USRE32325E - Tack-free polymer pellets - Google Patents
Tack-free polymer pellets Download PDFInfo
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- USRE32325E USRE32325E US06/853,342 US85334286A USRE32325E US RE32325 E USRE32325 E US RE32325E US 85334286 A US85334286 A US 85334286A US RE32325 E USRE32325 E US RE32325E
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- United States
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- ethylene
- vinyl acetate
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- copolymers
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- 239000008188 pellet Substances 0.000 title claims abstract description 82
- 229920000642 polymer Polymers 0.000 title claims abstract description 47
- 229920001577 copolymer Polymers 0.000 claims abstract description 79
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims abstract description 61
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000005977 Ethylene Substances 0.000 claims abstract description 50
- OXDXXMDEEFOVHR-CLFAGFIQSA-N (z)-n-[2-[[(z)-octadec-9-enoyl]amino]ethyl]octadec-9-enamide Chemical group CCCCCCCC\C=C/CCCCCCCC(=O)NCCNC(=O)CCCCCCC\C=C/CCCCCCCC OXDXXMDEEFOVHR-CLFAGFIQSA-N 0.000 claims abstract description 46
- 239000000654 additive Substances 0.000 claims abstract description 36
- 230000000996 additive effect Effects 0.000 claims abstract description 27
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 26
- 229920001897 terpolymer Polymers 0.000 claims abstract description 19
- 230000000903 blocking effect Effects 0.000 claims abstract description 17
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims abstract description 12
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims abstract description 10
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims description 17
- GUIUQQGIPBCPJX-CLFAGFIQSA-N (z)-n-[2-[[(z)-docos-13-enoyl]amino]ethyl]docos-13-enamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCC\C=C/CCCCCCCC GUIUQQGIPBCPJX-CLFAGFIQSA-N 0.000 claims description 7
- 239000001993 wax Substances 0.000 claims description 7
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 4
- 239000012188 paraffin wax Substances 0.000 claims description 4
- 238000005453 pelletization Methods 0.000 claims description 4
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 claims description 3
- NBEIUXCFFIDOCZ-CLFAGFIQSA-N n,n'-bis[(z)-docos-13-enyl]hexanediamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCCNC(=O)CCCCC(=O)NCCCCCCCCCCCC\C=C/CCCCCCCC NBEIUXCFFIDOCZ-CLFAGFIQSA-N 0.000 claims description 3
- FOZDUYPQLBGEKB-CLFAGFIQSA-N n,n'-bis[(z)-octadec-9-enyl]hexanediamide Chemical compound CCCCCCCC\C=C/CCCCCCCCNC(=O)CCCCC(=O)NCCCCCCCC\C=C/CCCCCCCC FOZDUYPQLBGEKB-CLFAGFIQSA-N 0.000 claims 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 4
- 238000012856 packing Methods 0.000 abstract 1
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 description 20
- 238000012360 testing method Methods 0.000 description 20
- 239000000155 melt Substances 0.000 description 18
- 239000000203 mixture Substances 0.000 description 13
- RKISUIUJZGSLEV-UHFFFAOYSA-N n-[2-(octadecanoylamino)ethyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCCCCCCCC RKISUIUJZGSLEV-UHFFFAOYSA-N 0.000 description 12
- 239000012141 concentrate Substances 0.000 description 11
- 229940037312 stearamide Drugs 0.000 description 10
- UAUDZVJPLUQNMU-UHFFFAOYSA-N Erucasaeureamid Natural products CCCCCCCCC=CCCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-UHFFFAOYSA-N 0.000 description 8
- 150000001408 amides Chemical class 0.000 description 8
- UAUDZVJPLUQNMU-KTKRTIGZSA-N erucamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-KTKRTIGZSA-N 0.000 description 8
- -1 for example Substances 0.000 description 8
- 238000013508 migration Methods 0.000 description 5
- 230000005012 migration Effects 0.000 description 5
- FATBGEAMYMYZAF-KTKRTIGZSA-N oleamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(N)=O FATBGEAMYMYZAF-KTKRTIGZSA-N 0.000 description 5
- FATBGEAMYMYZAF-UHFFFAOYSA-N oleicacidamide-heptaglycolether Natural products CCCCCCCCC=CCCCCCCCC(N)=O FATBGEAMYMYZAF-UHFFFAOYSA-N 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000004927 clay Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 229920003345 Elvax® Polymers 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- SYWDPPFYAMFYQQ-KTKRTIGZSA-N (z)-docos-13-en-1-amine Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCCN SYWDPPFYAMFYQQ-KTKRTIGZSA-N 0.000 description 2
- QGLWBTPVKHMVHM-KTKRTIGZSA-N (z)-octadec-9-en-1-amine Chemical compound CCCCCCCC\C=C/CCCCCCCCN QGLWBTPVKHMVHM-KTKRTIGZSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 101100020663 Neurospora crassa (strain ATCC 24698 / 74-OR23-1A / CBS 708.71 / DSM 1257 / FGSC 987) ppm-1 gene Proteins 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012943 hotmelt Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229920003145 methacrylic acid copolymer Polymers 0.000 description 2
- 229940117841 methacrylic acid copolymer Drugs 0.000 description 2
- 125000001117 oleyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])/C([H])=C([H])\C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000012748 slip agent Substances 0.000 description 2
- ALSTYHKOOCGGFT-KTKRTIGZSA-N (9Z)-octadecen-1-ol Chemical compound CCCCCCCC\C=C/CCCCCCCCO ALSTYHKOOCGGFT-KTKRTIGZSA-N 0.000 description 1
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical compound C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 description 1
- GVNWZKBFMFUVNX-UHFFFAOYSA-N Adipamide Chemical compound NC(=O)CCCCC(N)=O GVNWZKBFMFUVNX-UHFFFAOYSA-N 0.000 description 1
- 229920002799 BoPET Polymers 0.000 description 1
- DPUOLQHDNGRHBS-UHFFFAOYSA-N Brassidinsaeure Natural products CCCCCCCCC=CCCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-UHFFFAOYSA-N 0.000 description 1
- URXZXNYJPAJJOQ-UHFFFAOYSA-N Erucic acid Natural products CCCCCCC=CCCCCCCCCCCCC(O)=O URXZXNYJPAJJOQ-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- 229920003298 Nucrel® Polymers 0.000 description 1
- 101100386054 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) CYS3 gene Proteins 0.000 description 1
- 229920003182 Surlyn® Polymers 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- DPUOLQHDNGRHBS-KTKRTIGZSA-N erucic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-KTKRTIGZSA-N 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 230000008570 general process Effects 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 238000011545 laboratory measurement Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- OJURWUUOVGOHJZ-UHFFFAOYSA-N methyl 2-[(2-acetyloxyphenyl)methyl-[2-[(2-acetyloxyphenyl)methyl-(2-methoxy-2-oxoethyl)amino]ethyl]amino]acetate Chemical compound C=1C=CC=C(OC(C)=O)C=1CN(CC(=O)OC)CCN(CC(=O)OC)CC1=CC=CC=C1OC(C)=O OJURWUUOVGOHJZ-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229940055577 oleyl alcohol Drugs 0.000 description 1
- XMLQWXUVTXCDDL-UHFFFAOYSA-N oleyl alcohol Natural products CCCCCCC=CCCCCCCCCCCO XMLQWXUVTXCDDL-UHFFFAOYSA-N 0.000 description 1
- 229920006254 polymer film Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 101150035983 str1 gene Proteins 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
- C08K5/20—Carboxylic acid amides
Definitions
- This invention relates to tack-free polymer pellets, for example, ethylene/vinyl acetate copolymer pellets having good handling and block resistance characteristics.
- vinyl acetate copolymer includes both the dipolymers and the terpolymers of ethylene with vinyl acetate and with carbon monoxide.
- Ethylene/vinyl acetate (EVA) copolymers find wide commercial use in flexible, heat sealable, functional, and decorative hot-melt and solvent-applied coatings; as wax additives to impart toughness, flexibility, and adhesion; as blending resins to impart flexibility to brittle materials; and as a component of hot-melt and solvent-applied adhesives.
- Most commercial EVA dipolymers contain about 2-55% by weight of vinyl acetate.
- Terpolymers of ethylene with vinyl acetate and with carbon monoxide may contain about 18-40 weight percent of vinyl acetate and 2-12 weight percent of carbon monoxide. Dipolymers of ethylene with vinyl acetate are available, e.g., from E. I.
- Copolymer pellets the usual commercial form, at the same time increasingly tend to block, that is, to stick together and form large agglomerates, especially at somewhat elevated temperatures and under pressure of their own weight. This stickiness and the resulting blocking also increase with the copolymer's melt index, that is, with decreasing molecular weight.
- the partly neutralized, ionic form polymers are available from the same source under the name "Surlyn”.
- Copolymers of ethylene with methyl methacrylate can be made according to U.S. Pat. Nos. 3,287,335 to Stuetz, 3,658,741 to Knudson et al., and 3,949,016 to Agouri et al.
- Terpolymers of ethylene with n-butyl acrylate and carbon monoxide can be made following the techniques of the above Brubaker and Hammer patents.
- All polymers contemplated by this invention have a tendency to block in storage in pellet form but not all present significant handling difficulties or have poor flow properties. Poor flow properties are indicated by a low "stick temperature", which is determined in a standardized test developed by E. I. du Pont de Nemours and Company and described below. This test measures the tendency of polymer pellets to flow after holdup for a fixed time at a fixed temperature and pressure.
- the EVA copolymers of interest in the practice of the present invention have a stick temperature of at most about 40° C., while the other polymers of interest have a stick temperature of less than about 60° C. Polymers having stick temperatures above those temperatures do not usually have a tendency to block under normal handling and storage conditions.
- Slip (anti-tack) agents are offered commercially to improve the slip of polymer films and polymer processability. These include, for example, various fatty acid amides, which for the most part have been found to be ineffective or only marginally effective in reducing the tendency of EVA pellets to block but are quite effective in certain polymers of other types.
- pellets can be significantly reduced or the free-flowing properties of the pellets can be significantly improved by incorporating into the polymer material prior to pelletization about 500-10,000 parts per million (ppm), especially 1000-5000 ppm, based on the polymer weight of an additive selected from the group consisting of N,N'-ethylenebisoleamide, N,N'-ethylenebiserucamide, N,N'-diolelyladipamide, and N,N'-dierucyladipamide.
- ppm parts per million
- oleyl means cis-9-octadecenyl, C 8 H 17 CH ⁇ CH(CH 2 ) 7 CH 2 --; and the term “erucyl” means cis-13-docosenyl, C 8 H 17 CH ⁇ CH(CH 2 ) 11 CH 2 --.
- This nomenclature is generally used in the trade, for example, for oleyl alcohol, oleylamine, and erucylamine.
- N,N'-Ethylenebisoleamide, ##STR1## the preferred additive is available commercially from Carstab Corp. in Reading, Ohio, under the name “Advawax” 240; from Humko Sheffield Co., Memphis, Tenn., under the name “Kemamide” W-20; and from Glyco Chemical Co., Greenwich, Conn. under the name “Glycolube” VL.
- the commercial product has a melting range of 113°-118° C. and is difficultly soluble in most commercial solvents. It is recommended by its manufacturers as processing lubricant and antiblocking agent for various polymers and copolymers, especially as a slip agent for films. Its recommended level is 0.5-2%.
- N,N'-ethylenebiserucamide is made by heating 1,2-ethylenediamine with erucic acid, and the remaining two amides are made by heating either adipic acid or its dimethyl ester with at least two equivalents of either oleylamine or erucylamine.
- the adipamide thus has the formula ##STR2## where R is either the oleyl or the erucyl group.
- the additives of this invention have a particular ability to migrate within the polymer pellets to the surface or "bloom".
- the resulting layer of additive on the pellet surface is responsible for the improvement of pellet properties, but all four additives do not migrate at the same rates.
- N,N'-ethylenebisoleamide migrates to the surface of EVA copolymer pellets nearly instantaneously, while for N,N'-ethylenebiserucamide the rate of migration is much slower.
- N,N'-ethylenebisoleamide thus is truly outstanding in its effectiveness both to reduce blocking and to improve handling and free flow properties.
- all four additives are very effective.
- an antiblocking agent can be estimated in various manners, although the best test naturally is actual storage over an extended period. One also may judge the feel of pellets made from a polymer, which should be slippery, rather than tacky.
- Stick temperature is the most useful laboratory measurement for EVA copolymers having about 25-30% of vinyl acetate as well as for most other polymers. Although a low stick temperature does not always mean that pellets will have a tendency to block, a high (e.g., more than 60° C.) stick temperature normally suggests that the pellets will not have such tendency.
- Such high stick temperature polymers include, for example, polyethylene (over 70° C.) and ethylene/vinyl acetate copolymers of low melt index and/or low vinyl acetate content, such as:
- the amides of this invention can be added to the copolymers by any convenient technique, for example, in the melt, as a dry powder below its melting temperature, or as a concentrate in the same or any compatible polymer.
- the additive is thoroughly blended with the polymer, and then the polymer is extruded into pellets. It is preferred to use the additive at a level of 1000-5000 ppm, especially 2000-4000 ppm because at lower levels the improvement in slip properties may not be sufficiently attractive, while at higher levels other properties, for example, the adhesive properties of the copolymer may be adversely affected.
- pellets of copolymers of ethylene with vinyl acetate of varying vinyl acetate contents and melt indices containing 3500 ppm of N,N'-ethylenebisoleamide could be stored for several months and shipped in bulk in insulated hopper cars.
- EVA copolymers sometimes are formulated with a small amount, up to about 13%, of wax, especially paraffin wax. Addition of an amide of this invention to such wax-containing EVA copolymer also improves its resistance to blocking.
- the amount of the additive is, as before, based on the weight of the EVA copolymer.
- pellets of various other polymers can also often be improved by the addition of standard prior art slip agents, such as, e.g., stearamide or N,N'-ethylenebisstearamide, which are much less effective in pellets of the polymers envisaged by the present invention.
- the rate of migration of two of the additives of this invention to the pellet surface was determined as follows: a sample, 100-200 g of pellets freshly cut underwater at a temperature of about 10°-15° C. was centrifuged in a wire basket for 30 seconds to spin-dry the pellets. The centrifuge was allowed to come to a stop; the wire basket was removed and turned upside down. From the instant the pellets were cut to that point, the total time was under 2.5 minutes. An ethylene/vinyl acetate dipolymer containing about 40% of vinyl acetate without additive did not fall out of the basket, but a sample containing 1000 ppm of N,N'-ethylenebisoleamide was free-flowing.
- the stick temperature is defined as the maximum temperature at which all the polymer pellets empty from the test apparatus in less than one minute following holdup under fixed conditions.
- Polymer pellets are placed in a vertical tube having inside diameter of 3.9 cm and length of 23.2 cm lined loosely with a 5-mil (0.13 mm) thick film of poly(ethylene terephthalate) (Mylar ®500D, Du Pont Co.).
- a 4086 g weight is placed on top of the pellets, so that the downward pressure is 33.5 kPa.
- Hot air is passed upward through the pellets at .[.11 cm 3 /min.]. .Iadd.23.5 L/min .Iaddend.for 15 min; then air at ambient temperature is passed at .[.11 cm 3 /min.]. .Iadd.23.5 L/min .Iaddend.for 5 min.
- the weight is then removed, and the tube is inverted.
- the test is repeated at gradually increasing temperatures until a point is reached when only a portion of the copolymer pellets or none of the pellets flow out of the tube.
- the stick temperature is the last temperature at which all the pellets flowed out in less than one minute.
- the stick temperature of a given copolymer will to some extent depend on the size and shape of the pellets. Smaller, nonspherical pellets block more readily than larger, spherical pellets. Therefore, it is important to run a control experiment for each stick temperature determination. All the pellets used in the examples below weighed 1.8-3.2 g per 100 pellets and were "pillow"-shaped.
- the stick temperature is affected by other factors, such, for example, as the particular pelletizing technique and equipment and subsequent handling.
- the stick temperature of commercial pellets of a given polymer will usually be higher than that of laboratory-made pellets of the same polymer. All the pellets used in Examples 1-17 were made in the laboratory by repelletizing additive-free commercial polymer pellets.
- a 5% concentrate of N,N'-ethylenebisoleamide in an EVA dipolymer containing 28% of vinyl acetate and having a melt index of 150 g/10 min was prepared by melting the EVA dipolymer in a kettle at 220° C. under nitrogen and adding the required amount of the bisoleamide. The concentrate was heated with occasional stirring until homogeneous, poured into a slab, and ground.
- Blends of EVA dipolymer having a melt index of 150 g/10 min and 28% of vinyl acetate with the above concentrate, which contained 1000, 2000, and 3000 ppm of the bisoleamide were prepared and pelletized. They had a definite slippery feel.
- EVA dipolymers having melt indices, respectively, of 150, 43, and 25 g/10 min and a vinyl acetate content of 28%, each was blended with the bisoleamide/EVA concentrate of Example 1 to give bisoleamide concentrations of 3000, 4000, and 5000 ppm and pelletized as before. All these blends had a slippery feel, which the control EVA copolymers did not have.
- Blends of EVA dipolymer having a melt index of 150 g/10 min and containing 28% of vinyl acetate with the N,N'-ethylenebisoleamide/EVA concentrate of Example 1 to give, respectively, 3000 and 5000 ppm of the bisoleamide were prepared. All had the slippery feel, but their stick temperatures were close to the stick temperature of the control copolymer. Six samples containing three commercial N,N'-ethylenebisstearamides at the same levels also were prepared. They did not have a slippery feel, and their stick temperatures also were close to the controls. It is possible that a weighing error was made in the case of the bisoleamide, so that the actual amount of this additive was less than intended.
- a 25% concentrate of N,N'-ethylenebisoleamide in EVA dipolymer having a melt index of about 57 g/10 min and a vinyl acetate content of about 40% was prepared.
- EVA dipolymer having a melt index of about 57 g/10 min and a vinyl acetate content of about 40% was blended with the above 25% concentrate to give a homogeneous blend containing 5000 ppm of the bisoleamide.
- Samples, 908 g each, of this blend, of re-extruded EVA dipolymer, and of commercial, clay-coated EVA dipolymer having the same melt indices and vinyl acetate concentrations were air dried for 16 hr at 40° C.
- the bisoleamide-containing sample flowed freely from a small bag; the other two samples were severely blocked.
- Samples, 9.08 kg each, of EVA dipolymer having a melt index of about 57 g/10 min and containing about 40% of vinyl acetate were prepared. They contained, respectively, 1000, 3000, and 5000 ppm of N,N'-ethylenebisoleamide. Each sample was placed in a bag under four bags of EVA copolymer (106.6 kg total) and checked from time to determine if it was free flowing. After 15 months, all samples still were free flowing. This performance is quite remarkable because the untreated copolymer is very soft and sticky and blocks in a matter of hours under these conditions.
- EVA dipolymer (28% of vinyl acetate and melt index of 150 g/10 min) samples containing 3000 and 5000 ppm samples of commercial anti-tack additives were prepared.
- Their stick temperatures were 34°-35° C., compared with untreated EVA copolymer control's stick temperature of 30.1°-33.5° C.
- N,N'-ethylenebisoleamide did not raise the stick temperature as much as stearamide but was somewhat more effective than either erucamide or N,N'-ethylenebisstearamide. It will be remembered, however, that N,N'-ethylenebisoleamide migrated very fast in this polymer in the migration test described earlier in this disclosure.
- the cylinder is filled with EVA copolymer pellets, and a 2050 g weight is placed on top of the pellets, resulting in a pressure of 4.3 kPa.
- the filled cylinder is kept at 30° ⁇ 2° C. for a period of 8 hours.
- the cylinder is then carefully slipped off the column of pellets. If the copolymer maintains the shape of the cylinder, it is said to be blocked. If the copolymer pellets fall into a pile, it is said to be free flowing.
- EVA copolymer having a melt index of 57 g/10 min and a vinyl acetate content of about 40% was formulated with 1000 and 5000 ppm of each of the following:
- EVA dipolymer 50% of vinyl acetate; melt index of 57 g/10 min samples containing the indicated level of the indicated amide were prepared via 10 or 25% amide concentrates, as described in Examples 1 and 4, and pelletized:
- the stick temperature of the base EVA copolymer used in runs 1-3 was 30° C.
- the stick temperatures of the samples of runs 1-3 were as follows:
- Stick temperatures of certain untreated and treated commercial ethylene/vinyl acetate copolymer pellets were determined according to the above-described method.
- Elvax® is a trademark of E. I. du Pont de Nemours and Company for ethylene/vinyl acetate copolymers.
- the melt indices, the weight proportions of vinyl acetate in the copolymers, and the stick temperatures of the pellets are given below.
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- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Certain N,N'-ethylenebisamides and N,N'-diadipamides added to ethylene/vinyl acetate dipolymers, terpolymers of ethylene with carbon monoxide, copolymers of ethylene with methacrylic acid, copolymers of ethylene with methyl methacrylate, and terpolymers of ethylene with n-butyl acrylate and carbon monoxide remarkably reduce the tendency of polymer pellets to block. Free-flowing copolymer pellets can be handled without blocking and moved more quickly through the packing equipment and can be stored for extended periods without blocking. Copolymer pellets containing these additives can be packed into large containers and shipped without blocking. The preferred additive is N,N'-ethylenebisoleamide.
Description
.Iadd.This is a reissue of U.S. Pat. No. 4,510,281 which issued from Ser. No. 563,231 filed Dec. 19, 1983. .Iaddend..[.This.]. .Iadd.Ser. No. 563,231 .Iaddend.is a continuation-in-part of my application Ser. No. 472,644, filed Mar. 7, 1983, abandoned, which was a continuation-in-part of my application Ser. No. 348,012, filed Feb. 16, 1982 and now abandoned, which was a continuation-in-part of my application Ser. No. 267,082 filed May 26, 1981, now abandoned.
This invention relates to tack-free polymer pellets, for example, ethylene/vinyl acetate copolymer pellets having good handling and block resistance characteristics.
For the purpose of this invention, the term "vinyl acetate copolymer" includes both the dipolymers and the terpolymers of ethylene with vinyl acetate and with carbon monoxide.
Ethylene/vinyl acetate (EVA) copolymers find wide commercial use in flexible, heat sealable, functional, and decorative hot-melt and solvent-applied coatings; as wax additives to impart toughness, flexibility, and adhesion; as blending resins to impart flexibility to brittle materials; and as a component of hot-melt and solvent-applied adhesives. Most commercial EVA dipolymers contain about 2-55% by weight of vinyl acetate. Terpolymers of ethylene with vinyl acetate and with carbon monoxide may contain about 18-40 weight percent of vinyl acetate and 2-12 weight percent of carbon monoxide. Dipolymers of ethylene with vinyl acetate are available, e.g., from E. I. Du Pont de Nemours and Company, Wilmington, Del., under the trademark "Elvax"; the terpolymers with carbon monoxide can be made according to the teachings of U.S. Pat. Nos. 2,495,286 to Brubaker and 3,780,140 to Hammer. As the vinyl acetate content of the copolymer increases, the copolymer tends to become increasingly sticky. Copolymer pellets, the usual commercial form, at the same time increasingly tend to block, that is, to stick together and form large agglomerates, especially at somewhat elevated temperatures and under pressure of their own weight. This stickiness and the resulting blocking also increase with the copolymer's melt index, that is, with decreasing molecular weight. For example, for bulk EVA copolymer containing about 25-80% by weight of vinyl acetate, problems of this nature usually are encountered when the melt index exceeds 6 g/10 min. Yet, even those copolymers will have different flow properties and blocking tendencies, depending on their melt index values. For example, those copolymers having melt indices below about 50 g/10 min can be shipped in 26.6 kg bags or in 500 kg boxes without blocking. Those having melt indices above about 100 g/10 min cannot be shipped in large containers without risk of blocking but can be shipped in bags. Pellets of all these copolymers are free flowing and can be handled without difficulty. Higher vinyl acetate content copolymers, for example, those containing above 35 weight percent of vinyl acetate, are very sticky, have poor flow properties, and block even in regular size bags. Most higher vinyl acetate content EVA copolymers cannot be shipped in hopper cars. Other polymers which present difficulties of similar nature, but especially in shipping and storage, are copolymers of ethylene with methacrylic acid in which the carboxyl groups are either free or partly neutralized with metal ions, copolymers of ethylene with methyl methacrylate, and terpolymers of ethylene with n-butyl acrylate and carbon monoxide. Copolymers of ethylene with methacrylic acid are available from E. I. du Pont de Nemours and Company under the name "Nucrel". The partly neutralized, ionic form polymers (ionomers) are available from the same source under the name "Surlyn". Copolymers of ethylene with methyl methacrylate can be made according to U.S. Pat. Nos. 3,287,335 to Stuetz, 3,658,741 to Knudson et al., and 3,949,016 to Agouri et al. Terpolymers of ethylene with n-butyl acrylate and carbon monoxide can be made following the techniques of the above Brubaker and Hammer patents.
A particularly serious problem, which occurs in the pelletization and packaging equipment handling tacky polymers, especially certain grades of ethylene/vinyl acetate copolymers, is the tendency of the pellets to stick both to themselves and to the equipment, thus slowing down the process flow rate below its optimum value. If the pellets cannot be handled at normal process speeds or cannot be handled at all, the efficiency of the process suffers greatly.
All polymers contemplated by this invention have a tendency to block in storage in pellet form but not all present significant handling difficulties or have poor flow properties. Poor flow properties are indicated by a low "stick temperature", which is determined in a standardized test developed by E. I. du Pont de Nemours and Company and described below. This test measures the tendency of polymer pellets to flow after holdup for a fixed time at a fixed temperature and pressure. The EVA copolymers of interest in the practice of the present invention have a stick temperature of at most about 40° C., while the other polymers of interest have a stick temperature of less than about 60° C. Polymers having stick temperatures above those temperatures do not usually have a tendency to block under normal handling and storage conditions. Various techniques have been proposed to improve the flow properties of EVA copolymer pellets and to reduce their tendency to block, especially, coating the pellets with various materials such as clay, talc, or powdered polyethylene. See, for example, U.S. Pat. No. 3,528,841 to Donaldson et al. These methods are effective in varying degrees but have a shortcoming in that they do not always completely eliminate agglomeration of the pellets, which may occur before the coating is applied; and, further, the coating may not remain indefinitely attached to a pellet but may be lost in part in normal handling.
Slip (anti-tack) agents are offered commercially to improve the slip of polymer films and polymer processability. These include, for example, various fatty acid amides, which for the most part have been found to be ineffective or only marginally effective in reducing the tendency of EVA pellets to block but are quite effective in certain polymers of other types.
It has now been discovered that the blocking tendency of pellets of polymers selected from the group consisting of
(a) copolymers of ethylene with vinyl acetate containing about 18-55 weight percent of vinyl acetate,
(b) terpolymers of ethylene with vinyl acetate and carbon monoxide containing about 20-40 weight percent of vinyl acetate and 3-12 weight percent of carbon monoxide,
(c) copolymers of ethylene with methacrylic acid containing about 6-30 weight percent of methacrylic acid, wherein the carboxyl groups are neutralized with zinc ions to the extent of 0 to about 50%,
(d) copolymers of ethylene with methyl methacrylate containing about 18-40 weight percent of methyl methacrylate, and
(e) terpolymers of ethylene with n-butyl acrylate and carbon monoxide containing about 20-40 weight percent of n-butyl acrylate and 3-15 weight percent of carbon monoxide,
wherein the stick temperature of copolymers of ethylene with vinyl acetate is at most about 40° C., while the stick temperature of the other polymers is less than about 60° C.,
can be significantly reduced or the free-flowing properties of the pellets can be significantly improved by incorporating into the polymer material prior to pelletization about 500-10,000 parts per million (ppm), especially 1000-5000 ppm, based on the polymer weight of an additive selected from the group consisting of N,N'-ethylenebisoleamide, N,N'-ethylenebiserucamide, N,N'-diolelyladipamide, and N,N'-dierucyladipamide.
For the purpose of this invention (the term "oleyl" means cis-9-octadecenyl, C8 H17 CH═CH(CH2)7 CH2 --; and the term "erucyl" means cis-13-docosenyl, C8 H17 CH═CH(CH2)11 CH2 --. This nomenclature is generally used in the trade, for example, for oleyl alcohol, oleylamine, and erucylamine.
N,N'-Ethylenebisoleamide, ##STR1## the preferred additive, is available commercially from Carstab Corp. in Reading, Ohio, under the name "Advawax" 240; from Humko Sheffield Co., Memphis, Tenn., under the name "Kemamide" W-20; and from Glyco Chemical Co., Greenwich, Conn. under the name "Glycolube" VL. The commercial product has a melting range of 113°-118° C. and is difficultly soluble in most commercial solvents. It is recommended by its manufacturers as processing lubricant and antiblocking agent for various polymers and copolymers, especially as a slip agent for films. Its recommended level is 0.5-2%. The other additives can be made by known methods from readily available materials. Thus, N,N'-ethylenebiserucamide is made by heating 1,2-ethylenediamine with erucic acid, and the remaining two amides are made by heating either adipic acid or its dimethyl ester with at least two equivalents of either oleylamine or erucylamine. The adipamide thus has the formula ##STR2## where R is either the oleyl or the erucyl group.
It is believed that the additives of this invention have a particular ability to migrate within the polymer pellets to the surface or "bloom". The resulting layer of additive on the pellet surface is responsible for the improvement of pellet properties, but all four additives do not migrate at the same rates. It has been found that N,N'-ethylenebisoleamide migrates to the surface of EVA copolymer pellets nearly instantaneously, while for N,N'-ethylenebiserucamide the rate of migration is much slower. N,N'-ethylenebisoleamide thus is truly outstanding in its effectiveness both to reduce blocking and to improve handling and free flow properties. However, when time is not a critical consideration, all four additives are very effective.
The effectiveness of an antiblocking agent can be estimated in various manners, although the best test naturally is actual storage over an extended period. One also may judge the feel of pellets made from a polymer, which should be slippery, rather than tacky. Stick temperature is the most useful laboratory measurement for EVA copolymers having about 25-30% of vinyl acetate as well as for most other polymers. Although a low stick temperature does not always mean that pellets will have a tendency to block, a high (e.g., more than 60° C.) stick temperature normally suggests that the pellets will not have such tendency. Such high stick temperature polymers include, for example, polyethylene (over 70° C.) and ethylene/vinyl acetate copolymers of low melt index and/or low vinyl acetate content, such as:
______________________________________
Wt % VA Melt Index
Stick temp., °C.
______________________________________
8.4 1.8 >70
12 0.35 70
15 8 61
______________________________________
For high vinyl acetate content copolymers and other sticky copolymers a laboratory blocking test has been devised because the stick temperature of those polymers is so low that a meaningful value cannot be obtained. Improvement of the handling and packaging throughput in actual production also is an excellent indication of good slip properties, especially for these higher vinyl acetate content copolymers.
The amides of this invention can be added to the copolymers by any convenient technique, for example, in the melt, as a dry powder below its melting temperature, or as a concentrate in the same or any compatible polymer. The additive is thoroughly blended with the polymer, and then the polymer is extruded into pellets. It is preferred to use the additive at a level of 1000-5000 ppm, especially 2000-4000 ppm because at lower levels the improvement in slip properties may not be sufficiently attractive, while at higher levels other properties, for example, the adhesive properties of the copolymer may be adversely affected.
It has been found that pellets of copolymers of ethylene with vinyl acetate of varying vinyl acetate contents and melt indices containing 3500 ppm of N,N'-ethylenebisoleamide could be stored for several months and shipped in bulk in insulated hopper cars.
EVA copolymers sometimes are formulated with a small amount, up to about 13%, of wax, especially paraffin wax. Addition of an amide of this invention to such wax-containing EVA copolymer also improves its resistance to blocking. The amount of the additive is, as before, based on the weight of the EVA copolymer.
While the additives of this invention have the unique ability of reducing blocking and improving the free-flowing properties of pellets of specific polymers recited in this specification and in the claims, they are also effective in various other polymers. However, pellets of various other polymers can also often be improved by the addition of standard prior art slip agents, such as, e.g., stearamide or N,N'-ethylenebisstearamide, which are much less effective in pellets of the polymers envisaged by the present invention.
This invention is now illustrated by the following examples of certain representative embodiments thereof, where all the parts, proportions, and percentages are by weight. All the blends were prepared in an extruder and underwater melt cut to pelletize the product.
The rate of migration of two of the additives of this invention to the pellet surface was determined as follows: a sample, 100-200 g of pellets freshly cut underwater at a temperature of about 10°-15° C. was centrifuged in a wire basket for 30 seconds to spin-dry the pellets. The centrifuge was allowed to come to a stop; the wire basket was removed and turned upside down. From the instant the pellets were cut to that point, the total time was under 2.5 minutes. An ethylene/vinyl acetate dipolymer containing about 40% of vinyl acetate without additive did not fall out of the basket, but a sample containing 1000 ppm of N,N'-ethylenebisoleamide was free-flowing. For the same concentration of N,N'-ethylenebiserucamide, the migration time to achieve free-flow of the pellets from the basket was 45 minutes. At the 3000 ppm level, both the bisoleamide- and the bis-erucamide-containing pellets were free-flowing as soon as the wire basket was removed. Similarly, an ethylene/vinyl acetate/carbon monoxide terpolymer containing 28% of vinyl acetate and 9% of carbon monoxide (melt index of 35 g/10 min) was not free-flowing without an additive. A sample containing 4000 ppm of N,N'-ethylenebisoleamide was free-flowing as soon as the wire basket was removed and turned upside down. When N,N'-ethylenebiserucamide was used instead, the additive migration time was 30 minutes.
The stick temperature is defined as the maximum temperature at which all the polymer pellets empty from the test apparatus in less than one minute following holdup under fixed conditions.
Polymer pellets are placed in a vertical tube having inside diameter of 3.9 cm and length of 23.2 cm lined loosely with a 5-mil (0.13 mm) thick film of poly(ethylene terephthalate) (Mylar ®500D, Du Pont Co.). A 4086 g weight is placed on top of the pellets, so that the downward pressure is 33.5 kPa. Hot air is passed upward through the pellets at .[.11 cm3 /min.]. .Iadd.23.5 L/min .Iaddend.for 15 min; then air at ambient temperature is passed at .[.11 cm3 /min.]. .Iadd.23.5 L/min .Iaddend.for 5 min. The weight is then removed, and the tube is inverted. Time during which all the pellets flow out of the tube is noted. The test is repeated at gradually increasing temperatures until a point is reached when only a portion of the copolymer pellets or none of the pellets flow out of the tube. The stick temperature is the last temperature at which all the pellets flowed out in less than one minute.
The stick temperature of a given copolymer will to some extent depend on the size and shape of the pellets. Smaller, nonspherical pellets block more readily than larger, spherical pellets. Therefore, it is important to run a control experiment for each stick temperature determination. All the pellets used in the examples below weighed 1.8-3.2 g per 100 pellets and were "pillow"-shaped.
In addition, the stick temperature is affected by other factors, such, for example, as the particular pelletizing technique and equipment and subsequent handling. Thus, the stick temperature of commercial pellets of a given polymer will usually be higher than that of laboratory-made pellets of the same polymer. All the pellets used in Examples 1-17 were made in the laboratory by repelletizing additive-free commercial polymer pellets.
A 5% concentrate of N,N'-ethylenebisoleamide in an EVA dipolymer containing 28% of vinyl acetate and having a melt index of 150 g/10 min was prepared by melting the EVA dipolymer in a kettle at 220° C. under nitrogen and adding the required amount of the bisoleamide. The concentrate was heated with occasional stirring until homogeneous, poured into a slab, and ground.
Blends of EVA dipolymer having a melt index of 150 g/10 min and 28% of vinyl acetate with the above concentrate, which contained 1000, 2000, and 3000 ppm of the bisoleamide were prepared and pelletized. They had a definite slippery feel.
The following stick temperatures were obtained:
______________________________________
EVA copolymer control
30.1° C.
1000 ppm blend 36.7° C.
2000 ppm blend 36.5° C.
3000 ppm blend 40.7° C.
______________________________________
EVA dipolymers having melt indices, respectively, of 150, 43, and 25 g/10 min and a vinyl acetate content of 28%, each was blended with the bisoleamide/EVA concentrate of Example 1 to give bisoleamide concentrations of 3000, 4000, and 5000 ppm and pelletized as before. All these blends had a slippery feel, which the control EVA copolymers did not have.
The following stick temperaturs were obtained for the 3000 ppm blends and for the control copolymers:
______________________________________
EVA dipolymer stick temperature
melt index control blend
______________________________________
150 32° C.
34° C.
43 30° C.
36° C.
25 30° C.
38° C.
______________________________________
Blends of EVA dipolymer having a melt index of 150 g/10 min and containing 28% of vinyl acetate with the N,N'-ethylenebisoleamide/EVA concentrate of Example 1 to give, respectively, 3000 and 5000 ppm of the bisoleamide were prepared. All had the slippery feel, but their stick temperatures were close to the stick temperature of the control copolymer. Six samples containing three commercial N,N'-ethylenebisstearamides at the same levels also were prepared. They did not have a slippery feel, and their stick temperatures also were close to the controls. It is possible that a weighing error was made in the case of the bisoleamide, so that the actual amount of this additive was less than intended.
A 25% concentrate of N,N'-ethylenebisoleamide in EVA dipolymer having a melt index of about 57 g/10 min and a vinyl acetate content of about 40% was prepared.
EVA dipolymer having a melt index of about 57 g/10 min and a vinyl acetate content of about 40% was blended with the above 25% concentrate to give a homogeneous blend containing 5000 ppm of the bisoleamide. Samples, 908 g each, of this blend, of re-extruded EVA dipolymer, and of commercial, clay-coated EVA dipolymer having the same melt indices and vinyl acetate concentrations were air dried for 16 hr at 40° C. The bisoleamide-containing sample flowed freely from a small bag; the other two samples were severely blocked.
Samples, 9.08 kg each, of EVA dipolymer having a melt index of about 57 g/10 min and containing about 40% of vinyl acetate were prepared. They contained, respectively, 1000, 3000, and 5000 ppm of N,N'-ethylenebisoleamide. Each sample was placed in a bag under four bags of EVA copolymer (106.6 kg total) and checked from time to determine if it was free flowing. After 15 months, all samples still were free flowing. This performance is quite remarkable because the untreated copolymer is very soft and sticky and blocks in a matter of hours under these conditions.
EVA dipolymer (28% of vinyl acetate and melt index of 150 g/10 min) samples containing 3000 and 5000 ppm samples of commercial anti-tack additives were prepared. The samples containing two commercial N,N'-ethylenebisoleamides, "Advawax" 240 and "Glycolube" VL, had a slippery feel. Their stick temperatures were 34°-35° C., compared with untreated EVA copolymer control's stick temperature of 30.1°-33.5° C. Samples containing three commercial makes of N,N'-ethylenebisstearamide, "Advawax" 275, 280, and 290 (Carstab Corp.), "Kemamide" W-40 (HumKo Sheffield Co., Memphis, Tenn.), and "Acrowax" C (Glyco Chemical Co., Greenwich, Conn.); oleamide, "Kemamide" U; and two materials of unknown composition, "Paricin" 285 (NL Industries, New York, N.Y.), and "Rosswax" (Frank B. Ross Co., Jersey City, N.Y.) were not slippery to the touch (did not bloom), and their stick temperatures were 29°-31° C.
EVA dipolymer having a melt index of 43 g/10 min and containing 33% of vinyl acetate and EVA dipolymer having a melt index of 400 g/10 min and containing 28% of vinyl acetate, each also containing, respectively, 1000, 3000, and 5000 ppm of N,N'-ethylenebisoleamide had a slippery feel, and their stick temperatures were moderately increased, as shown:
______________________________________
EVA Copolymer bisoleamide
Stick Temp
Vinyl Acetate, %
ppm °C.
______________________________________
33 -- 26
1000 29
3000 31
5000 31
28 -- 25
1000 30
3000 30
5000 31
______________________________________
An industrial batch, 18160 kg, of EVA copolymer having a melt index of 57 g/10 min and containing 40% of vinyl acetate blended with N,N'-ethylenebisoleamide to a level of 4000 ppm of the bisoleamide was prepared and pelletized. It was found that N,N'-ethylenebisoleamide migrated to the surface of the pellets and formed a protective coating in a matter of seconds. These coated pellets could be transferred, purged and blended without blocking, and their transfer rate was about 20% higher than that of clay-coated pellets. They continued to flow freely after 6 weeks at 32° C. Clay-coated copolymer pellets block in less than 30 days under these conditions.
A plant run copolymer containing 90% of ethylene and 10% of methacrylic acid (melt index of 500 g/10 min) was blended with the indicated amounts of test amides. The compositions and stick temperatures of the samples are given in the table below. It can be seen that N,N'-ethylenebisoleamide provides a meaningful increase of stick temperature.
______________________________________
Additive (ppm) Stick Temp., °C.
______________________________________
Control 46
5000 erucamide 43
5000 stearamide 48
5000 N,N'--ethylenebisstearamide
48
1000 N,N'--ethylenebisoleamide
49
5000 N,N'--ethylenebisoleamide
55
______________________________________
The same test was performed with an ethylene/methacrylic acid copolymer containing 15% of methacrylic acid. Again, N,N'-ethylenebisoleamide provided a significant increase of stick temperature, as can be seen from the following table:
______________________________________
Additive (ppm) Stick Temp., °C.
______________________________________
Control 34
5000 erucamide 36
5000 stearamide 42
5000 N,N'--ethylenebisstearamide
42
1000 N,N'--ethylenebisoleamide
34
5000 N,N'--ethylenebisoleamide
47
______________________________________
The same test was performed with an ethylene/methacrylic acid copolymer containing 15% of methacrylic acid and 20% neutralized with Zn++ ions. The copolymer had a melt index of 12 g/10 min. Here again, the most significant improvement of stick temperature was obtained with N,N'-ethylenebisoleamide. The experimental results are provided in the table below.
______________________________________
Additive (ppm) Stick Temp., °C.
______________________________________
Control 30
5000 erucamide 31
5000 stearamide 40
5000 N,N'--ethylenebisstearamide
41
1000 N,N'--ethylenebisoleamide
40
5000 N,N'--ethylenebisoleamide
48
______________________________________
A similar test was performed with an ethylene/methyl methacrylate copolymer containing 20% of methyl methacrylate. Its melt index was 3.2 g/10 min. The results are tabulated below.
______________________________________
Additive (ppm) Stick Temp., °C.
______________________________________
Control 53
5000 erucamide 55
5000 stearamide 52
5000 N,N'--ethylenebisoleamide
60
______________________________________
A similar test was performed with a terpolymer of ethylene with vinyl acetate (28%) and carbon monoxide (9%), which had a melt index of 35 g/10 min. The results are given in the following table:
______________________________________
Additive (ppm) Stick Temp., °C.
______________________________________
Control 30
5000 erucamide 30
5000 stearamide 37
5000 N,N'--ethylenebisstearamide
30
1000 N,N'--ethylenebisoleamide
33
3000 N,N'--ethylenebisoleamide
33
5000 N,N'--ethylenebisoleamide
33
______________________________________
It can be seen that in this test N,N'-ethylenebisoleamide did not raise the stick temperature as much as stearamide but was somewhat more effective than either erucamide or N,N'-ethylenebisstearamide. It will be remembered, however, that N,N'-ethylenebisoleamide migrated very fast in this polymer in the migration test described earlier in this disclosure.
Highly tacky polymers cannot be evaluated satisfactorily in the stick temperature test. Therefore, a blocking test was developed for evaluation of the effectiveness of anti-tack agent candidates.
A hollow metal cylinder, 7.5 cm in inside diameter and 10 cm in length, lined with poly(ethylene terephthalate) film, is placed on a thin metal plate covered with poly(ethylene terephthalate film). The cylinder is filled with EVA copolymer pellets, and a 2050 g weight is placed on top of the pellets, resulting in a pressure of 4.3 kPa. The filled cylinder is kept at 30°±2° C. for a period of 8 hours. The cylinder is then carefully slipped off the column of pellets. If the copolymer maintains the shape of the cylinder, it is said to be blocked. If the copolymer pellets fall into a pile, it is said to be free flowing.
EVA copolymer having a melt index of 57 g/10 min and a vinyl acetate content of about 40% was formulated with 1000 and 5000 ppm of each of the following:
"Kemamide" S (stearamide) and
"Kemamide" E (erucamide)
All samples were sticky (similar to wet snow). Samples containing 1000 ppm of additive blocked in the bags and were not subjected to the blocking test. Both 5000 ppm samples blocked in the test.
The following EVA dipolymer (40% of vinyl acetate; melt index of 57 g/10 min) samples containing the indicated level of the indicated amide were prepared via 10 or 25% amide concentrates, as described in Examples 1 and 4, and pelletized:
______________________________________
Amide
Run Concentration,
No. Type ppm
______________________________________
1 stearamide 10000
2 " 15000
3 N--oleyl-N--palmitamide
1000
4 " 5000
5 oleamide 1000
6 " 5000
7 N,N'--ethylenebisstearamide
1000
8 " 5000
9 N,N'--ethylenebisoleamide
1000
10 " 5000
11 oleamide 1000
12 " 5000
13 " 3000
14 N,N'--ethylenebisoleamide
3000
15 N,N'--ethylenebisoleamide*
3000
16 erucamide 1500
stearamide 375
17 N,N'--ethylenebisoleamide*
1875
18 N,N'--ethylenebisoleamide*
500
______________________________________
*Prepared from a 25% concentrate in EVA copolymer having a melt index of
150 g/10 min and a vinyl acetate content of 28%
During the preparation of the above samples, each was observed on the drying screen immediately after pellet formation for pellet flowability. The pellets made in the following runs were free-flowing:
1, 2, 9, 10, 14, 15, 17, and 18.
In the blocking test described above in Example 14, the following samples remained free-flowing:
9, 10, 14, 15 and 17.
The remaining samples blocked. A commercial sample of clay-coated EVA copolymer also blocked in this test.
The following EVA copolymer (28% of vinyl acetate, melt index of 150 g/10 min) samples were prepared as described in Example 15:
______________________________________
Amide
Run Concentration,
No. Type ppm
______________________________________
1 oleamide 3000
2 N,N'--ethylenebisoleamide*
3000
3 N,N'--ethylenebisoleamide
3000
______________________________________
*Prepared from a 10% concentrate in EVA copolymer having a melt index of
400 g/10 min
The stick temperature of the base EVA copolymer used in runs 1-3 was 30° C. The stick temperatures of the samples of runs 1-3 were as follows:
______________________________________ Run Stick Temperature, °C. ______________________________________ 1 29 2 36 3 34 ______________________________________ IT can be seen that oleamide was a poor performer in this test, while N,N'-ethylenebisoleamide was a good performer.
The stick temperatures of untreated pellets of a terpolymer of ethylene with n-butyl acrylate (30%) and carbon monoxide (10%) made by the general process of U.S. Pat. No. 3,780,140 to Hammer, which had a melt index of 5.0 g/10 min, as well as of pellets of the same terpolymer containing varying levels of N,N'-ethylenebisoleamide were determined as follows:
______________________________________
Additive level (ppm)
Stick Temperature, °C.
______________________________________
-- (control) 25
1000 26
3000 29
5000 29
______________________________________
Stick temperatures of certain untreated and treated commercial ethylene/vinyl acetate copolymer pellets were determined according to the above-described method. Elvax® is a trademark of E. I. du Pont de Nemours and Company for ethylene/vinyl acetate copolymers. The melt indices, the weight proportions of vinyl acetate in the copolymers, and the stick temperatures of the pellets are given below.
______________________________________
Commercial Elvax ®
Resin Designation Stick Temperature
Untreated
Treated MI VA Untreated
Treated
______________________________________
40 P 40 W 57 40 <24.sup.1
34.sup.2
220 220 W 150 28 40 46.sup.3
210 210 W 400 28 34 40.sup.3
150 150 W 43 33 31 38.sup.3
______________________________________
.sup.1 Claycoated
.sup.2 4000 ppm N,N--ethylenebisoleamide
.sup.3 3000 ppm N,N'--ethylenebisoleamide
Claims (14)
1. A pellet of a polymer selected from the group consisting of:
(a) copolymers of ethylene with vinyl acetate in which the amount of vinyl acetate is about 18-55 weight percent,
(b) terpolymers of ethylene with vinyl acetate and carbon monoxide in which the amount of vinyl acetate is about 20-40 weight percent and the amount of carbon monoxide is about 3-12 weight percent,
(c) copolymers of ethylene with methacrylic acid in which the amount of methacrylic acid is about 6-30 weight percent, the carboxyl groups of the copolymers being neutralized with zinc ions to an extent of 0 to about 50%,
(d) copolymers of ethylene with methyl methacrylate in which the amount of methyl methacrylate is about 18-40 weight percent, and
(e) terpolymers of ethylene with n-butyl acrylate and carbon monoxide in which the amount of n-butyl acrylate is about 20-40 weight percent, and the amount of carbon monoxide is about 3-15 weight percent;
the stick temperature of the copolymers of paragraph (a) being at most about 40° C., and the stick temperature of the polymers of paragraphs (b) through (e) being below about 60° C.;
said pellet having incorporated into the copolymer an effective amount from about 500 to about 10000 parts by weight per million parts by weight of the polymer (ppm) of an additive selected from the group consisting of N,N'-ethylenebisoleamide, N,N'-ethylenebiserucamide, N,N'-dioleyladipamide, and N,N'-dierucyladipamide to reduce the tackiness of the pellet;
with the proviso that when the polymer in the pellet is a dipolymer with vinyl acetate, it may also contain blended therewith wax in an amount of up to about 13% of the copolymer weight.
2. A pellet of claim 1 wherein the polymer is a dipolymer of ethylene with vinyl acetate or terpolymer of ethylene with vinyl acetate and carbon monoxide.
3. A pellet of claim 2 wherein the additive is N,N'-ethylenebisoleamide.
4. a pellet of claim 3 wherein the polymer is a dipolymer of ethylene with vinyl acetate.
5. A pellet of claim 1 wherein the amount of the additive is 1000-5000 ppm.
6. A pellet of claim 5 wherein the amount of the additive is 2000 to 4000 ppm.
7. A pellet of claim 1 wherein the additive is N,N'-ethylenebisoleamide.
8. A pellet of claim 1 wherein the wax is paraffin wax.
9. A method of reducing the tack and blocking tendency of polymers selected from the group consisting of:
(a) dipolymers of ethylene with vinyl acetate in which the amount of vinyl acetate is about 18-55 weight percent,
(b) terpolymers of ethylene with vinyl acetate and carbon monoxide in which the amount of vinyl acetate is about 20-40 weight percent and the amount of carbon monoxide is about 3-12 weight percent,
(c) copolymers of ethylene with methacrylic acid in which the amount of methacrylic acid is about 6-30 weight percent, the carboxyl group of the copolymers being neutralized with zinc ions to an extent of 0 to about 50%,
(d) copolymers of ethylene with methyl methacrylate in which the amount of methyl methacrylate is about 18-40 weight percent, and
(e) terpolymers of ethylene with n-butyl acrylate and carbon monoxide, in which the amount of n-butyl acrylate is about 20-40 weight percent, and the amount of carbon monoxide is about 3-15 weight percent;
the stick temperature of the polymers of paragraph (a) being at most about 40° C., and the stick temperature of the polymers of paragraphs (b) through (e) being below about 60° C.;
said method comprising incorporating into the polymer prior to pelletization an effective amount of about 500 to about 10000 parts by weight per million parts by weight (ppm) of an additive selected from the group consisting of N,N'-ethylenebisoleamide, N,N'-ethylenebiserucamide, N,N'-dioleyladipamide, and N,N'dierucyladipamide;
with the proviso that when the polymer in the pellet is a dipolymer with vinyl acetate, it may also contain blended therewith wax in an amount of up to about 13% of the copolymer weight.
10. The method of claim 9 wherein the amount of the additive is 1000-5000 ppm.
11. The method of claim 10 wherein the amount of the additive is 2000-4000 ppm.
12. The method of claim 9 wherein the polymer is a dipolymer of ethylene with vinyl acetate or terpolymer of ethylene with vinyl acetate and carbon monoxide, and the additive is N,N'-ethylenebisoleamide.
13. The method of claim 9 wherein the wax is paraffin wax.
14. The method of claim 12 wherein paraffin wax is present in the pellets.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/853,342 USRE32325E (en) | 1981-05-26 | 1986-04-17 | Tack-free polymer pellets |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US26708281A | 1981-05-26 | 1981-05-26 | |
| US06/853,342 USRE32325E (en) | 1981-05-26 | 1986-04-17 | Tack-free polymer pellets |
Related Parent Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06472644 Continuation-In-Part | 1983-03-07 | ||
| US06/563,231 Reissue US4510281A (en) | 1981-05-26 | 1983-12-19 | Tack-free polymer pellets |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USRE32325E true USRE32325E (en) | 1987-01-06 |
Family
ID=26952200
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/853,342 Expired - Fee Related USRE32325E (en) | 1981-05-26 | 1986-04-17 | Tack-free polymer pellets |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USRE32325E (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5175049A (en) * | 1989-04-27 | 1992-12-29 | The Dow Chemical Company | Polyolefin laminate cling films |
| US5286771A (en) * | 1992-05-12 | 1994-02-15 | E. I. Du Pont De Nemours And Company | Ethylene/acid copolymers with improved block resistance |
| US5399401A (en) * | 1992-10-19 | 1995-03-21 | E. I. Du Pont De Nemours And Company | Flexible, low haze chlorine-free ethylene copolymer article |
| US5661201A (en) * | 1994-04-20 | 1997-08-26 | Elf Atochem S.A. | Thermoplastic film capable of being sealed by high frequency current |
| US5695881A (en) * | 1995-11-01 | 1997-12-09 | At Plastics Inc. | Coated soft copolymers suitable for bulk shipment and storage |
| US6255368B1 (en) * | 1997-08-29 | 2001-07-03 | Kevin P. Gohr | Plastic wood-fiber pellets |
| US6361844B1 (en) | 1999-01-27 | 2002-03-26 | David T. Ou-Yang | Release article and adhesive article comprising the release article |
| US6465091B1 (en) | 2000-03-27 | 2002-10-15 | 3M Innovative Properties Company | Release article and adhesive article containing a polymeric release material |
| US6528174B1 (en) * | 1996-10-04 | 2003-03-04 | E. I. Du Pont De Nemours & Co. | Ethylene vinyl acetate compositions and film and methods related thereto |
| US6616968B2 (en) | 1999-02-19 | 2003-09-09 | Equistar Chemicals, Lp | Coated polymeric particles having improved anti-block characteristics, method of making such particles, and apparatus therefor |
| US20040143034A1 (en) * | 2001-05-09 | 2004-07-22 | Hartmut Primke | Hot-melt adhesive in particulate form |
| US20050065250A1 (en) * | 2003-09-24 | 2005-03-24 | Davis Donna Sue | Inorganic antiblock |
| US20100286766A1 (en) * | 2009-05-08 | 2010-11-11 | Greatbatch, Ltd. | Surface modification for coating |
| US9903086B2 (en) * | 2015-07-16 | 2018-02-27 | Foundation Technologies, Inc. | Friction reduction pile jacket with slip additive |
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|---|---|---|---|---|
| US3165492A (en) * | 1959-10-14 | 1965-01-12 | Eastman Kodak Co | Solid poly-alpha-mono-olefin containing n, n'-alkylene bis amides |
| US3407162A (en) * | 1966-03-30 | 1968-10-22 | Chevron Res | Hot tack high gloss wax compositions |
| US3645822A (en) * | 1969-01-31 | 1972-02-29 | Dow Chemical Co | Method for providing multilayer films having improved slip properties |
| US3969304A (en) * | 1974-11-27 | 1976-07-13 | National Distillers And Chemical Corporation | Ethylene polymer films |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3165492A (en) * | 1959-10-14 | 1965-01-12 | Eastman Kodak Co | Solid poly-alpha-mono-olefin containing n, n'-alkylene bis amides |
| US3407162A (en) * | 1966-03-30 | 1968-10-22 | Chevron Res | Hot tack high gloss wax compositions |
| US3645822A (en) * | 1969-01-31 | 1972-02-29 | Dow Chemical Co | Method for providing multilayer films having improved slip properties |
| US3969304A (en) * | 1974-11-27 | 1976-07-13 | National Distillers And Chemical Corporation | Ethylene polymer films |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5175049A (en) * | 1989-04-27 | 1992-12-29 | The Dow Chemical Company | Polyolefin laminate cling films |
| US5286771A (en) * | 1992-05-12 | 1994-02-15 | E. I. Du Pont De Nemours And Company | Ethylene/acid copolymers with improved block resistance |
| US5399401A (en) * | 1992-10-19 | 1995-03-21 | E. I. Du Pont De Nemours And Company | Flexible, low haze chlorine-free ethylene copolymer article |
| US5661201A (en) * | 1994-04-20 | 1997-08-26 | Elf Atochem S.A. | Thermoplastic film capable of being sealed by high frequency current |
| US5695881A (en) * | 1995-11-01 | 1997-12-09 | At Plastics Inc. | Coated soft copolymers suitable for bulk shipment and storage |
| US6528174B1 (en) * | 1996-10-04 | 2003-03-04 | E. I. Du Pont De Nemours & Co. | Ethylene vinyl acetate compositions and film and methods related thereto |
| US20030049478A1 (en) * | 1996-10-04 | 2003-03-13 | Vogel Randall Allen | Process for preparing improved ethylene vinyl acetate compositions and films |
| US6255368B1 (en) * | 1997-08-29 | 2001-07-03 | Kevin P. Gohr | Plastic wood-fiber pellets |
| US6361844B1 (en) | 1999-01-27 | 2002-03-26 | David T. Ou-Yang | Release article and adhesive article comprising the release article |
| US6616968B2 (en) | 1999-02-19 | 2003-09-09 | Equistar Chemicals, Lp | Coated polymeric particles having improved anti-block characteristics, method of making such particles, and apparatus therefor |
| US6465091B1 (en) | 2000-03-27 | 2002-10-15 | 3M Innovative Properties Company | Release article and adhesive article containing a polymeric release material |
| US20040143034A1 (en) * | 2001-05-09 | 2004-07-22 | Hartmut Primke | Hot-melt adhesive in particulate form |
| US7267878B2 (en) | 2001-05-09 | 2007-09-11 | Henkel Kommanditgesellschaft Auf Aktien (Henkel Kgaa) | Hot-melt adhesive in particulate form |
| US20050065250A1 (en) * | 2003-09-24 | 2005-03-24 | Davis Donna Sue | Inorganic antiblock |
| US20100286766A1 (en) * | 2009-05-08 | 2010-11-11 | Greatbatch, Ltd. | Surface modification for coating |
| US9289540B2 (en) | 2009-05-08 | 2016-03-22 | Greatbatch Ltd. | Surface modification for coating |
| US9903086B2 (en) * | 2015-07-16 | 2018-02-27 | Foundation Technologies, Inc. | Friction reduction pile jacket with slip additive |
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