comprising lubricants, blowing agents, light stabilizers, nucleating agents, antistatic agents and antioxidants.


In another aspect of this invention, the invention preferably provides a liquid colorant for use in molding or extruding plastic products where the colorant preferably comprises pigment dispersed in cottonseed oil. In a more limited aspect of the invention, the invention provides a liquid colorant for use in molding or extruding plastic products consisting of only pigment and cottonseed oil.


In still another aspect, this invention provides a liquid colorant for use in molding or extruding plastic products where the colorant preferably includes pigment, cottonseed oil, and at least one additive, with the additive desirably being preferably dispersed together with the pigment in the cottonseed oil. In this aspect of the invention, the additive may preferably be one or more lubricants, blowing agents, light stabilizers, nucleating agents, antistatic agents, and/or antioxidants.


In one preferred practice of this invention, a single pigment dispersion is prepared initially by dispersing pigment of a desired color in cottonseed oil to create a liquid blend. The pigment is preferably initially introduced into a vat of cottonseed oil, which acts as a liquid carrier. The pigment is preferably stirred into the cottonseed oil. The pigment is preferably added to the cottonseed oil in the known correct proportion. Typically the batch of pigment added to the cottonseed oil is from 50% to 70% by weight of the resulting pigment-cottonseed oil blend. That is the preferred range; the range can be as low as 25% by weight of pigment, relative to the weight of the resulting pigment-cottonseed oil blend, and can range up to 80% by weight of pigment to the weight of the resulting pigment-cottonseed oil blend.


In general, it is desirable to put as much pigment into the cottonseed oil as is possible.


Next the dispersion of the pigment in the cottonseed oil is preferably milled by passing the liquid through a mill serving to break down any agglomerates of pigment that may remain in the single pigment dispersion, thereby reducing particle size of the pigment to as small a size as possible. The resulting particles of pigment powder are very, very small, producing the fullest, richest color. Milling the single pigment dispersion allows use of less pigment to perform the particular coloring function, thereby reducing costs. The milling may be done using a roller mill or a sand mill. Both roller mills and sand mills are common industrial mills.


In the practice of the invention, it is desirable at times to produce a color or hue that is not one of the colors of the basic pigment. In such case, two or more single pigment dispersions, each dispersion being of a single pigment in cottonseed oil, are prepared. The two or more single pigment dispersions are then blended together to produce a resulting dispersion exhibiting the correct hue or shade of color desired. The resulting dispersion is then milled. This two-step process allows milling of a larger quantity of pigment in the resulting dispersion at one time so that clean up between milling different colors is less frequent and the expense of milling of each of the single pigment dispersions separately is avoided.


Use of cottonseed oil as the carrier for the single pigment dispersion or the blend of single pigment dispersions results in liquid color that is compatible with nearly all resins that are currently used in plastic molding and extrusion. The cottonseed oil-based pigment dispersion does not leach out of any finished product, nor does the cottonseed oil by itself leach out of any finished product. The cottonseed oil has been found to hold the pigment powder particles in suspension very well and accepts a high loading of pigment.


Pigment-cottonseed oil liquid colorant in accordance with the invention may be used to color most commercially used thermoplastics, whether processed by means of extrusion, injection molding or blow molding, as well as thermoplastics that are processed using less conventional processes. When properly formulated, the pigment-cottonseed oil liquid color according to the invention is not just compatible with a base resin, but frequently improves the fabricating process and/or the performance properties of the fabricated plastic parts.


The range of thermopolymers with which the cottonseed oil colorants and single pigment cottonseed oil dispersions of the invention may be used is quite broad, and includes acrylic, nylon, acrylonitrile butadiene styrene, polycarbonate, polybenzimidazole, polyether sulfone, polyetherether keytone, polyethermide, polyethylene, polypropylene, polythenylene sulfide, polyphenylene oxide, polystyrene, polyvinyl chloride, polytetrafluoroethylene, as well as others.


Liquid color according to this invention may be formulated in various ways to provide various advantageous product characteristics. For example, commodity colorants may be formulated in accordance with the invention to maximize savings without sacrificing processability and cosmetic appearance of the final plastic parts. Such commodity colorants offer the processor economies of color and are suitable for mass manufacture of volume parts such as housewares, disposable goods, toys and the like.


The invention also has applicability to providing liquid color for use in fabricating articles designed for outdoor use, specifically for lawn and garden applications, for the toy and recreation industries. The liquid color in accordance with the invention may be formulated to meet very stringent requirements of heat stability and color fastness of the resulting fabricated color parts. Such parts may be used in applications requiring extended exposure to sunlight and/or unusually high temperatures during the fabrication process.


The liquid color according to the invention may be produced to provide special effects such as fluorescent, phosphorescent, pearlescent, and non-dispersing finishes, where such unconventional appearances are dictated by the design of the parts.


Liquid color in accordance with the invention is typically from 20% to 40% cheaper than use of pelletized color concentrate.


In another method for practicing the invention, one may make liquid color for use in the course of molding or extruding plastic parts by initially providing a collection of pigments. Next, one selects a formula for the pigment(s) and liquid carrier that will provide liquid color in a desired hue for coloring plastic parts being molded or extruded. Selecting the formula may be a “trial and error” process, in that slight changes in hue as required by a customer require changes in the pigment constituency, thereby requiring experimentation as to the exact formula of pigments required to produce the required hue.


Once the formula has been established for the amount of pigment(s) and the amount of liquid carrier, the pigments are selected in amounts required in the formula by the collection of pigments. A liquid carrier of cottonseed oil is provided in an amount according to the formula and the selected pigments are then blended, preferably but not necessarily all at once, into the cottonseed oil to produce a required liquid color. When this approach is used, the finished liquid color is generally not milled, as the mill would have to be cleaned after every color blend. However, such liquid color can be milled if necessary. This method of the invention avoids the two-step process of making the single pigment dispersions, milling single pigment dispersions individually, and then combining the single pigment dispersions to produce the required liquid color.


The processing of thermoplastic resin and/or the performance of the fabricated plastic parts can often be greatly enhanced through use of additives. Many commercial resins already include additives. However, significant benefits can be derived from further modification of such compounds in many cases. Moreover, use of additives affords a plastics processor the opportunity to tailor the plastic resin material to a specific application.


Processing aid-type additives improve productivity of the molding or extrusion machinery through reduction of internal friction; these additives are referred to as “lubricants.” Other processing aid-type additives change polymer morphology and are referred to as “nucleating agents.” Still other processing aid-type additives remove excessive heat and are in the form of endothermic blowing agents. Yet additional processing aid-type additives suppress thermal decomposition during processing and are generally referred to as “antioxidants.”


Other additives, such as blowing agents and optical brighteners, enhance aesthetics and/or performance properties of the final parts by, for example, providing antistatic properties or ultraviolent light stabilization characteristics to the product.


Modification of properties of thermopolymers through the addition of various chemical additives is economically preferable to the introduction of an entirely new resin. The most economical way to add these additives to the molding or extrusion process is through the use of liquid color, in accordance with this invention.


This invention may be embodied in other specific forms without departing from the spirit or essential characteristics of the invention. The disclosed embodiments are therefore to be considered in all respects as being illustrative and not restrictive with the scope of the invention being indicated by the appended claims rather than by the foregoing description. All changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Suitable additives within the scope of the invention are discussed below:


Glide Slip Agents: Plastic processing often needs a slip agent to assist in polymer flow and provide internal and external slip characteristics. Friction characteristics, when processing polymers, requires slip/lubricants in order to improve cycle times, improve dispersion, assist mold release and improve assembly of molded parts. The amount of slip depends on the process and end use requirements. Consumer packaging requirements often need slip for the finished product, but the plastic processor may also need it to improve processing and plastic parts assembly.


Shield Liquid Light Stabilizer Agents: Liquid light stabilizers are effective in a broad range of plastics and can help achieve long-term sustainability goals as in the recycling of plastics, including products formulated with hindered amines (HALS) and UV absorbers. For certain applications, blends of these two products provide improved performance. Ultraviolet (UV) radiation from the sun needs the combination of HALS and antioxidants for long-term stability. Polymer photo-oxidation is a combined action of light and oxygen. The visible result of this action is deterioration of the appearance of the polymer as well as mechanical and chemical concerns. Additive products can protect against these conditions. UV absorbers protect the contents of plastics packaging from ultraviolet rays up to 390 nm.


Speed Nucleating Agents: Liquid nucleating agents improve the physical properties of semi-crystalline polyolefins. This results in fast crystallization rates, which allows for improved cycle times and better production capacity along with quality. When the clarifying agent is added to polypropylene, the size of crystalline structures of the polymer reduces to improve the stiffness and clarity. Additionally, when added to the process, the rate of crystal initiation is increased dramatically so the crystals become smaller in size thereby clarifying the polypropylene. These aspects of the invention meet the needs of a well-nucleated product by offering a combination of high crystalline temperature in the polymer with the most isotropic (uniform) shrinkage in the finished product.


Guard Antioxidant Agents: Heat is a necessary function for molding plastics. However, under higher than normal processing temperatures, it may be necessary to add an additional stabilizer to maintain the integrity of the polymer. Degradation of polymers, due to excessive heat, can have an effect on the process, product stability and screw barrel contamination. Another factor of concern is the increased use of PCR. Antioxidant additions to the combinations of virgin and PCR resins can provide the heat stability needed to maintain a healthy polymer. Solutions range from a single functional antioxidant, for processing with higher heat conditions, to multifunctional products that improve heat stability as well as long-term heat aging.


Foam Liquid Blowing Agents: For many years, foaming agents have been used to reduce the densities of molded and extruded thermoplastics. Today, this need is receiving more attention because of the desire to make plastics more sustainable. This can be accomplished by reducing the amount of plastic needed to make a finished product. By reducing the density, one reduces the amount of plastic used to make molded parts and extruded products, thereby reducing the carbon footprint. Liquid foaming agents can be metered precisely into the melt flow to achieve the desired level of density reduction and are produced without a heat history eliminating pre-decomposition concerns. The selection of endothermic, exothermic, or a combination of both is within the scope of the invention. Processing with liquid endothermic foaming agents also reduce energy required for the process.


Clean Antimicrobial Agents: These are inorganic silver based antimicrobials, which inhibit the growth of gram-positive/gram-negative bacteria, mold and yeast. Untreated plastic products run the risk of microbial growth causing unsightly discoloration, staining, unpleasant odors as well as deterioration and corrosion of manufactured products.


Gains Flow Modifiers: There are many situations in plastics processing where a slight change in resin dispersion and flow characteristics benefits the process as well as the product. Additives that, when metered at low letdowns, solve processing problems such as poor dispersion, black specks, easier flow properties, better mold release, improved surface characteristics, reduction in sheer stress along with heating, and an overall reduction in energy consumption. The raw materials used in practicing the invention have a history of performing well in plastics.


As discussed above and from the foregoing description of the exemplary embodiments of the invention, it will be readily apparent to those skilled in the art to which the invention pertains that the principles and particularly the composition and methods disclosed herein can be used for applications other than those specifically mentioned. All such applications of the invention are intended to be covered by the appended claims unless expressly excluded therefrom.


As used in the claims below, “comprising” means “including” while “consisting of” means “having only”, and “consisting essentially of” means having the stated constituents plus trivial amounts of other reagents which do not materially affect the claimed invention or products embodying the same.


The scope of the invention is, therefore, indicated by the appended claims rather than by the foregoing description and all changes which come within the range of equivalency of the claims are to be considered to be embraced within the scope of the claims. Additional objects, other advantages, and further novel features of the invention will become apparent from study of the appended claims as well as from study of the foregoing detailed discussion and description of the preferred embodiments of the invention, as that study proceeds.

Claims
  • 1. A method for making colored plastic parts comprising plastic resin being selected from the group comprising acrylic, nylon, acrylonitrile butadiene styrene, polycarbonate, polybenzimidazole, polyether sulfone, polyetherether ketone, polyethermide, polyethylene, polypropylene, polyethylene sulfide, polyphenylene oxide, polystyrene, polyvinyl chloride, polytetrafluoroethylene, the method comprising: a) providing a collection of pigments;b) providing a quantity of a liquid carrier consisting of cottonseed oil;c) from the collection of pigments creating a plurality of separate single pigment liquid dispersions in separate portions of the cottonseed oil;d) blending one or more of the plurality of separate single pigment liquid dispersions to create a liquid blend of a desired color;e) combining the liquid blend with the selected plastic resin;f) molding the resin-liquid blend combination into the colored plastic parts.
  • 2. A colored plastic part comprising a plastic resin selected from the group comprising acrylic, nylon, acrylonitrile butadiene styrene, polycarbonate, polybenzimidazole, polyether sulfone, polyetherether ketone, polyethermide, polyethylene, polypropylene, polyethylene sulfide, polyphenylene oxide, polystyrene, polyvinyl chloride, and polytetrafluoroethylene, made by the process comprising: a) providing a collection of pigments;b) providing a quantity of a liquid carrier consisting of cottonseed oil;c) from the collection of pigments creating a plurality of separate single pigment liquid dispersions in separate portions of the cottonseed oil;d) blending one or more of the plurality of separate single pigment liquid dispersions to create a liquid blend of a desired color;e) combining the liquid blend with the selected plastic resin;f) molding the resin-liquid blend combination into the colored plastic part.
  • 3. The method of claim 1, wherein the pigment in each of the plurality of separate single pigment liquid dispersions comprises from about 25% to about 80% by weight of the plurality of separate single pigment liquid dispersion.
  • 4. The method of claim 1, wherein the pigments in the blend of the desired color comprises comprise about 25% to about 80% by weight of the liquid blend.
  • 5. The method of claim 1, wherein at least one of the pigments in the collection of pigments is a powder.
CROSS-REFERENCE TO RELATED PATENT APPLICATION

This patent application is a 35 USC 120 continuation-in-part application, claiming the benefit of the priority of parent U.S. patent application Ser. No. 15/432,495, now published as United States patent publication US 2017-0152366 A1, filed 14 Feb. 2017 in the name of Stephen B. Maguire and entitled “Cottonseed Oil Based Liquid Color Composition and Plastics Coloring Method Using the Same.” This patent application, through the '495 application and the parent of the '495 application, namely U.S. patent application Ser. No. 14/333,579 filed 17 Jul. 2014 in the name of Stephen B. Maguire and entitled “Liquid Color Composition with Cottonseed Oil Base,” published 22 Jan. 2015 as United Stated patent publication 2015/0020713 A1, and issued as U.S. Pat. No. 9,708,462 on 18 Jul. 2017, claims the benefit of the priority under 35 USC 120 of the '579 application (now the '462 patent) and the benefit of the priority of U.S. provisional patent application Ser. No. 61/847,119 entitled “Liquid Color Composition with Cottonseed Oil Base” filed 17 Jul. 2013 in the name of Stephen B. Maguire.

US Referenced Citations (157)
Number Name Date Kind
600233 Palm Mar 1898 A
1305964 Dickson Jun 1919 A
1451759 Bruhn Apr 1923 A
1482376 Anderson Feb 1924 A
1489348 Hampton Apr 1924 A
1707977 Davis Apr 1929 A
2188646 Bunch Jan 1940 A
2199657 Bunch May 1940 A
2387233 Clapp Oct 1945 A
2606696 Miner Aug 1952 A
2656828 Conover Oct 1953 A
2665825 Poitras et al. Jan 1954 A
2701881 McGee Feb 1955 A
2873892 Nelson et al. Feb 1959 A
2909315 Sampietro Oct 1959 A
2956822 Kates Oct 1960 A
3252618 Anderson May 1966 A
3297049 Moscovitz Jan 1967 A
3391645 Koza Jul 1968 A
3468904 Kritchevsky Sep 1969 A
3471178 Roe Oct 1969 A
3477698 Smith et al. Nov 1969 A
3481509 Marhauer Dec 1969 A
3488204 Hardy Jan 1970 A
3518033 Anderson Jun 1970 A
3785412 Stone Jan 1974 A
3814388 Jakob Jun 1974 A
3820828 Fiddler Jun 1974 A
3883275 Browne May 1975 A
3953218 Pollard Apr 1976 A
3957399 Siczek May 1976 A
3960393 Hosokawa Jun 1976 A
3988088 King et al. Oct 1976 A
3998103 Bjorklund et al. Dec 1976 A
4046495 Grimm, Jr. Sep 1977 A
4124042 Foulkes Nov 1978 A
4185948 Maguire Jan 1980 A
4211345 Taubenmann Jul 1980 A
4251796 Soeda Feb 1981 A
4377291 Albertini Mar 1983 A
4382618 Grisebach May 1983 A
4469127 Kitamura Sep 1984 A
4473173 DeGroff et al. Sep 1984 A
4479107 Bleeke Oct 1984 A
4501405 Usry Feb 1985 A
4571416 Jarzombeck et al. Jan 1986 A
4580721 Coffee Apr 1986 A
4586882 Tseng May 1986 A
4605297 Livingston et al. Aug 1986 A
4606710 Maguire Aug 1986 A
4621990 Forsythe et al. Nov 1986 A
4657490 Abbott Apr 1987 A
4759189 Stropkay Jul 1988 A
4796782 Wales Jan 1989 A
4815042 Pratt Mar 1989 A
4834071 Hosoi et al. May 1989 A
4921132 Wales May 1990 A
4967940 Blette et al. Nov 1990 A
5039279 Natwick et al. Aug 1991 A
5116547 Tsukahara et al. May 1992 A
5183075 Stein Feb 1993 A
5187993 Nicholson et al. Feb 1993 A
5199852 Danby Apr 1993 A
5215215 Sauer Jun 1993 A
5225210 Shimoda Jul 1993 A
5257914 Reynolds Nov 1993 A
5318431 Chang Jun 1994 A
5344232 Nelson et al. Sep 1994 A
5364242 Olsen Nov 1994 A
5402670 Wicnienski Apr 1995 A
5404904 Glaser Apr 1995 A
5423455 Ricciardi Jun 1995 A
5580503 Hall, III Dec 1996 A
5609191 Topping Mar 1997 A
5622392 Gochenouer Apr 1997 A
5723517 Campo Mar 1998 A
5853244 Hoff et al. Dec 1998 A
5911339 Peterson Jun 1999 A
5953923 Davies Sep 1999 A
5980490 Tsoukalis Nov 1999 A
5984777 Kuchar Nov 1999 A
5988983 Furusawa Nov 1999 A
6007236 Maguire Dec 1999 A
6057514 Maguire May 2000 A
6188936 Maguire et al. Feb 2001 B1
6213739 Phallen et al. Apr 2001 B1
6287491 Kilim et al. Sep 2001 B1
6386841 Probst May 2002 B1
6402363 Maguire Jun 2002 B1
6402865 Handa et al. Jun 2002 B1
6502013 Sosnik Dec 2002 B1
6523451 Liao et al. Feb 2003 B1
6599005 van Der Wel Jul 2003 B2
6669358 Shimoda Dec 2003 B2
6719453 Cosman et al. Apr 2004 B2
6732629 Miller et al. May 2004 B1
6840744 Watling Jan 2005 B2
6853100 Yumita Feb 2005 B2
6879876 O'Dougherty et al. Apr 2005 B2
6880965 Sheffield, Jr. Apr 2005 B1
6991004 Kaufhold et al. Jan 2006 B2
7118349 Oglesby Oct 2006 B2
7154069 Gordon Dec 2006 B1
7201290 Mehus Apr 2007 B2
7264161 Polarine Sep 2007 B2
7311882 Renzi Dec 2007 B1
7390119 Maguire Jun 2008 B2
7416096 Maguire Aug 2008 B2
7526911 Pickard et al. May 2009 B2
7594717 Sheinman Sep 2009 B2
7958915 Maguire Jun 2011 B2
7980834 Maguire Jul 2011 B2
8042578 Post Oct 2011 B2
8230877 Roberge et al. Jul 2012 B2
8627852 Hatton Jan 2014 B2
8757217 Maguire Jun 2014 B2
8800821 Maguire et al. Aug 2014 B2
8844584 Haley Sep 2014 B1
9188118 Maguire Nov 2015 B2
9599265 Maguire Mar 2017 B2
9637283 Maguire May 2017 B2
20020023449 Park et al. Feb 2002 A1
20020031822 Van Der Wei et al. Mar 2002 A1
20020036950 Cosman Mar 2002 A1
20020122103 Yamamoto et al. Sep 2002 A1
20020189667 O'Dougherty et al. Dec 2002 A1
20030051767 Coccaro Mar 2003 A1
20030071868 Koshikawa et al. Apr 2003 A1
20030095468 Shimoda May 2003 A1
20030142580 Maguire Jul 2003 A1
20030218014 Gregory et al. Nov 2003 A1
20040020723 Schuman Feb 2004 A1
20050052945 Maguire Mar 2005 A1
20050126638 Gilbert Jun 2005 A1
20060067844 Iversen Mar 2006 A1
20060151051 Py Jul 2006 A1
20060169718 Buining Aug 2006 A1
20070071624 Brewer Mar 2007 A1
20070292288 Maguire Dec 2007 A1
20080267002 Rannasmaa Oct 2008 A1
20100276033 Asp et al. Nov 2010 A1
20100322644 Ajima Dec 2010 A1
20110200464 Maguire et al. Aug 2011 A1
20120189762 Reineccius Jul 2012 A1
20120195771 Brender a Brandis Aug 2012 A1
20120260992 Maguire Oct 2012 A1
20130334258 Maguire Dec 2013 A1
20140087035 Cummings Mar 2014 A1
20140147288 Maguire May 2014 A1
20140224830 Maguire Aug 2014 A1
20140348667 McCourt et al. Nov 2014 A1
20150020713 Maguire Jan 2015 A1
20150066794 Maguire et al. Mar 2015 A1
20150108748 Maguire Apr 2015 A1
20150165662 Maguire Jun 2015 A1
20160040661 Maguire Feb 2016 A1
20170001354 Nobuta et al. Jan 2017 A1
Foreign Referenced Citations (13)
Number Date Country
2643213 Aug 2007 CA
2809263 Aug 2006 CN
3433693 Mar 1986 DE
40 23 933 Jan 1991 DE
1400332 Mar 2004 EP
1 477 595 Apr 1967 FR
2 273 648 Jan 1976 FR
1145752 Mar 1969 GB
3550699 Aug 2004 JP
2013-018283 Jan 2013 JP
10-2011-0100596 Sep 2011 KR
WO 0149374 Jul 2001 WO
WO 2015089499 Jun 2015 WO
Non-Patent Literature Citations (20)
Entry
Forty-four page two-sided brochure including cover and back pages entitled “Maguire: Auxiliary equipment for the plastics industry” of Maguire Products Inc. Oct. 2000.
Two-sided color brochure entitled Maguire: Model MPA Liquid Color Pump Maguire Products Inc. published Dec. 28, 1995.
International Search Report for PCT/US02/02934 dated Feb. 20, 2003.
Written Opinion for PCT/US02/02934 dated Mar. 24, 2003.
International Search Report for PCT/US11/021994 dated May 24, 2011.
Written Opinion for PCT/US11/021994 dated May 24, 2011.
Thirty-two page catalog entitled “Maguire Color Blending Equipment” published by Maguire Products Inc. 1993 United States.
International Search Report for PCT/US2014/070284 dated Apr. 15, 2015.
Written Opinion for PCT/US2014/070284 dated Apr. 15, 2015.
International Search Report for PCT/US2014/053391 dated Jan. 29, 2015.
Written Opinion for PCT/US2014/053391 dated Jan. 29, 2015.
Wayback Machine of SMC Linear Actuators Sep. 11, 2011 SMC Accessed on Apr. 6, 2016.
Wayback Machine of SMC Linear Actuator C02 Series Catalog Sep. 11, 2011 SMC Accessed on Apr. 6, 2016.
Extended European Search Report and Written Opinion for European Patent Application No. 14870414.1, dated Sep. 12, 2017.
European Search Report and Written Opinion for European Patent Application No. 14840183.9, dated Apr. 24, 2017.
Dec. 31, 2018 Non-Final Office Action against Applicant's co-pending U.S. Appl. No. 15/420,762.
Jan. 25, 2019 Final Office Action against Applicant's co-pending U.S. Appl. No. 15/581,960.
Mar. 6, 2019 Final Office Action against Applicant's co-pending U.S. Appl. No. 15/298,802.
Mar. 8, 2019 Final Office Action against Applicant's co-pending U.S. Appl. No. 14/700,911.
International Search Report and Written Opinion for PCT/US2018/025069; dated Jul. 17, 2018.
Related Publications (1)
Number Date Country
20180155522 A1 Jun 2018 US
Provisional Applications (1)
Number Date Country
61847119 Jul 2013 US
Continuations (2)
Number Date Country
Parent 15432495 Feb 2017 US
Child 15883501 US
Parent 14333579 Jul 2014 US
Child 15432495 US