Patent Application
20080004384
A full and enabling disclosure of this invention, including the best mode shown to one of ordinary skill in the art, is set forth in this specification. The following Figures illustrate the invention:
Reference now will be made to the embodiments of the invention, one or more examples of which are set forth below. Each example is provided by way of explanation of the invention, not as a limitation of the invention. In fact, it will be apparent to those skilled in the art that various modifications and variations can be made in this invention without departing from the scope or spirit of the invention.
The invention may comprise a composition comprising:
wherein M1 and M2 are the same or different, and may be combined into one cation, and are selected from at least one metal cation of calcium, strontium, lithium, and monobasic aluminum; and
wherein R1, R2, R3, R4, R5, R6, R7, R8, R9, and R10 are either the same or different and are individually selected from the group consisting of hydrogen, C1-C9 alkyl, hydroxy, C1-C9 alkoxy, C1-C9 alkyleneoxy, amine, and C1-C9 alkylamine, halogens, and phenyl, said metal salt compound being provided in a concentration of greater than about 0.5% by weight of the polyolefin composition; and silica. The composition may be in the form of a masterbatch, and may also include a stearate, such as zinc stearate, and a hydrotalcite compound. In one more specific embodiment, the invention comprises a masterbatch of polyolefin, Ca HHPA, and silica. Typically, the Ca HHPA is provided in a concentration of greater than about 0.5% by weight of the overall composition, as in the case of a masterbatch or concentrate. Further embodiments of the invention may include as well a hydrotalcite compound. The silica may be either hydrophilic or hydrophobic. Further, in some selected aspects of the invention, silica is provided in a concentration of less than about 5% of the composition (i.e. less than about 5% of the concentrate/masterbatch composition). The polyolefin may be polyethylene, polypropylene, or another known polyolefin such as polybutene, polyisoprene, or copolymers of such species. An acid scavenger such as a stearate may be employed, but is not required in the practice of the invention. Furthermore, an acid scavenger such as zinc stearate may be employed as an optional feature of the invention.
In yet another embodiment, the composition may include a polyolefin, a metal salt structure as generically shown, with greater than 0.5% by weight of the metal salt compound in the overall masterbatch, and a hydrotalcite compound. In this embodiment, the composition also may employ an optional acid scavenger, such as a stearate-containing compound. Zinc stearate may be particularly useful, but other stearates could be used as well, as optional additives into the masterbatch. Further, in yet another more specific embodiment of the invention, the Ca HHPA is employed as the metal salt compound. The Ca HHPA may be used at a concentration range of between about 0.5% and 20% by weight of the masterbatch concentrate.
Any of the embodiments described herein may be used to make solid polyolefin articles or polyolefin film, including for example polyethylene or polypropylene film. The invention may be used to manufacture linear low density polyethylene (LLDPE) blown film, by dispersing the masterbatch in LLDPE resin, and then preparing a blown film.
“Hydrotalcite compound” for purposes of its use in the invention refers to compounds which are either naturally occurring or synthetic hydrotalcite. One known and effective synthetic hydrotalcite compound that may be employed in the practice of the invention is set forth below in connection with Example 3 below, as in the form of: (Mg4.3Al2(OH)12.6CO3-3.5H2O)(known commercially as DHT-4A, available from the Kyowa Chemical Industry Company of Kagawa, Japan).
Many plastic converters engaged in the transformation of resin or resin pellets into useful articles employ various types of additive concentrates to manufacture film, sheet, plaques, or other plastic articles. Such additive concentrates are sometimes referred to as “masterbatch” concentrates, or simply “masterbatch” materials. The use of such masterbatch concentrates is useful in manufacturing operations, as it provides a convenient means of adequately dispersing into a resin additives or additive “packages” in relatively low final concentrations. It can be very difficult or impossible in some instances to disperse quickly and efficiently an additive at relatively low concentration levels into a resin. Masterbatches, however, make this possible and convenient. Concentrates or masterbatch compositions typically contain a carrier resin. It is not necessary that the carrier resin be the same type of resin that is used for dispersal of said masterbatch. For example, a carrier resin may be used in a masterbatch that is a polypropylene carrier resin, in which the polypropylene-based masterbatch is dispersed (“let down”) into a polyethylene for final article manufacture. This is just one example of how different resins may be used, by taking advantage of masterbatch intermediate compositions. Methods of employing each of the inventive compositions by combining the masterbatch (first polyolefin) with a second polyolefin to form a nucleated polyolefin composition are disclosed herein.
The additive concentrate of this invention may be used by a converter to easily “let down” the additive into the resin. By “let down” it is meant that the additive concentrate may be dispersed to a much lower concentration readily by mixing the additive into additional polymer resin. The masterbatch may be let down in processes such as injection-molding, film-blowing, extrusion blow molding or the like at a certain ratio to reach a final additive loading concentration in the manufactured plastic parts. Further, the use of a masterbatch facilitates relatively easy dispersion of such additives at low concentrations into a resin. A method is disclosed for making a nucleated polyolefin composition by providing a masterbatch composition comprising a polyolefin carrier, Ca HHPA nucleating agent, and silica and then mixing the masterbatch composition with a second polyolefin. This is by a “let down” step, which serves to disperse the Ca HHPA nucleating agent, thereby forming a nucleated polyolefin composition. The method optionally may employ a stearate-containing compound and/or a hydrotalcite compound. Yet another method of making a nucleated polyolefin composition involves making a masterbatch of a polyolefin carrier, a Ca HHPA nucleating agent, and a hydrotalcite compound.
Effective masterbatch compositions have been discovered, by way of the invention. Such composition provides improved dispersion and provides a very desirable and low haze for LLDPE blown film, injection molded polypropylene (PP) plaques, and injection molded polyethylene (PE) plaques. For purposes of this disclosure and claims herein, Ca HHPA shall refer to the following compound, described in commonly owned U.S. Pat. No. 6,599,971:
In one specific embodiment, the invention may exist as a combination of the following, which includes both a hydrotalcite compound and a silica compound:
1. DHT-4A (Mg4.3Al2(OH)12.6CO3-3.5H2O), a synthetic hydrotalcite compound sold by Mitsui Chemical Company;
2. Sylox 2: a hydrophilic silica compound sold by Grace Davison Company;
3. Zinc stearate,
4. Ca HHPA; and
5. Polypropylene or polyethylene.
In the practice of the invention, the polypropylene may be homopolymer (HPP), random copolymer (RCP), or metallocene-catalyzed polypropylene. Polyethylene may be employed in the practice of the invention in the form of linear low density polyethylene (LLDPE), low density polyethylene (LDPE), high density polyethylene (HDPE), or metallocene-catalyzed polyethylene.
Polypropylene homopolymer (HPP) with a melt flow rate of 12 (gram/10 min) with an additive package consisting of antioxidants such as 500 ppm Irganox 1010 and 1000 ppm Irgafos 168 and acid scavenger such as 2% zinc stearate and 4% of a nucleating agent composition such as Ca HHPA were high-intensity blended and melt-compounded on a twin screw extruder. The formulations are listed in Table 1 (antioxidants are standard formulations which are well known in the industry and not listed hereafter). “Sylox 2” is a silica-based product of Grace Davison of Columbia, Md.
The concentrates made herein were let down into injection-molding grade linear low density polyethylene (LLDPE) resin and plastic plaques (1.27 mm) were made with the final 1000 ppm nucleating agent loading. Haze and Tc were measured and listed in Table 1. Tc refers to peak crystallization temperatures as determined by differential scanning calorimetry (DSC), at a cooling rate of 20 degrees C/minute. The haze results are also shown in
Table 1,
Polypropylene homopolymer (HPP) with a melt flow rate of 12 (gram/10 min) with 4% of a nucleating agent such as Ca HHPA and 1% of ZnSt and different loadings of DHT-4A were melt-compounded and concentrates (masterbatches) were made. The Ca HHPA concentrates were made as in Example 1, and were let down into injection-molding grade homopolymer polypropylene (HPP). Plastic plaques (1.27 mm) were made as in Example 1, with a final 1000 ppm Ca HHPA loading. Plaque haze and Tc were measured and listed in Table 2. The results clearly show that DHT-4A improves Ca HHPA dispersion and decreases injection-molded plaque haze when employed at appropriate loadings.
Concentrates were made using the method described in Example 1. Two different carrier resins and different co-additives were used. The concentrates were tested using LLDPE injection-molding and a laboratory-line LLDPE blown film as in Example 1. The haze numbers are shown in Table 3 and the results confirmed the findings from Example 1 and 2 above. For the data below in Table 3, all concentrate samples contain 4% Ca HHPA and 2% ZnSt and the let-down ratio (LDR) was 2.5% which leads to 1000 ppm Ca HHPA loading in the final film or plaque articles. Adding both co-additives further improves film haze. “ICP” refers to impact copolymer. “LLDPE” refers to linear low density polyethylene.
Ca HHPA concentrates with different carrier resins were made as shown in Example 1 and then were let down into injection-molding grade LLDPE resin to make 1.27 mm plaques, as in Example 1. Also, such compositions were let down into LLDPE resin and 1 mil blown film was made from the resulting final composition. Both the injection-molded plaque and blown film haze measurements are listed in Table 4. Let down ratio (LDR) for all samples was 2.5%. The results show that Ca HHPA concentrates with co-additives have better haze even though these concentrates have lower final Ca HHPA loadings than the concentrates without co-additives.
Ca HHPA masterbatch concentrates (2.67% Ca HHPA and 1.33% ZnSt) having different co-additives with a polypropylene carrier resin having a melt flow rate of 37 were made as shown in Example 1 and they were let down at 2.5% ratio into injection-molding grade LLDPE resin. Plastic plaques having 667 ppm Ca HHPA loading were injection-molded and plaque haze was measured. The concentrates were also let down into LLDPE resin at 2.5% ratio and blown film was made having 667 ppm final additive loading. Both the injection-molded plaque and blown film hazes were listed in Table 5. Co-additive 1 (DHT-4A) was applied at a loading of 2% in samples 1-6. The results show that silica having the nature of hydrophobic rather than hydrophilic performs somewhat better in terms of haze. Furthermore, the use of relatively large particle size of silica rather than smaller nano-size particles improves performance of the concentrate.
Table 6 lists the performance of concentrates made from Ca HHPA having different processing aids in LLDPE injection-molding and LLDPE blown film, as in Example 1. The results show that certain processing aids improve the performance of Ca HHPA concentrates as well. For example, adding 2% GMS (glycerol monostearate)(Glycolube 825, manufactured by the Lonza Company) decreases the film haze from 16.9 to 15.3% when the carrier resin is a 37 MFR polypropylene homopolymer (HPP).
Concentrates with a twelve melt flow rate homopolymer as the carrier resin were made using the method described in Example 1. Different nucleators and acid scavengers and co-additives are used with the formulation shown in Table 7. The concentrates were let down into a twelve melt flow rate homopolymer and plaques were injection-molded. Plaque haze and Tc are shown in Table 7 as well.
The haze results show that the co-additives are effective in decreasing haze for Ca HHPA regardless of the acid scavenger used, for example, zinc stearate as shown in Example 3 above, calcium stearate, DHT-4A Hydrotalcite. Also, the co-additives help the haze performance of some other clarifiers such as AlpTBBA, NaBz etc. The amount of improvement varies depending on the clarifiers used and the co-additive loading.
However, the co-additives do not seem to improve haze performance for other known commercial nucleators such as;
1) Millad® 3988 (i.e. bis(3,4 dialkylbenzylidene sorbitol acetal); or
2) NA-21® (an organophosphate nucleating agent) sold by Asahi Denka of Japan. In fact, the co-additives of the invention had somewhat negative effects upon haze values for these known nucleating agents.
Given these chemical facts, it is unexpected that the co-additives of this invention, at appropriate concentrations, provide such tangible and significant benefits upon polymer haze and other polymer properties when these additives are used with HHPA-type nucleating agents.
“AlpTBBA” refers to aluminium para-tertiary butyl benzoic acid. “NA-11” is an organophosphate nucleating agent sold by Asahi Denka of Japan. “NaBz” refers to sodium benzozate made available through the Kalama Company. Here haze change is calculated as ((haze with co-additives)−(haze without co-additives))/(haze without co-additives). Tc change is calculated as ((Tc with co-additives)−(Tc without co-additives))/(Tc without co-additives).
Masterbatch concentrates made using Ca HHPA with a 12 MFR (melt flow rate) homopolymer as the carrier resin and different loadings of Ca HHPA were made using the method described in Example 1. The concentrates were let down into a twelve melt flow rate polypropylene homopolymer and an eleven melt flow rate random copolymer (RCP). Plaques were injection-molded and their haze and Tc are shown in Table 8.
It is understood by one of ordinary skill in the art that the present discussion is a description of exemplary embodiments only, and is not intended as limiting the broader aspects of the present invention, which broader aspects are embodied in the exemplary constructions. The invention is shown by example in the appended claims.
