CA1203933A - Surfactant-containing filled and plasticized thermoplastic compositions based on ethylene interpolymers - Google Patents

Abstract

TITLE
SURFACTANT-CONTAINING FILLED AND PLASTICIZED
THERMOPLASTIC COMPOSITIONS BASED ON
ETHYLENE INTERPOLYMERS
ABSTRACT OF THE DISCLOSURE
Filled thermoplastic compositions having enhanced elongation and useful, e.g., as sound-deadening sheeting for automotive carpet, are obtained by blending about 0-50% by weight of an ethylene interpolymer, such as ethylene/vinyl ester, ethylene/unsaturated mono- or dicarboxylic acids or esters of said unsaturated acids, etc.; 0-20% by weight of a plasticizer selected from the group consisting of processing oils, epoxidized oils, polyesters, polyethers, polyether esters and combinations thereof; about 40-90% by weight of filler; from about 0.05 to about 5.0% by weight of at least one surface active agent such as sulfonates, sulfates, phosphates, etc.; and optionally, modifying resins, such as tackifiers and certain ethylene and propylene homo- and copolymers.

Description

3~33 TITLE
SURFACTANT-CONTAINING FILLED AND PLASTICIZED
THERMOPLASTIC COMPOSITIONS BASED ON
ETHYLENE INTERPOLYMERS
_ACKGROUND OF THE INVENTION
Field of the Invention This invention relates -to filled and plas-ticized blends of ethylene interpolymers and more specifically it relates to such blends modified with surface active agents.
Description of the Prior Art Japanese Patent Publication 23128~1980 of Yamaka Seito KK, published 19~0 June 20,describes filled ethylene copolymer compositions (in particular, ethylene/ethyl acrylate; 5 to 30~ ethyl acrylate) with 100 to 500 parts by weight of an inorganic filler which has been surface-treated with a titanate-based coupling agent (e.g. isopropyl triisostearyl titanate). The compositions which result are claimed to provide notice-ably improved tensile strength, elongation at break, stretchability, and heat shrinkage, vs. compositions which do not employ titanate-based coupling agents.
Japanese Patent Publication 21052-1980 of Watanabe et al, published 1980 June 6, describes a filled polymer composition which uses as raw materials a polymer mixture of (a) ethylene/vinyl acetate (EVA) copolymer, which contains from 10 to 28~ vinyl acetate;
(b) rubber, preferably chloroprene rubber or ethylene-propylene rubber, and (c) filler. The ratio of EVA:
rubber is from 60:40 to 90:10. The mixture should contain 100 parts of polymer mixture and 150 parts of a high specific gravi-ty filler. It may optionally con-tain other ingredients, such as dibutyl phthalate as a plasticizer, and stearic acid. It is intended for use in vacuum-molded sheet or in injection molded form or sound-deadening purposes.

3.3 U.K. Patent Application 2,067,576A of C. Peoples et al, published 19~1 July 30, describes a composition which contains three essential ingredients - 10 to 25% of a thermoplastic resin component (such as ethylene/ethyl acrylate or ethylene/vinyl acetate copoly-mers), 4 to 15~ of an olefinic elastomer (such as ethylene/propylene rubber; ethylene/propylene/diene rubber, or polyisobutylene/isoprene copolymer), and from 60 to 85% of a filler component, such as barium sulfate or calcium carbonate. Optional additional ingredients include 0.25 to 200% of stearic acid and stearates which allegedly function as a processing aid; 2 to 10% of a parafinnic or napthenic hydrocarbon oil; tackifying resins;
titanates or polymeric ester surface-treating aids, etc.
Carpet constructions employing the above compositions are also disclosed. The compositions described in this appli-cation are alleged to offer unusually high flexibility as compared with blends known heretofore.
Summary of the Invention According to the present invention there is provided a composition comprising (a from 0 to about 50~ by weight of at least one copolymer of ethylene with at least one comonomer selected from the group consisting of vinyl esters of saturated carboxylic acids wherein the acid moiety has up to 4 carbon atoms, unsaturated mono- and dicarboxylic acids of 3 to 5 carbon atoms, salts of said unsaturated acids, and esters of said unsaturated acids wherein the alcohol moiety has 1 to g carbon atoms, the ethylene content of said copolymer being from about 40 to about 95% by weight, the comonomer content of said copolymer being from about 5 to about 60% by weight, and the melt index of said copolymer being from about 0.1 to about ~00, T~S
,7 3~33 provided that when sai.d copolymer of ethylene is an ethylene/vinyl ester or ethy].ene/unsaturated mono- or dicarboxylic acid ester copolymer said copolymer can contain up to about 15 percent by weight of carbon monoxide or sulfur dioxide; provided, that when the olefin polymer of paragraph (e) is absent, the amount of ethylene copolymer is at least about 5% by weight;
(b) from 0 to about 20 percent by weight ox at least one plasticizer selected from the group consisting of processing oils, epoxidized oils, polyesters, polyethers, and polyether esters;
(c) from about 40 to about 90% by weight of filler;
(d) from about 0.05 to about 5.0% by weight of it least one surface active agent selected from the group consisting of alkanol amides: betaine derivatives; block copolymers comprising a series of condensates of ethylene oxide with hydrophobic bases formed by condensing propylene oxide with propylene glycol; ethoxylated compounds comprising alcohols, alkyl phenols, amines and amides; sulfonated derivatives comprising alkyl sulfonates, aryl I: sulfonates, alkyl-aryl sulfonates, amine and amide sulonates, olefin sulfonates, sulfosuccinates, :~ sulfonated fatty acid esters, sulfonates of : 2S ethoxylated alkyl phenols and of oils and of fatty acids, naphtholene and alkyl naphtholene sulfonates condensed:naphtholene sulfonates, ~aphthalene and : alkyl naphthalene sulfonates and petroleum sulfonates, and dodecyl and tridecyl benzene sulfonates; dodecyl and tridecyl sulfonic acids;
sulfates of alcohols, of ethoxylated alcohols ox ethoxylated alkyl phenols, of oils, of fatty acids, : of fatty esters, alkaryl sulfates, and sodium, ammonium and amine salts thereof; phosphate 35 - derivatives comprising phosphate esters, phosphate alcohol ethoxylates, phosphate ether ethoxylates, phosphate alkyl acids and phosphate alkyl quaternaries; and quaternary surfactants;
(e) from 0 to about 55% by weight of olefin polymer selected from the group consisting of low density branched polyethylene, high density linear polyethylene, linear copolymers of ethylene and another olefin comonomer, polypropylene and copolymers o propylene and ethylene where the ethylene content is up to 20% by weight provided, that when the ethylene copolymer of paragraph (a) is absent the amount of olefin polymer is at least about 5~ by weight; and (f) from 0 Jo about 50~ by weight of elastomeric polymer; and (g) from 0 to about 30% by weight of tac~ifier.
Further provided according to the present invention are the above compositions in the form of a sound-deadening sheet.
Still further provided according to the I: present invention are carpets and especially automotive carpets and foam fabric or scrip having a backside coating consisting essentially of the above composition, : 25 etailed Description of the Inyention ....... .
: The inclusion of a processing oil in highly : loaded blends of ethylene-vinyl acetate (EVAj and filler has been described in USP 4,191,798. When the filler loading exceeded about 70%, the tensile elongation of the blend tended to drop sharply--to -I the undeslrably low range of 15-30~ It has been found that inclusion of very small amounts of a surface active agent (surfactant) of the proper type will produce a remarkably and unexpectedly large 3~3 s increase in the tensile elongation value of the individual blend.
The ethylene copolymers suitable for the composition of the present invention are copolymers ~~
with at least one comonomer selected from the group consisting of vinyl esters of saturated carboxylic acids wherein the acid moiety has up to 4 carbon atoms, unsaturated mono- or dicarboxylic acids of 3 to 5 carbon atoms, salts of said unsaturated acids and esters of said unsaturated mono- or dicarboxylic acids wherein the alcohol moiety has 1 to 8 carbon atoms Terpolymers of ethylene and the above comonomers are also suitable. In addition, terpolymers of ethylene/vinyl acetate/carbon monoxide or ethylene/vinyl acetate/sul~r dioxide containing up to about 15 percent by weight of carbon monoxide or sulfur dioxide can also be employed.
The ethylene content of the copolymer is from about 40 to about 95~ by weiyht, and the comonomer content is from about 5 to about 60% by weight. The preferred ethylene and comonomer level i5 from about 45 to about 91% and from about 9 to about 55% by weight, respectiYely. The most : preferred ethylene and comonomer content is from about 88 to about 72~ and from about 12 to about 28~, respectively. A mixture of two or more ethylene copolymers can be used in the lends of the present nvention in place of a single copolym~r as long as the average values for the comonomer content will be within the above indicated range.
: Employing a copolymer containing over 28 : nonethylen.ic comonomer such as vinyl acetate) results in blends that are less stiff and have lower tensile strength, while their elongat~cn is - 35 increased. The most preferred level is about 12 to ;33~3~
28 weight percent Below 12~ vinyl acetate, the blends become much stiffer, lose elongation, and oil compatability problems may arise. Even blends made with nonbleeding oils tend to become "oily" as -polyethylene homopolymer is approached.
Melt index of the copolymer can range from about 0.1 to about 400, preferably from about 0.1 to about 50O Physical properties, principally elongation, decline to lower levels when the ethylene copolymer melt index is above about 50. Lower melt index ranges, from about 1 to about 10, are most preferred to maintain strength.
Generally from about 5 to about S0~ by --weight of ethylene copolymer is employed in the composition of the present invention, preferably from about 8 to about 35% by weight, and most preferably from about 12 to about 25~ by weight.
Particularly useful properties can be obtained when two properly-selected ethylene copolymers are used in blends of the present invention. By combining at least two different properly selected EVA copolymer grades, copolymers PA) and (B), with filler, plasticizer, and an effective surfactant, unexpected and unusual mcdi~ication of the physical properties ox the filled compositiGn can be achieved as compared with compositions containing only a single EVA resin - ~~ grade. Mos significantly, by replacing a single EVA
grade in a filled blend with an equal amount of a 30 properly selected mixture of two EVA grades, where the`mixture has the same weight percent vinyl acetate content and melt index as the single EVA grade - replaced, the tensile elongation can be increased substantially.

1;2~3~33 The polar comonomer (such as vinyl acetate)content of the first copolymer, copolymer (A), is from about to about 3Q percent by weight. The polar comonomer content of the second copolymer, copolymer (B), is from about 28 to about 60 percent by weight, provided that the polar comonomer content of the second copolymer is at least 12 weight percent greater than the polar comonomer content of the first copolymer. The balance of copolymers (A) and (B) is made up by ethylene.
The polar comonomer content of the first copolymer is preferably from about 5 to about ~8 percent by weight, and the polar comonomer content of the second copolymer is preferably from about 30 to about 60 percent by weight, provided that the polar comonomer content of the second copolymer is at least 15 weight percent greater than the polar comonomer content of the first copolymer.
The most preferred polar comonomer content of the first copolymer is from about 10 to about 25 percent by weight, and the most preferred polar comonomer content of the second copolymer is from about 33 to about 60 percent by weight, provided that ~~:- the polar comonomer content of the second copolymer is at least 18 percent greater than the polar comonomer content of the first copolymer.
The weight ratio of the first copolymer to -the second copolymer in the compositions of the - -present invention can range from about 99/1 to about 55/45, preferably from about 97/3 to about 60/40, and most preferably from about 95/5 to about h5/35~
` -The melt index of the irst copolymer can range from about 0.1 to about 20, preferably from : - :about 0.3 to about 10, and most preferably from about ~3S - 0.5 to about 2. The melt index of the second 3~

copolymer can range from about 5 to about 1000, preferably from about 10 to about 200, and most preerably frorn about 15 to about 100.
Generally, prom about 5 to about 50 percent by weight of the mixture of the first copolymer and the second copolymer is employed in the composition of the present invention. Preferably from about 8 to about 35 percent by weight, and most preferably Erom about 12 to about 25 percent by weight is employed.
In accordance with the above, suitable ethylene copolymers are such as ethylene/vinyl acetate, ethylene/acrylic acid and its ionomers, ethylene/methacrylic acid and its ionomers, ethylene/methyl acrylate, ethylene/ethyl acrylate, ethylene/isobutyl acrylate, ethylene~normal butyl acrylate, ethylene/isobutyl acrylate/methacrylic acid and its ionomers, ethylene/normal butyl acrylatetmethacrylic acid and its ionomers, ethylene/isobutyl acrylate/acrylic acid and its ionomers, ethylene/normal butyl acrylate/acrylic acid : : and its ionomers, ethylene/methyl methacrylate, : ethylene/vinyl acetate/methacrylic acid and its ionomers, ethylene/vinyl acetate/acrylic acid and its ionomer~, ethylene/vinyl acetate/carbon monoxide, ethylene~methyl acrylate/carbon monoxide,.
ethylene/normal butyl acrylate~carbon monoxide, ethylene/isobutyl acrylate/carbon monoxide, ethylene/vinyl acetate/monoethyl maleate and ethylene/methy} acrylate/monoethyl maleate.
Particularly suitable copolymers are ethylene/vinyl acetate, ethylene/ethyl acrylate, ethylene/methyl acrylate, ethylenefisobutyl acrylate, ethylene/methyl methacrylate, and ethylene/vinyl acetate/methacrylic acid.

~3~33 The first group of plasticizer ingredient of the composit;on of the present invention is known as process or processing oil. Three types of processing oils are known--paraffinic, aromatic and naphthenic.
None of these are pure; the grades identify the major oil type present.
Paraffinic oils tend to "bleed" from blends. Bleeding is normally not desirable, but could be useful in specialty applications for example, in concrete forms where mold release characteristics are value.
On the other hand, naphthenic and aromatic oils are nonbleeding when used in proper ratios and are thus preferable for uses such as automotive carpet backsize.
Processing oils are also subdivided by viscosity range "Thin" oils can be as low as 100-500 SUS (Saybolt Universal Seconds) at 100F
(38C). "Heavy" oils can be as high as 6000 SUS at 100F t38C). Processing oils, especially naphthenic and aromatic oils with viscosity of prom about 100 to 6000 SUS at 100F (38C) are preferred.
The amount of plasticizer, such as the process oil, present in the composition of the - 25 present invention is from 0 to about ~0% by weight, preferably from about 2 to about 15% by weight. Most preferably when using a filler of medium density, such as calcium carbonate the amount of processing -oil i5 from about 4 to about 10~ by weight, and when using a filler of higher density such as barium sulfate, the amount of processing oil is from about 3 to about 10% by weight In many cases, addition of processing oil in an amount of less than about 2% will not haze a 35 - significant effect. Processing oil in excess of ~2~13~3 about 10% will cause the melt index to rise rapidly and the blend to become much softer. At extremes, for example, at 70% filler, over 15% oil and less than 15% EVA, the oil content overwhelms the blend as the amount of EVA present is not adequate to provide adequate strength for the blend.
In the selection of a process oil, other factors such as the type of oil selected and its viscosity must be considered. These are discussed in detail in USP 4,191,798.
The second group of plasticizers that are effective in the practice of the present invention is the group comprising epoxidized oils such as epoxidiæed soybean oil and epoxidized linseed oil.
The third group of plasticizers that are effective are the polyesters, which, in general, are liquid condensation products of a polybasic acid and a polyol. The term "liquid" in the context of the present invention is used to mean pourable at room temperature. The acid component is most often a saturated aliphatic dibasic acid or an aromatic dibasic acid; adipic acid, azelaic acid, phthalic acid, sebacic acid, and glutaric acid, or mixtures thereof. The polyol can be an aliphatic polyol or a polyoxyalkylene polyol, such as ethylene glycol, propylene glycol, 1,4- and 1,3-butane glycol, diethylene glycol, and polyethylene glycolO
Preferred polyester compositions would consist of an acid component of which greater than 50% by weight are aliphatic dibasic acids, and a polyol component of aliphatic polyol or even more preferably aliphatic glycol. Most preferred compositions are based on adipic or azelaic acid/ and propylene glycol or 1,3-or 1,4-butane glycol. The molecular weight of these .~

3~333 plasticizers can vary from a low of a few hundred up to a high of about 10,000. The molecular weight of commercial products is seldom specified. Typically in the trade the molecular weight range of the product is classified as low, medium, or high. The preferred range for purposes of this invention is that classif ied as medium.
Mixtures of polyesters with hydrocarbon oils are also effective plasticizers in the present invention. One objective of using such a mixture is to couple the high efficiency of the relatively high cost polyester with the low cost of the hydrocarbon oil. The cost/performance of a compound plasticized with such a mixture can be improved significantly for a given application because properties can ye tailored more precisely, or filler levels can be increased. Actually certain advantages in the performance of the blends of the present invention are obtained as will be discussed below, when such a mixture is used 2S the plasticizer.
When used alone, the amount of polyester plasticizer in the composition of the present invention is from about 1 to about 15% by weight, : preferably from about 2 to about 12~ by weight.
I: 25 Where a mixture of the polyester plasticizer and a hydrocarbon Gil is employed, the relative proportions of the two component can be varied over a wide range depending upon performance objectives.
Mixtures containing 50% or less of the polyester are preferred for economic reasons, and most preferred are those containing 20% or less of~the polyester.
A separate class of plasticizers, polyethers :~ and polyether estersi are also effective plasticizers : in blends of the ethylene copolymers and fillers 35 - described above. In general, polyethers are , . . .
:

~Z~3s333 oligomers or polymers of alkylene oxides; polymers of ethylene or propylene oxide are the most common types available commercially. Polyethers can be prepared by polymerization of aldehydes using various types of catalysts, or by acid or base catalyzed polymerization of an alkylene oxide, for example.
Polyethers can be terminated by hydroxyl groups to form the diol (glycol) or, in the case of adducts of alkylene oxides with glycerol, for example, the triol, and so forth. The hydroxyl terminated polyether can also be reacted with an acid to form the ester. Fatty acids such as lauric and stearic acids are commonly used; the most common examples of these compounds are the mono- and diesters of polyethylene or polypropylene glycol. The molecular weight of polyethers may range up to those typical of high polymers.
Preferred polyether compositions in the practice of this invention are those consisting of the polyols based on random and/or block copolymers of ethylene oxides and propylene oxides. The copolymer poIyols provide better performanc~-in-terms of efficiency in compounds of the present invention containing very high levels of filler.
When used alone the amount of polyether plasticizer in the composition of the present invention is from about l to about 15~ by weight, preferably from about 2 to about 12% by weight.
Mixtures of the polyether or the polyether 30 ester plasticizers with either a polyester plasticizer or a hydrocarbon processing oil can also be used in the practice of this invention The advantage of polyether/polyester combination-is the lower cost since the polyethers are cheaper than the - polyesters. Combinations of polyether and processing oil are also cheaper because of the lower C05t of the oil.
The relative proportions of the two components in a polyether/polyester combination will --be adjusted according to the eficiency of the system based on property requirements and cost. Those based primarily on polyester will not be as stiff and will be more expensive, for example, than those based primarily on a polyether or polyether ester.
lOWhere a mixture of the polyether or polyether ester and a hydrocarbon oil is employed, the relative proportions used will again depend upon cost and property requirements. Since the polyethers are more expensive than the processing oils, mixtures containing 50~ or less of the polyethers are preferred.
As referred to above a mixture of processing oil, on the one hand, and epoxidized oil, polyester or polyether or polyether ester, or any combination thereof, on the other hand, can also be used very effectively as the plasticizer for the compositions of the present invention. In tact, such a two or more component plasticizer system, comprising from about 50 to about 95 percent by weight of processing oil, gives higher tensile elongation than can be obtained using either plasticizer alone at the same level. Maximum elongation is achieved using a mixture of processing oil and polyester or polyether or polyether ester or any combination thereof comprising from about 50 to about 80 percent by weight of processing oil.
Where a mixture of plasticizers is used, the amount of plasticizer may range from about 2 to about 15% by weight, preferably from about 4 to about 12%
35 - by weight . Most preferably when usins a filler of 3,~
medium density, such as calcium carbonate, the amount of plasticiæer is from about 5 to about 10% by weight, and when using a filler of higher density, such as barium sulfate, the amount o plasticizer is S from about 4 to about 8~ by weight.
The third essential ingredient of the composition of the present invention is he filler.
The percentage of filler that can be included in the composition of the present invention on a weight basis is primarily a function of the density of the filler. Particle size and shape of the filler also will have an effect on properties of blends Fine particle size fillers generally have a tendency to result in higher blend viscosities and they are also more expensive. No. 9 Whiting which has been used extensively in the present compositions tabout 9 through 325 mesh) represents a viable midpoint in coarsenesst availability, and cost. Most preferred fillers are calcium carbonate and barium sulfate The amount of filler present in the composition of the present invention is from about 40 to about ~0%
by weight, preferably from about 55 to about 90~ by weight. Most preerably, when using a filler of medium densityt such as calcium carbonate, the amount of filler is from about 65 to about 85~ by weight, and when using a filler of higher density, such as barium sulfate, the amount of filler is from about 70 to about 90~ by weight.
When the ethylene interpolymer employed in the composition of the present invention is an ethylene/vinyl ester copolymer, such as e~hylene/vinyl acetate, and when the filler employed - in combination therewith is clay, such as SUP~E~
Clay, it is necessary to add oil to the blend in order to passivate the clay Proper sequencing of *denotes trade mark ~3~333 the addition of the ingredients is necessary to attain success in the mixing operationO Sequence A, below, during intensive mixing will be successful:
while Sequence B may fail, if the EVA/clay mixture is --heated before the clay is passivated, because of the decomposition of the EVA copolymer caused by the clay. Decomposition is accompanied by liberation of anhydrous acetic acid and discoloration of the blend.
Sequence A: "Xn - Clay - MY" OIL - Mix - EVA - Mix.
Sequence B: K - Clay - EVA - Mix - Oil - "Y" - Mix.
In the above illustration, "XN end "Y' may be either nothing or other fillers, diluents or resins that do not influence the otherwise probable adverse reaction of the EVA with untreated clay. The above passivation of clay, in order to enable use of substantial amounts of clay in ethylene/vinyl ester blends, is the subject matter of USP 47222,924~
Further details on the effect of particle size of the filler on blend properties is given in U5P 4,263,196.
In addition to the fillers mentioned above, incorporation of many other types is, of course, possible without altering the fundamentals taught in this patent. For example, inclusion of alumina trihydrate (hydrated alumina - Al~O3 3H2O) is highly desirable when flame-retardant or low-smoke-tendency blends are desired. Heavy fillers, such as powdered iron or lead, or oxides of - -- them, can be employed when ultra~deQse blends are - desired. Similarly, minerals having low density, such as magnesium carbonate, calcium sulfate, silica, flyasht and cement dust, or organic fillers such as - yarns, wood flourl nut shells, rice hulls etc., can be employed when light-density blends are preferable. Finally, fillers with varied a5pec 35 - ratios, such as talc, mica, from highly acicular 3~33 ~wollastonite, etc.) to round (ylass beadst etc.) can also be employed to alter tensile strength/elongation relati.onshipsO
The final essential ingredient for the --subject blend is a surface active agent of the proper type. For purposes of this invention, a surfactant it defined as "any compound which reduces the interfacial tension between a liquid and a solid."
(Condensed Chemical Dictionary, Tenth Edition, Van Nostrand Reinhold Company, page 9861. Further, the key characteristic property for liquids is surface tension, and that of a solid surface is adsorption.
Both have the same cause, namely, the inward cohesive --forces acting on the molecules at the surface"
(ibid., p. 5~4, ~interfacen). In the descriptions which follow, the terms "surfactant" and "surface active agent" will be used interchangeably.
Literally thousands of surfactants exist.
To classify and to distinguish by category those : 2~ surface active agents which are suitable for the : purposes of this invention, the system utilized in a standard reference source - McCutcheon's "Emulsifiers and Detergents" - nNorth American Edition - 1981" has b en selected.
Surfactants which are effective in attaining : the purposes o this invention are those which are selected from the group consisting of alkanol amides;
~~ betaine derivatives; block copolymers comprising a series of condensates of ethylene oxide with : 30 hydrophobic bates formed by condensing propyIene : oxide with propylene glycol; ethoxylated compounds comprising alcohols, alkyl phenols, amines and - amides; sulfonated derivatives comprising alkyl : sulfonates, aryl sulfonates, alkyl-aryl sulfonates amine and amide sulfonates, olefin sulfonates, 3~3;~

sulfosuccinates, sulfonated fatty acid esters, sulfonates of ethoxylated alkyl phenols and of oils and of fatty acids naphtholene and alkyl naphtholene sulfonates, condensed naphtholene sulfonates, naphthalene and alkyl naphthalene sulfonates and petroleum sulfonates, and dodecyl and tridecyl benzene sulfonates; dodecyl and tridecyl sùlfonic acids; ~u'lfates ox alcohols, of ethoxylated alcohols, of ethoxylated alkyl phenols, of oils, o f f atty acids, of fatty esters, alkaryl sulfates, and sodium, ammonium and amine salts thereof: phosphate derivatives comprising phosphate esters, phosphate alcohol ethoxylates, phosphate ether ethoxylates, phosphate alkyl acids and phosphate alkyl qua~ernaries; and quaternary surfactants.
The number of surfactants in existence is enormous; the examples named above can be replaced by other close analogs with good results and without departing from the spirit of this inventionO
The preferred surface active agents are selected from the group consisting of alkanol amides;
betaine derivatives; block copolymers consisting essentially of a series of condensates of ethylene oxide with hydrophobic bases formed by condensing propylene oxide with propylene glycol: ethoxylated-compounds consisting essentially of ethoxylated alcohols, alkyl phenols, amin~s and amides;
sulfonated derivatives consisting essentially of alkyl sulfonates, alkyl-aryl sulfona~es, amine and amide sulfonates, sulfonated fatty acid esters, - sulfonates of ethoxylated alkyl phenols and of oils and of fatty acids, naphtholene and alkyl naphtholene sulfonates, and condensed naphtholene ~ulfonates and dodecyl and tridecyl benzene sulfonates; sulfates of alcohols, of ethoxylated alcohols, of fatty acids, alkaryl sulfates, and sodium, ammonium and amine salts thereof; phosphate derivatives consisting essentially of phosphate esters, phosphate alcohol ethoxylates, phosphate ether ethoxylates, phosphate alkyl acids and phosphate alkyl quaternaries; and quaternary surfactants.
The most preferred surfactants are selected from the group consisting of sul~onated derivatives consisting essentially of alkyl sulfonates, alkyl-aryl sulfonates9 amine and amide sulfonates, sulfonated fatty acid esters, sulfonates of ethoxylated alkyl phenyls and of oils and of fatty acids, naphtholene and alkyl naphtholene sulfonates, and condensed naphtholene sulfonates; sulfates of alcohols, of ethoxylated alcohols, of fatty acids, alkaryl sulfates, and sodium, ammonium and amine salts thereof; and phosphate esters.
In using surface active agents of the types described in the compositions of this invention the amount is from about 0.05% to about 5~ by weight, and preferably from about 0.1~ to about 2.5%. Most preferably, when using a surfactant which is--particularly effective, the amount is from about 0.12% to about 0.75%.
- 2S In many cases, for the userls convenience, - the surfactant may be offered as a solution or dispersion in water or in an organic solvent. In -I such cases the percentages in the preceding- -- ` paragraph refer to the amount of active ingredient present - and not to the product as supplied.
Polymers, both homo- and copolymers, other - than the ones referred to above, can also be used to - some extent in combination with the above speciied polymers without significantly interfering with the 35 - advantages obtained by the present invention. These include, but without limitation, polymers such as ethylene/carbon monoxide and ethylene/sulfur dioxide. Similarly, other ingredients can also be added to the compositions of the present invention by a compounder in order to obtain some desired effect such as reduction of cost, or enhancement of a physical property. Accordingly, extender resins, waxes, foaming agents, crosslinking agents, antioxidants, etc. that are widely used, particularly 10 in hot melts, can be included in the compositions of the present invention. Illustrative examples of several special additives and of potentially desirable resin ingredients are siven below.
Elas~omeric polymers are of interest as 15 modifying resins for the blends ox the present invention. They exhibit good compatibility in the blends and can be useful for modifying flexibility or other physical properties. The blends of the present invention can contain from O to about 50% by weight of an elastomer or a mixture of elastomers, preferably from 0 to about 25~ by weight, and most preferably from 0 to about 12% by weight. Mooney viscosity of the elastomers is preferably in the range of from 20 to 90. Thermoplastic elastomers ~5 (e.g., ethylene-propylene rubber, styrene-butadiene-styrene, polyurethane, eta or vulcaniæable elastomers (e.g., styrene-butadiene - - rubber, ethylene/propylene/diene terpolymer ~EPDM), chlorosulfonated polyethylene, etc.) can be used.
Preferred elastomers are ethylene-propylene rubber and EPDM rubber In which the ethylene content should range from above 20 percent by weight to about 80 - percent by weight. The diene comonomer (in EPDM) is - usually methylene norbornene, ethylidene norbornene,-35 -dicyclopentadiene or 1,4-hexadiene, although other 3~33 dienes may be used, and the concentration of the diene is usually less than about 5 percent by weight. When vulcanizable elastomers are used, they are added in the nonvulcaniæed state; if desired, the resulting compound can be cured in a subsequent operation to produce a product with increased tensile strength and improved high temperature performance.
The basic blends described above are essentially free of surface tack at ambient temperature. Even if made with a "bleeding" type of paraffinic oil, the final sheet, at ambient temperature, may be slippery to the touch but will not be tacky. (Of course, as temperatures are increased to the 200F 250F level, the blends will be progressively softened and will adhere well to many substrates.) From time to time, compounders provably will want to produce sheeting with enhanced surface tack or adhesiveness. This can be done in the blends described in the present invention by incorporating a ~ackifier resin in the formulation.
The tackifier may be any suitable tackifier known generally in the art such as those listed in-U.S.
- PatO 3,4a4,405. Such tackifiers include a variety of natural and synthetic resins and rosin materials.
- 25 The resins which can be empIoyed are liquid, - semi-solid to solid, complex amorphous materials generally in the form of mixtures of organic -- compounds having no definite melting point and no tendency to crystallize. Such resins are insoluble in water and can be of vegetable or animal origin, or can be synthetic resins. The resins employed function to provide substantial and improved - tackiness of the composition. Suitable tackifiers include, but are not necessarily limited to the 35 -resins discussed below.

21 ~3S~3~3 A class of resîn components which can be employed as the tackifier composition hereof, are the coumarone-indene resins, such as the para coumarone-indene resins. Generally the coumarone-indene resins which can be employed have molecular weight which ranges from about 500 to about ~,000. Examples of resins of this type which are available commercially include those materials marketed as Picco*-25 and ~Piccon-100.
Another class of resins which can be employed as the tackifier hereof are the terpene resins, including also styrenated terpenes. These terpene resins can have a molecular weight range from about 600 to 6,000. Typical commercially available resins of this type are marketed as Piccolyte* S-100, as Staybelite Ester* ~10, which is a glycerol ester of hydrogenated rosin, end as Wingtack* 95 which is a polyterpene resin.
A third class of resins which can be employed as the tackifier are the butadiene-styrene resins having a molecular weight ranging from about 500 to about 5,000. A typical commercial product of this type is marketed as Buton* 100, a liquid butadiene-styrene copolymer resin having a molecular weight of about 2,500. A fourth class of resins - - which can be employed as the tackifier hereof are the polybutadiene resins having a molecular weight ranging from about 500 to about 5,0U0~ A
commercially available product of this type is that marketed as "Buton~ 150, a liquid polybutadiene resin having a molecular weiyht of about 2,000 to about

2,500.
- A fifth class of resins which can be employed as the tackifier are the so-called 35 -hydrocarbon resins produced by catalytic *denotes trade mark 22 3~33 polymerization of selected fractions obtained in the refining of petroleum, and having a molecular weigh'c range of about 500 to about S,ûOO. Examples of such resin are those marketed as Piccopale*-100, and as Amoco* and Velsicol* resinsD Similarly polybutenes obtained from the polymerization of isobutylene may be included as a tackifier.
The tackifier may also include rosin matexials, low molecular weight styrene hard resins such as the material marketed as Piccolastic* A-75, - disproportionated pentaerythritol esters, and copolymers of aromatic and aliphatic monomer systems of the type marketed as "Velsicol" WX 1232. The rosin which may be employed in the present invention may be gum, wood or tall oil rosin but preferably is tall oil rosin. Also the rosin material may be a modified rosin such as dimerized rosin, hydrogenated rosin, disproportionated rosin, or esters o rosin.
Esters can be prepared by esterifying the rosin with polyhydriG alcohols containins 2-6 alcohol groups A number of examples of suitable tackifiers - is given in Table 9, below. These must be regarded only as typical examples, as literally hundreds of logical candidates exist. A more comprehensive I; - 25 listing of tackifiers which can be employed is provided in the TAPPI CA Report #55, February 1975g pages 13-20, inclusive, a publication of the - I- Technical Association of the Pulp and Paper Industry, Atlanta, Georgia, which lists well over 200 commercially available tackifie~ resins.
In use, the compounder generally will want to select an ethylene-based copolymer and a tackifier - resin which will be mutually compatible; chemical similarities which will indicate compatibility can be 35 . used for guidance. For a few highly specialized *denotes trade mark

3 3~
uses, such as super-hot~tack, quick-stick blends, the compounder may well elect to use incompa'cible sys'cems. Finally, the reverse effect may be sought--in such instances, where an unusually slippery surface is desired, incorporation of small amounts of a slip aid such as Armid*O may prove benef icial.
In using tackifier resins, the amount used in compositions of this invention is from 0 to about 30% by weight of the blend; preferably from 0 to about 20% by weight: and, most preferably, from 0 to about 15~ by weight.
The surface active additives described in .
- this specification are particularly helpful when one of the many commercially available polyethylenes is employed as a substitute for part or all of the ethylene copolymer of the blend. As polyethylenes (whether LDPE, LLDPE, or HDPE) do not wet filler effectively, it is not practical to incorporate more than perhaps 10 to 20% filler into binary blends of - PE and filler. However, as shown in Table 5, useful - blends in which the polyethylene is the only resinous ingredient can be prepared by employing both a.
: process oil and a surfactant additive. Thus, the substitution of homopolymer for copolymer can cover the entire range from 0 to 100%. In practice,.
: intermediate PE levels would be used in most . -- commercial blends to attain a desired stiffness -level concomitant with other needed propertiesO The I'ideal~ level will, of necessity, vary according to the physical property desired.
The teachings above have dealt with several different potential polymeric ingredients on an ~individual-ingredient" basis to outline 35 .contributions possible from widely varying resin or *denotes trade mark.

P3~3~
polymer types. It mu,st be stressed that polymer ingredients of the above types can, of course, be mixed so that, for example, the compounder may elect to modify a simple four-component EVA/oil/filler/surfactant composition by replacing part of the EVA with a small amount of rubber as a polymeric softener, or of tackifier for adhesivity.
In addition part of the oil can be replaced with a polyester or polyether-type additive to attain highly effective plasticization with a lower total amount of plasticizer. Thus, the possible combinations and permutations available to a skilled compounder will be infinite; yet remain within the spirit and intent of this invention.
The blends of the present invention are thermoplastic in nature and therefore can be recycled after processing. The recycled material may also contain textile fihers, jute, etc. present in the trim obtained during production of the finished product (e.g., back-coated automotive carpet). .
A commercially sized batch-type Banbury or equivalent intensive mixer is entirely suitable for preparing the compositions of the presen invention A Farrel*continuous mixer ~"FCM") is also an -- 25 excellen mixing device. In either instance, dry ingredients are charged in routine ashion. It is convenient in most cases to inject the plasticizer component directly into the mixing chamber of either unit as per widely used practice with this type of equipment. When more than one plasticizer is used, and where any one of the plas~iciæers is present in a small amount (less than about }0 weight percent of the total plasticizer mixture), the plasticizers should be preblended before addition to the other 35 . ingredients of the present invention. This will *denotes trade mark : 24 , I, acilitate uniorm distribution of each plasticizer component in the final composition and thus ensure that optimum properties are obtained. Similarly, since the amounts of surfactant employed generally is so small less than 1% for many cases, it is important to be certain that the surfactant is thoroughly mixed into the final blend. If this is not done, highly erratic values for physical properties may result. Thus, it may often prove helpful to premix the surfactant into a portion of one of the other ingredients, e.gO, a liquid surfactant may be premixed with the process oil or a solid surfactant may be premixed with an aliquot of the filler If desired, the copolymer and the plas~icizer~s) can be precompounded as a ~Masterbatch" in a suitable intensive mixing device ~e.g., Banbur~ mixer or screw extruder). This ~Masterbatch" can then be compounded with the filler and the-other remaining ingredients to produce the final composition. A mix cycle of about 3 minutes i5 generally adequate for the 8anbury mixer at an - operating temperature usually between 3~5 and 375F~
The operating rate for the FCM unit generally will - fall within ranges predicted by literature prepared by the Farrel Company, Ansonia, Connecticut Here, - temperatures between 325 and 425F are effective. In both cases, a very low plasticizer lever, say about 2~3~, may require hiyher temperatures, while plasticizer levels above about 7% may mix we}l:at lower mixer temperatures. While not evaluated, it is expected that other devices or handling viscous mixes (MI of 0.1 to 20) should be entirely -- satisfactory - but in any case, prototype trials in advance are desirable.
*denotes trade mark 3S~33 2~
Generally, chalnges in the sequence of additiGn of ingredients has not been found to be significant, provided that the final mixture is thoroughly fluxed to attain homogeneity. --Once blends are mixed, routine commercial practices may be used, such as underwater melt cutting plus drying or use of sheeting plus chopping methods, to produce a final pelletized product.
Alternately, the hot mixture also may be immediately fabricated into a final form, e.g~ sheeting, molding, etc.
Primary use for the compositions of the present invention will probably be in the sheeting field, particularly for low cost, dense, sound deadening structures. Outstanding characteristics such as improved hand" 9 "drape", reduced stiffness, higher elonyation and reduced thickness of the extruded sheeting result from the compositions of the present inventionO
Other uses are possible. The principal advantage of the blends of this invention i5 that - . certain physical properties, such as flexibility and - toughness, which are typically reduced when fillers are added to polymers, can be maintained within I- ~5 useful limits over a broad range of iller concentrations. Thus, blends of this invention could be used in the manufacture of wire and cable - -I compounds, of various molded parts, of sealants and caulks, or in other uses where flex bility and toughness are desired, coupled with the economies normally achieved by the incorporation of low cost tillers.
: the blends of the present invention can readily be extruded onto a substrate, such as an automotive carpet, a form, a fabric or a scrim 27 ~Z~3S~33 material, or can be extruded or calendered as unsupported film or sheet. Depending upon the equipment used, and the compounding techniques employed, it is possible to extrude a wide range of film thickness, from below 20 mils to above 190 mils. This then provides industry with an opportunity to vary the amount of sound deadening to be attained by varying film thic~ness~ density of blends, ratio of filler load to binder, and similar techniques well known in the art.
The sound deadening sheet produced may be used in various ways:
When applied to automotive carpet blends -described are an effective and economic means o - 15 deaden sound, while also simultaneously serving as a moldable support for the carpet.
When used in sheet form, especially when coated onto a fabric, the blends can be installed in other areas of an automobile, truck, bus, etc., such as side panels, door panels, roofing areas, dash insulta~ors, etc.
In sheet form, blends may be used as drapes or hanging to shield or to surround a noisy piece of factory equipment such as a loom, a forging press, US etc.
: . In laminated sheet form, blends, faced with another material, might be used to achieve both a . . decorative and a functional use--such as dividing panels in an open-format office.
The application of the compositions of the . . present invention in carpets, and particularly in : automotive carpets, is essentially identical to the methods as alxeady described in U.S. Patent -

4,191,798 O 3~3i33 The highly-filled compositins described herein may be processed industrial].y into final sheet or three-dimensional solid form by using standard fabricating methods well known to those skilled in the art. Thus, fabricating methods such as extrusion, calendering, injection or rotomolding, extrusion coating, sheet laminating, sheet thermoforming, etc. are all practical means for forming the compositions of this invention.
The examples which follow are given for the purpose of illustrating the present invention. All parts and percentages are by weight unless otherwise specified. In all examples, the ingredients were premixed in a one-galIon (about 3.8 1) can by shaking the contents manually for about 0.5 minutes. (Where liquid surface active agents are employed, it is often preferable to premix the very small mount of agent into the much larger volume ox liquid plasticizer, separately, before adding the liquid to the one-gallon can, to ensure reaching homogeneity rapidly). The ingredients were then added to a Banbury-type laboratory-sized intensive high-shear mixer. Mix condition used were fluxing for-3 minutes, at a temperature of about 3~5 to 375F
(about 160 to 190C).
Examples 1 to 23 and Comparative_Example 1 The composition and physical properties of - these blends are summarIzed in Table 1.
- Comparative Example 1 shows key properties 30 for a typical highly filled thermoplastic composition ; ` based on ethylene/vinyl acetate (EVA) copolymer resins, a process oil, and calcium carbonate resin, -I - as taught in U.S.P. 4,1~1,798. The stiffness value is about 75 grams; the Melt Index (MI) is a40ut 2.2s 35 - and the elongatlon is about 25%. The tensile /3~333 strength is about 650 psi. The indicated MI and stiffness levels are well within practical useful ranges The tensile strength is jar higher than i5 needed for most industrial uses. However, the elongation is close to the minimum level wh.ich is acceptable for commercial sheeting. A lesser value, e.g. less than about 10% elongation, means the sheet will probably tear on handling, unless costly special care is used Thus, the average user would clearly prefer to sacrifice some degree of tensile strength in order to attain substantially better elongation and tear resi tance.
It was found that the addition of a very small amount of selected surfactants produced an astoundingly large change in physical properties for the basic composition In Examples 1, 3, 8, 9~ 10, and 18, only 0.25% of one of the surface active agents tested proved highly effective in enhancing the relatively low elongation value already seen for Comparative Example 1. In all of these instances, the increase in elongation was nearly twenty-fold or higher - far higher than might have been predicted.
Ten additional su~factants, at the 0025% leveI, showed smaller but significant improvements in - :
elongation. For additives 2, 4, 6, 7, 13, 14~ lS, 16, 21, and 22, the final elongation values measured from 32~ to 52% - equivalent to a 33 to 100~ increase in elongation when compared to the 25% level noted :
for C-l. The balance of the additives tried, at 0.25% addition level, showed smaller or no enhancement in elongation. In several instances, e.g. additives 5, 11, 12, 17, and 20, the lack of effectiveness may ref}ect the low percentage of -active ingredient which the additive containsO
: 35 -3~33~

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# # l I) v Jo V .C pi ~3 CO En ~:~ o :~ s 3~ 3~33 Footnote for Table 1 (1) EVA l = Elvax* 360 resin, E. I. du Pony de Nemours and Company, Inc. 25% VAc; 75~ E;
M.I. ~Ø

5 (~) EVA ~2 = "Elvax" 3120 resin, E. I. du Pont de Nemours and Company, Inc., 7.5 VAc; 92.~%
E; M.I. 1.2.
(3) RCircosol~ 4240 - A naphthenic process oil, ex Sun Oil Company, ASTM type 103; ~525 SUS
at 100F; approximate composition is CA -21%; CN = 39%; Cp = 40%.
(4) Duponol* G - Anionic, alcohol sulfate, amine salt of saturated long chain alcohol.
(5) "Duponol" EP - Anionic, alcohol sulfate, diethanolamine lauryl sulfate, technical.
[35% active ingredient content (A,I.C.)].
t6) ~Duponol~ ME - Anionic, alcohol sulfate, sodium salt of lauryl alcohol.
(7) "Duponol" SP - Anionic, alcohol sulfAte, sodium salt. (35% A~IoC~)~
8j "Duponol~ WAQE - Anionic, alcohol sulfate, sodium salt, with extremely low sulfated alcohol content. (30% A.I.C.) ~9) Zelec* TY - Anionic antistatic agent. (50%
A.I.C.) - ~10) "Zelec" UN - Anionic antistatic agent -unneutralized fatty alcohol phosphate.
(11) "Zelec" NX - Anionic antistatic agent -fatty alcohol phosphate.
(12) ~Zelec" NE - Anionic antistatic agent -fatty alcohol phosphate composition (13) Zonyl* A - Nonionic, surface active agent, modified alkyl polyethylene ~lycol type.
(14) ~Zonyl" FSP Anionic fluorosurfactant. (35 A.I.C.) 4 *denotes trade;mark .i ~15) No 9 whiting - Commercial ground limestvne, CaCO3, ex Georgia Marble Company. Medium .
ground, approximately 20 micron average.
~16) ~Zonyl" FSN - Nonionic fluorosurfactant.
(50~ A.I.C.) (17) Merpol* DA - Nonionic liquid surfactant.
Dyeing aid for synthetic fibers and wool. A
nitrogen-containing ethylene oxide condensate. (60% A~IoC~)~
(18) ~Merpol" 5H Nonionic alcohol/ethylene oxide adduct. Detergent and wetting aid for textile and paper uses. (50% A~IoC~ ) (19) ~Merpol~ SE - Nonionic alcohol/ethylene oxide adduct. Low foaming type, for textile and paper uses.
(20) Product BCO * - Amphoteric surfactant; a C-alkyl betaine. (25~ A.I.C.), a product of E. I. du Pont de Nemours and Company.
(21) Al~anol~ ND - Anionic; a dyeing assistant -sodium alkyl diaryl sulfonate. (45% A,I.C.3 . (22) NAlkanol" XC - Anionic; surface tension reducer; sodium alkyl naphthalene sulfonate. --(23) "Alkanol" S Anionic;
dispersing/solubili~ing agent:
- 25 tetrahydronaphthalene sodium sulfonate~
(~4) "Alkanol" DOA - Polymeric dispersant for nonaqueous systems. (50~ A.I.C.) - -- (25) Avitex* LCP - Cationic; quaternary ammonium salt. (50~ A.I~C.) 30 (26) Petrowet* - Anionic; saturated hydrocarbon sodium sulfonate; wetting and penetrating agent. ~25% A.I.C.) ~27) Avitone* A - Anioni~i coating lubricant and plasticizer to prevent paper from sticking to dryers; textile softener. (75% A.I.C.) *denotes trade mark ~2~)3~3t33 (28) ASTM D1238, Procedure A, Condition E; units are dg~min~
(29) Referred to water.
(30) Tensile strength and elongation measurements S made on Instron* Tester using ASTM Method D1708 at crosshead speed of 2 in. (5.1 cm)/min. Samples are 0.876 in. (2.23 am x 0.187 inO (0.47 cm) in size, at strip thickness shown in table.
10 (31) Stiffness of strip measured by placing a 1 in7 X 6 in. (2.54 cm x 15.2 cm) strip on a platform scale, and measuring the force required to make the ends of the test strip meet, at room temperature. - -Note: "Alkanol"
~Avi~ex" All are products af ' nAvitonen E. I. du Pont de Nemours and "Duponol" Company and are registered Merpol trademarks. Where an active ~Petrowet~ ingredient content is not 20"Zelec~ indicated, the product as ~onyl" supplied contains 95% or more - of the active ingredient *denotes trade mark ::

35 .

~2~3~33 ., , ~112~35~33 For the mo5t effective additives, numbers 1, 3, 8, I, 10 and 18, the small amount of additive employed showed several totally unexpected benefits:
The elongation for the blends, versus that o Comparative Example 1, is enhanced by factor of from 18 to 22-~far beyond any predictable benefit.
The stiffness of the strip was reduced by about 1/3, in most instances.
The melt index of the blend nearly doubled or most blends.
- The tensile strength was reduced by about 50~--but still, at the 350 psi level, was - clearly high enough to perform well in most end uses.
The "toughness" of the blend--defined as the product of the tensile strength in psi and I- the elongation in percent- has risen : sharply. The "toughness" for Comparative Example 1 is about 650 x 25%, or slightly : over 16,000. By contrast, the "toughness"
range for the six most effective additives was from 128,000 to 220,000, with an average : toughness value of 173,000. : This tenf;old - 25 enhancemen is totally unpredictable prom any information known to us ;
The reduction ln both stiffness and melt ; index values is~also of considerable;signi~icance~ .- . -: : As will be shown later, these shifts open the way to -adding increased amounts of fillers, while - : maintaining acceptable levels fo:r both~elongation and ; "toughness" of the blend ExamFles 24 to~36 .. .
In view of the large differences in effectiveness noted in Table I, a serles of further :

: ; :

. ,~

~3~33 exploratory tests was initiated. The goals were two-fold--to determine the minimum effective levels needed for some of the highly effective additives, and, in addition, to determine whether use of higher concentrations would result in enhancement of elongation. The key findings are summarized in Table 2, again using the blend of Comparative Example 1 as a yardstick. Composition and property data from Table 1, Examples 3, 7, 8, and 21 have been included again to emphasize the unusual results attainable through inclusion of surfactants.
he first series of comparisons was made to determine the minimum effective level for additive No. 3 in blends which contained 72.5% filler, as compared to the base case r Of which had an elongation value of 25~. At 0.25% inclusion of Additive No. 3, the elongation value was 560%o Reduction of the Additive No. 3 level - Ex. 24 - to - 0.15% yielded an elongation ox 360% - still over 14 times than for C-1. Ex. 25 shows that 0.12~ of Additive No. 3 was only modestly effective - the elongation measured 36% - better than that for C-l, but far below that for Ex. 24.
A parallel experimental series was then made - 25 to determine the effective minimum amount for - - Additive No. 8. (C-l, vs. Ex. 8, 26, ~7 and 28). In this series, the astounding improvement in properties - - - persisted even at levels for Additive No. 8 o only 0.l2%. However, at 0.09~, the knife-edge was - 30 crossed, and elongation fell from 440% tEx. 27) to I; only 33% (Ex~ 28). Some benefit remained, but it was modest WQ are unaware of anything in the prior art that would disclose such unusual behavior for a surfa~tant~

93~3~

Additive No 7, as noted earlier Rex. 7), produced a significant but relatively small (ca.
100~) improvement in elongation vs~ the base case, at 0.25% additive level. Increasing the additive level to 0.5% Rex. 29~ produced a dramatic increase in elongation, to 540~, a totally unpredictable enhancement. Even more surprisingly, further addition ox Additive No. 7 (Examples 30, 31 and 3Z) to as high as 4.0% did not produce any further improvementO Indeed, at the 4~ additive level, the test plaques pressed from the composition showed a moderate amount of process oil exudation at the surface. All other compositions up to this point showed no tendency toward "blooming" or exudation of lS process oil.
The same test approach was also tried with Additive No. 21, which, as sold, contains only S0~
active ingredient. Initially (Ex. 21), at the 0.25%
additive level, the elongation enhancement, to 34~, was modest. Use of 0~5% additive (Ex. 33) caused a further enhancement to 47~--desirable, but not -: . . outstanding But, at 1%, the elongation rose rapid}y .~ to 580%. (Data are not included in Table 2, but the same effects occurred when Additive No. 2, which, as-I:- . 25 supplied, contains only 35~ active ingredient, was : tested at higher levels.) :

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Z :~: l s v . . , ~3~33 As with previous blends, the melt index doubled; the stiffness fell by 40%; the toughness rose well better than ten-fold; and the tensile strength dropped by about one-third. tAll are compared to the values of the blend of C-l). A further increase in the additive level to 2% and to 4~ did not produce a further change in the properties measured-^but did not harm thy overall product. In this instance (Ex.
36), the irst signs of process oil migration were noticed on close examination--but probably would not interfere with the product for most sound-deadening or molding uses. Thus, when compounding highly-filled blends of this type, it is important to consider the amount of active ingredient contained in the additive.
In a f ew instances, not shown in Table 2, use of even 4% additive in this particular blend (i.e., based on C-l) produced very little overall effect. this was true for Additives No. 19 and 20.
However, it is not possible to predict what will - happen in all cases, and a trial series is strongly :~ - recommended for any doubtful case. For example,--: : . . Additive No. 15 did not enhance blend elongation at a 2% level--but, at 4%, the elongation value rose to - : 25 well o'er 400~. Thus, a 4% additive level, or even a - higher concentration, may offer merit, and should not be dismissed arbitrarily.
: - Examples 3? to 43,_and ComParative Examples 2 and 3 . .
: :-Surfactants are effective in improving the elongation of highly filled blends even when no process oil is included in the system. This is shown by the data of Table 3. The blends of Comparative Examples 2 and 3 are at 70% and 75% filler levels, respectively. The melt index values are very low, - 5 and elongation values are poor, particularly in view 4~

~35~3 of the high resin level used. (See, for comparison, blend C-l, Table 1.) The blends are also very stiff, which would present difficulty in some end uses where flexibility is important, such as sound-deadening --textile constructions for automotive use.
Examples 37 through 41 show the striking and unexpected enhancement in elongation attainable through inclusion of relatively small amounts of surfactants. Examples 37 and 38 were made at 72.5%
filler loading--one might predic* elonsation values, based on the data of Comparative Examples 1 to 3, of about 30~ to 40% at best. Instead, use of l and 2%
Additive No. 8 increased the elongation value by a factor of 18 from the anticipated level. In addition, a very large reduction in stiffness occurred. The blends now will pass an am~ient-temperature "zero-T" bend, which C-3 does not pass.
Examples 39, 40 and 41 show that the beneficial effects discussed above can be attained with as little as 0.5% of Additive No. 8; or, at 1%
additive level, excellent results can be attained even at a 75% filler loading. -- As might be expected, highly filled plasticizer~free EVA blends are hard to mix, and reproducible results are difficult to attain. As will be shown later (Table 7), the fineness of the filler is also an important variable, which is also of great importance in unplasticiæed systems, because wet-out of the filler is difficult to attain. Where doubt or difficulty exists, the amount of surface active agent should be increased, probably to the 2~-4% level.
Example 42 was prepared to determine the 35 . effect of a further increase in filler loading upon ~3~3~

the properties of an umplas~icized blend. Now, at 80% CaCO3 load, the blend will no longer flow through a standard Melt Index test unit. This, in turn, means the blend can no longer be processed at practical rates using many commercial extruders, as prohibitive head pressure would be needed.
Nevertheless, the elongation value remained well above 400%, indicating that other uses (such as molding might be practicalf at or above 80~ filler loading, when CaCO3 is used as the filler.

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~5 LZ~3$~33 Footnotes for Table 3 (1) EVA No. 3 = "Elvax" 260 resin; 28% VAc, 72%
E; 6 M.I., E. I. du Pont de Nemours and Company Inc. -I
(2) E/VA/MAA Resin #1 = "Elvax" 4260 resin;
ethylene/vinyl acetate/methacrylic acid terpolymer; 71% ethylene/28~ vinyl acetate/l~ methacrylic acid; MI - 6~0 .

~0 : :`
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~Z~ 33 Example 43 was included to show the additional substantial benefits which can result for blends of the type of Ex. 42, if only a very 1GW (1%) amount of plasticizer is added Now, the MI value again is in a practical range for commercial extruders; the elongation, at 640%, shows that a still higher filler level should be practicable; and the stiffness has been sharply reduced.
As will be shown later, when a dense filler such as BaSO4 is used, the filler level can be increased to well above the 80% level.
Examples 44 to 52 and Comparative ExamPles 4 to 12 The use of blends of polymers has long been an art practiced by skilled compounders. Indeed, U.S. Patent 4,191~798 points out (col. 9, lo 4-7;
col. 15, 1. 38-42; col. 18, 1. 6~9) that minor property changes can be effected in highly filled ethylene copolymer blends which contain process oil by adding unrelated resins, rubberst elastomers extenders, etcO Table 4 shows the types of property changes which can be effected through the use of hydrocarbon rubber (e.g., E/P or EpDM types) as an - additive in E~A/process oil/filler systems.
The overall "base case" for comparisons made - 25 is Comparative Example 1, which contains 72.5~ filler - and 7.3~ process oil (as do all other compositions in - Table 4), plus 20~2% EVA resin. Comparative Example 4 is identical to it, except that the EVA resin has been totally replaced by E/P resin No 1. As a result of the change, the blend has become far softer and has a far higher elongation value. However, the negative aspects are severe--the composition of - Comparative Example 4 is no longer moldable; it has a `~ nno-flow" result on a melt indexer, which indicates 35 high difficulty in extruding it, and it will have a signiicantly higher cost per pound.

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) 'h 5~ 3~33 Footnotes for Table 4 (1) Ethylene/Propylene Resin #1 - Vistalon*
3708; Exxon Chemicals Company;
Ethylene/Propylene/Diene Terpolymer, Spy -Gr. 0.86; ML 1 + 8 (260F) = 44-55. Diene used is 5-ethylidene-2-norbornene.
(2) Ethylene/Propylene Resin #2 = Nordel* 1560 hydrocarbon Rubber-Du Pont Company;
Sulfur-Curable Polymer Based on Ethylene/Propylene/1,4-Hexadiene. Sp. Gr.
0085; ML 1 + 4 (250F) = 60.
(3) Ethylene/Propylene Resin ~3 = "Nordel" 1470 Hydrocarbon Rubber-Du Pont Companyu Sulfur-Curable Polymer Based on Ethylene/Propylene/ and a Nonconjugated Diene, Sp. Gr. 0.8S; ML 1 + 4 (250F) = 70

6.

*denotes trade mark l 3"333 At first glance, it might appear that mixing of Compositions C-l and C~4 might produce an average system of potential attractiveness. However, when this was done (C-5 and C-6), the initially high elongation of C-4 was essentially destroyed. Alsot the stiffness fell, but less than might have been expected, and melt index values remained quite low.
Mote now (Examples 8~ 44, 45, and 46) the unusual and unpredictable effects which resulted when 0.25~ of Additive No. 8 was added to the compositions of the corresponding comparative examples In the case of the unmodified E/P rubber, the percentage of improvement was quite modest (about 30~. By --contrast, the blends which contained up to 50~ EVA
resin (of the total resin component) showed a ten- to twenty-fold increase in elongation value.
The balance of the Examples in Table 4 confirms the results of the earlier Examples summarized in this Table. The chanye in termonomer used in making the E/P rubber and the higher viscosity level for it did not alter the effects obtained with E/P resin l The fundamental - conclusion is clear - the use of surfactants enhances the performance of EVA resins; key properties o E/P
or EPDM rubber are relatively unaffected by employment of a surface active agent - Examples 53 to 58 and Comparative Examples 13 to 18 -- - The benefits of addition of surfactants to ethylene/vinyl acetate copolymers extends also to a wide variety of other copolymers--including the so-ralled ~polyethylenes," which at times may contain small amounts ox other olefinic materials as a - comonomer. For example, in Table 5 the formulations of Comparative Example No. 13 and example No. 53 show the results ox use of surfactant No. 8 at 0.25% as an ~2 .333 additive in a blend where high density polyethylene (HDPE) is the sole polymeric material, the remaining .ingredients are filler and process oil.

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Footnotes for Table 5 (1) Polymer #1 = Alathon* 7835 - High Density (Oa96) Polyethylene; MoI~ = 3.0;
E. I. du Pont de Nemours and Company.
(2) Polymer ~2 = Dowlex* 2045 - Linear Low density (00913) Polyethylene.
Ethylene/~-Olefin Copolymer (About 15~
Octene Comonomer); M.I. = 1.14; Dow Chemical Company.
*denotes trade mark :
: 25 :~
I` 3 .

:; :::

A major increase in elongation occurs, as does a reduction it stiffness and an increase in melt index. The next two pairs of examples (C-14 and Ex.
54; C-i5 and Ex~ 55~ show that this effect continues S when ETA resins are also present, at 75~ and at 50 of the total polymer fraction.
The effects noted occur in essentially the same way when the HDPE is replaced instead with a linear low-density polyethylene (LLDPE). Once again, small amounts of a surfactant added to the comparative example blends, at widely varying LLDPE
content, produce very substantial increases in elongation, plus reduction in stiffness level.
Example 59 to 64 U.S. Patent 4,191,798 stresses the art of proper selection of a process oil or special uses.
In particular, most oils classed as naphthenic and aromatic process oils will produce highly filled EVA
blends that are nonbleeding or "dry" to the touch.
Conversely, otherwise identical blends made with most paraffinic process oils will bleed and thus are useful only in specialty applications.
Table 6 shows the results of including either Surfactant No. 3 or No. 9 in typical highly filled EVA blends made with the three different process oil types. The blends of Comparative Example 1 and Examples 3 and 9 are all made using a readily available naphthenic process oil) ~Circosol" 4240.
These compositions do not bleed. If a different naphthenic oil, ~ufflo* 2000P, or an aromatic oil, Sundex* 790, is substituted for "Circosoln4240, the overall results are very similar to those attained for Examples 3 or 9 (see Examples 59, 60 and 62, 63);
that is, in comparison to the C-l blend, the elongation values are excellent; melt index values *denotes trade mark are higher; the stiffness of the blend is appreciably lower, and the sacrifice in tensile strength is modest. Most of these statements also apply to the blends (Ex. 62 and 65) which were made with a paraffinic process oil The principal differences are that the blends are now far softer than the C-l blend, and the blends "bleed" severely.
In compounding highly filled EVA blends which contain process oils and additives, it is clear that the compounder must take great care to be certain the final product will prove suitable for its intended use. Interactions can well occur which might lead to unanticipated side effects. For example, we have made some blends which showed no tendency to "bloom" when the additive level was low--e.g. r 0.25 to 0.5~. In a few instances, as levels of additives were increased, the nonblooming"
blends would begin to "bloom". Any blend must thus by checked with considerable care to be certain all 20 final goals are met~-not just the enhancement of one particular property. -: The synthetic organic surfactants art not the only class of additives which can enhance elongation and modify stiffness, melt index, etc. at very low addition levels. Naturally occurring fat~yacids and selected derivatives of them can also yxoduc s~im~lax re$ult.~t Thus its c Sue of a co pending application, Canadian Serial No. 419 225, filed Jan. 11, 1983 of F. G. Schumacher and W. Yllo.
Other additives also can be used to produce beneficial effects. For example, organosilanes have some degree of activity in enhancing the elongation of filled EVA blends.
In addition, they caused an increase in tensile strength, which is quite diferent from all other additives studies. Thus, the silanes may prove ~3~3~
highly attractive in combination with organic surfactants. Also organotitanates have been used in filled systems to improve pigment wetting or dispersion. Here, too, combining the ~itanat2s with the surfactants disclosed herein should provide unusual blend properties for specialty uses.

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_ 5: - ' 3.~33 Examples 65 to 70 and Comparative Examples 19 and 20 The filler used in all of the Examples heretofore was No. g whiting, which is a logical choice because of reasonable purity, appropriate 5 particle size, availability of limestone, and a moderate price. However, where special effects are desired, it is possible to change the filler type, both physically and chemically. In so doing, filler morphology can also be changed widely. Some of these 10 changes are illustrated in Table 7.
Comparative Example 19 shows properties for a 60%-illed system where 1/4 of the whiting filler has been replaced by clay. Clay is a very fine, active, plate-like filler, not normally used in EVA f 15 systems, as the clay attacks EVA resins (cf. U.S.
Patent 4,222,9~4-blends of clay, processing oil, and EVA copolymers) unless a protective agent suck as process oil is present. Further, the resin system has been changed to evaluate a high MI type, EVA No.
20 4, at 400 MI. Despite these two marked changes in t.
composition, once again, the employment of 0.5% of - - Additive No. 8, as in Example 65, produces a six-fold - increase in elongation, and a S0+~ reduc ion in ,r_.
stiffness for the compound.
Further changes in filler content are shown --by Examples C-20 and 66, where Atomite*~ filler i5 -.
used to replace No. 9 whiting. nAtomite" CaCO3, is - far iner than is No. 9 whiting, nevertheless, 0.5% ¦
of Additive No. 9 produces a 30-fold elongation -30 enhancement, a nearly three-fold melt index increase, and a modest reduction in stiffness for the compound. Then if the "Atomite" is replaced by the ! -- less-dense hydrated alumina (Example 67), a further I-increase in filler surface results. At this point, I-35 . the amount of additive is no longer sufficient - and *denotes trade mark .....
.......
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",','',-'.''"' the elongtion of the lend of ex. 67 drops very sharply to only 25~. By further increasing the level of additive to about 4~, (Example 68), the elonyation of the blend is restored to the 600% level.

.

: 25 .

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35~3 Footnotes for Tablel (l) EVA #4 = "Elvax" 310 Resin, E. I. du Pont de Nemours and Company, Inc. 25% Vac; 75~ E;
MI = 400.
5 (2) "Atomite" - A finely ground (approximately 2.5 micron average) limestone filler, primarily CaCO3, ex Thompson, Weinman Company, Cartersville, GA. lO0~ pastes 325 mesh.
lO (3) Hydrated Alumina - Grade KC-100, Al2O3-3H2O, 98~ mint iner than 325 mesh, supplied by A. B. Wood Company, Charlotte, NC.
(4) No. 22 Barytes - A heavy filler which has a density of about 4.4 g/cm3; primarily BaSO4, ex Thompson, Weinman Co. Approx.
99O5% finer than 325 mesh.

' :;
: 25 : 30 :
.

.

3~333 ~6 The final Examples for Table 7 show the further effects possible through use of a dense filler. Barytes, 4.4 Sp. Gr.~ is a very satisfactory filler for systems which employ surfactants as additive Jo enhance blend properties, as shown by Examples 69 and 10. The elongation for Examples 69, at 730%, is far in excess of the needs for many sound-deadening sheet products. Example 70 was prepared, with a barytes level of 88% by weight -containing only 6.5% resin binder. Nevertheless, byuse of lo of Additive No. 9, the final product has a MI value of 5 - thus indicating extrudability - an elongation value of 700~, and a very low stiffness level. Thus, it appears entirely practical, with barytes, to make a useful EVA-based blend with 90-94%
filler loading.
While not demonstrated, one skilled in the art can readily conceive of other variants possible with still different filler types. For example, low-density fillers such as yarns, wood fiber, etc., when used at 20-60% filler level, should provide products which can be formed into useful constructions. Alternately, very dense fillers, such as lead, lead oxide, etch should readily permit - 25- preparation of surfactant-enhanced compositions which will contain in the range of 95-96% filler - yet be flexible, extrudable~ and have a 5p. Gr. of well above 4. (The Sp. Gr. of litharge, PbOI is 9.3, while that of metallic lead is over ll.) ; 30 Examples ?1 to 75 and Comparative Examples 21 to 25 In addition to the good results attained with HA resins, parallel tests summarized in Table I- 8 show that the same beneficial effects occur when E/EA, E/IBA, E/MMA, and E/VA/M~A resins are substituted for E/VA resins. In all vases, the , ,, 3~3~3 addition of small amounts of Additives 8 or 9 enhanced elongation values for test strips by from 10 to over 30-fold. Also, strip stifness was lowered appreclably in most instances. ~~

;

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l g JJ 0 5~ t'~ ~s3 us ~8 3~3 ~9 Footnotes for Table 8 .
(1) E/EA Resin #l - Ethylene/ethyl acrylate copolymer, Grade DPDA 6182 NT; contains about lS~ EA; 85~ E; M.I. - about 1.5; ex Union Carbide Corporation (2) E/IBA Resin #1 - Ethylene/isobutyl acrylate copolymer; 20% IBA~and 80% E; 2.5 M.I.
(3) ~/MMA Resin #1 - 2thylenetmethyl methacrylate copolymer; 18% MMA; 82% E; 2.2 M.I.
(4) E/VA/MAA Resin #2 = nElvaxn 4355 Resin:
En I. du Pont de Nemours and Company, Inc.
Ethylene/vinyl acetate/methacrylic acid terpolymer; 74% E; 25% VAc; l MAA; 6.0 M.I.
15 (5) E/MA Resin #1 = Ethylene/methyl acrylate copolymer; 20% MA; 80g E; 2 M.I.

: : 25 : 30 : ::

.

3~33 Tests employing an ethylene/methyl acrylate copolymer at different filler levels showed that blend properties are particularly and beneficially affected by inclusion of Additive No. 8 at a moderate (2.5~ level. The enhancement in elongation values from 12~ for Comparative Example 25 to 320% for Example 75 is far beyond any prediction based on prior art. In addition, the over lO-fold increase in MI, and the 75% reduction in stiffness for comparable strips, are both spectacular.
Examp es 76 to 80 and Comparative Examples 26 to 29 Table 9 summarized certain combinations that can be employed to augment the properties of highly filled ethylene copolymer blends. Comparative Examples l and 26 show that the blend properties for C-l can be enhanced by the use of the polymer alloy principler Addition of EVA No. 5 as a replacement for a part of the EVA No. 1 content improves the elongation of the blend of C-l about 5-fold. (This discovery is the subject matter 20 of and is more fully described in Canadian Patent l 167 992 of T. T. Schenck, which issued 1984 May 22.) However, when 1% of Additive No. 8 is included in the blend of C-26, there is an additional 4-fold enhancement of blend elonga-tion (cf. Example 76~.
The results of C-27 and Example 77 show another means to enhance blend properties. The 470%
elongation shown by C-27 is far beyond what might be expected for this composition. The improvement resulted from inclusion of a small amount of polyester plasticizer in place of part of the process oil component. This discovery is the subject matter of and is more fully described in Canadian Patent 1 169 990 of M.C. Couyhlin, which issued 1984 June 26. Indusion of a small amount of Additive No. 8 33~3 (only 0.5%3 wlll produce a further 15% improvement in elongation (Ex. 77) and, in addition, will increase the melt index nearly two-fold and reduce the stiffness of the strip by almost one half. Thus, combining these ingredients provides a skilled formulator with additional means to attain a desired balance of properties.
Binary compositions of an ethylene-containing thermoplastic resin plus appreciable vanities of a process oil--say, in a 3:1 ratio by weight--will, when warm, be fluid and adhere well to plastics, textile webs, etc. However, when filler is added as a third COmpQnent~ the dry filler will make the filled resin charge progressively less fluid--less tacky--and thus adhere less well to substrates. For blends where filler levels are high--say, 70~ and over--poor adhesion to substrates may pose a problem to a manuacturer of - composite sound-deadening carpeting. We explored the effect of the use of tackifiers on the improved elongation properties that surfactants impart to the highly filled, oil-containing EVA blends. Data for . ; . these tests are provided by Comparative Example 28 and Example 78.
. 25 lends with 76% filler, and no tackifier, show little or no tack - even a rating of 1 on the tack scale i5 seldom obtainedO Also, as shown in I. C-28, the physical properties of tackifier-containing : blends are poor, as evidenced by the very low (10%) elongation value for C-28. The tack rating for C-28 is also poor, at only 1.5 units To make the blend of Ex. 78, with a high (4.0) tack rating, the amount of tackifier was raised to the 5% level, at the -I expense of the EVA resin (15% in C-28, reduced to 1 - 35 -in Ex. 78). This change should make the blend more tacky - which it did - and should totally destroy elongation, etc. properties, as the tackifier per se has very poor tensile and elongation resistance. To compensate, only 0.5% of surfactant No. 8 was added to the system, with startingly good results:
a. The tack rating is good, at 4Ø
b. The MI has been increased c. The elongation, instead of vanishing, has been increased over 60-fold, and d. The blend is now soft and flexible, rather than stiff.
The blends of C-29, Ex. 79 and Ex. 80, show the same effects as noted abovel when a different EVA --resin with no inherent tack tendency is employed, and tackifier No. 2 is substituted for tackifier No. 1.
Additive No. 8 plus the tackifier haze a. markedly improved the tack ratins, b. decreased the MI, c. sharply enhanced the elongation, and d. made a very stiff blend soft and flexible.
In summary, the use of surfactants in ethylene copolymer based blends provides an -I: . outstanding means to enhance the elongation of blends which contain very high levels of inert fillers The method is effective for a wide variety of ethylene copolymers; for illers of widely varying specific gravities, particle sizes, and chemical - compositions. The method is effective for common : : 30 types of process oils - and for systems where the process oil contains a polymeric-type plasticizer : . ingredient. It also is effective for compounds wher - . ethylene-~ype polymers are used as polymer alloys -- for systems based on ethylene homopolymer - and where 35 -the polymer system also contains synthetic rubber.

......

"3~3 It is manifestly impossible to illustrate all variants of 50 complex a system. A skilled compounder can effect many other variants, without departilre from the teachings of this invention. All 5 required final properties should be tested to confirm the suitability of a given combination of ingredients for the intended purpose.

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, l o o_~ o o I! ~,.3 a En o f o o on o go ED I I I I I I
r-JO d O
5P O o us f 0 . . . I I . . I I I I . .
I C.) I` O o f _l O Lo 0 Us U
Ye N,_ v ~3 to: sup a3 v3 sl m C , _ o o Z Z 0 V~
l us o ;1 N Lo f ta V
O O O W ~4-~ :~ X C O
z z;
g go O
Ed IY

" ., 3~
Footnotes for Table 9 (1) EVA 45 = "Elvax'l 40 resin, En I. du Pont de Nemours and Company, Inc., 40.5~ VAc;
59.5% E; 57 M.I.
5 (2) EVA ~6 = NElvax" 470 resin, E. I. du Pont de Nemours and Company, Inc., 18% VAc; 82%
E; 0.7 M.I.
(3) EVA ~7 = "Elvax" 67~ resin, E. I. du Pont de Nemours and Company, IncO, 12% VAc; 88 E; 0.3 M.I.
~4) Santicizer* 4~9 - medium molecular weight polyester type plasticizer from Monsantv:
Sp.Gr. 1.1, freezing point -60C, acid --number 22 mg KOH/g, viscosity Q 25C is 50 stokes.
(5) Tackifier No. 1 = nPiccovar" L-60 (Hercules, Inc.) low softening point, aromatic type resin.
t6) Tackifier No. 2 = ~Piccopa}e" 100 [Hercules, : 20 Inc.) aliphatic low molecular weight hydrocarbon resin.
~7) The tack ratings were the average of values obtained by several observers, who used a common subjective standard from zero to 4~
2S 0 - Not tacky to touch. Sample plaque will slide easily along a smooth surface.
1 = Perceptible tack to fingerO Plaque no longer slides easily. --2 - Moderate tack to finger. Plaque slides with difficulty.
. 3 = Sticky to touch. Samples will nearly : adhere to observer's zingers.
: : 4 = Strongly stic,ky. Samples will stick in inverted position for S-10 seconds or 35 - longer.
: : *denotes trade mark : 75 . :

Claims (22)

76

1. A composition comprising (a) from 0 to about 50% by weight of at least one copolymer of ethylene with at least one comonomer selected from the group consisting of vinyl esters of saturated carboxylic acids wherein the acid moiety has up to 4 carbon atoms, unsaturated mono- and dicarboxylic acids of 3 to 5 carbon atoms, salts of said unsaturated acids, and esters of said unsaturated acids wherein the alcohol moiety has 1 to 8 carbon atoms, the ethylene content of said copolymer being from about 40 to about 95% by weight, the comonomer content of said copolymer being from about 5 to about 60% by weight, and the melt index of said copolymer being from about 0.1 to about 400, provided that when said copolymer of ethylene is an ethylene/vinyl ester or ethylene/unsaturated mono- or dicarboxylic acid ester copolymer said copolymer can contain up to about 15 percent by weight of carbon monoxide or sulfur dioxide; provided, that when the olefin polymer of paragraph (e) is absent, the amount of ethylene copolymer is at least about 5% by weight;
(b) from 0 to about 20 percent by weight of at least one plasticizer selected from the group consisting of processing oils, epoxidized oils, polyesters, polyethers, and polyether esters;
(c) from about 40 to about 90% by weight of filler;
(d) from about 0.05 to about 5% by weight of at least one surface active agent selected from the group consisting of alkanol amides; betaine derivatives;
block copolymers comprising a series of condensates of ethylene oxide with hydrophobic bases formed by condensing propylene oxide with propylene glycol;
ethoxylated compounds comprising alcohols, alkyl phenols, amines and amides; sulfonated derivatives comprising alkyl sulfonates, aryl sulfonates, alkyl-aryl sulfonates, amine and amide sulfonates, olefin sulfonates, sulfosuccinates, sulfonated fatty acid esters, sulfonates of ethoxylated alkyl phenols and of oils and of fatty acids, naphtholene and alkyl naphtholene sulfonates, condensed naphtholene sulfonates, naphthalene and alkyl naphthalene sulfonates and petroleum sulfonates, and dodecyl and tridecyl benzene sulfonates; dodecyl and tridecyl sulfonic acids; sulfates of alcohols, of ethoxylated alcohols, of ethoxylated alkyl phenols, of oils, of fatty acids, of fatty esters, alkaryl sulfates, and sodium, ammonium and amine salts thereof; phosphate derivatives comprising phosphate esters, phosphate alcohol ethoxylates, phosphate ether ethoxylates, phosphate alkyl acids and phosphate alkyl quaternaries; and quaternary surfactants;
(e) from 0 to about 55% by weight of olefin polymer selected from the group consisting of low density branched polyethylene, high density linear polyethylene, linear copolymers of ethylene and another olefin comonomer, polypropylene and copolymers of propylene and ethylene where the ethylene content is up to 20% by weight provided that when the ethylene copolymer of paragraph (a) is absent the amount of olefin polymer is at least about 5% by weight;
(f) from 0 to about 50% by weight of elastomeric polymer: and (g) from 0 to about 30% by weight of tackifier.

2. The composition of Claim 1 wherein said surface active agent is selected from the group consisting of alkanol amides; betaine derivatives;
block copolymers consisting essentially of a series of condensates of ethylene oxide with hydrophobic bases formed by condensing propylene oxide with propylene glycol; ethoxylated compounds consisting essentially of ethoxylated alcohols, alkyl phenols, amines and amides; sulfonated derivatives consisting essentially of alkyl sulfonates, alkyl-aryl sulfonates, amine and amide sulfonates, sulfonated fatty acid esters, sulfonates of ethoxylated alkyl phenols and of oils and of fatty acids, naphtholene and alkyl naphtholene sulfonates, and condensed naphtholene sulfonates and dodecyl and tridecyl benzene sulfonates; sulfates of alcohols, of ethoxylated alcohols, of fatty acids, alkaryl sulfates, and sodium, ammonium and amine salts thereof; phosphate derivatives consisting essentially of phosphate esters, phosphate alcohol ethoxylates, phosphate ether ethoxylates, phosphate alkyl acids and phosphate alkyl quaternaries; and quaternary surfactants.

3. The composition of Claim 2 wherein said copolymer of ethylene is present in an amount of from about 5 percent to about 50 percent by weight and is a mixture of at least two copolymers of ethylene, copolymer (A) and copolymer (B), each copolymer having at least one polar comonomer selected from the group consisting of vinyl esters of saturated carboxylic acids wherein the acid moiety has up to 4 carbon atoms, unsaturated mono- or dicarboxylic acids of 3 to 5 carbon atoms, the salts of said unsaturated acids, and esters of said unsaturated acids wherein the alcohol moiety has 1 to 8 carbon atoms, copolymer (A) having a polar comonomer content of from about 2 to about 30 percent by weight, an ethylene content of from about 70 to about 98 percent by weight and a melt index of from about 0.1 to about 20, and copolymer (B) having a polar comonomer content of from about 28 to about 60 percent by weight, an ethylene content of from about 40 to about 72 percent by weight and a melt index of from about 5 to about 1000, provided that the polar comonomer content of copolymer (B) is at least 12 percent by weight higher than the polar comonomer content of copolymer (A) and the weight ratio of copolymer (A) to copolymer (B) is from about 99/1 to about 55/45.

4. The composition of Claim 3, wherein (a) said mixture of at least two copolymers of ethylene is present in an amount of from about 8 to 35 percent by weight, copolymer (A) having a polar comonomer content of from about 5 to about 28 percent by weight, an ethylene content of from about 72 to about 95 percent by weight and a melt index of from about 0.3 to about 10, and copolymer (B) having a polar comonomer content of from about 30 to about 60 percent by weight, an ethylene content of from about 40 to about 70 percent by weight and a melt index of from about 10 to about 200, provided that the polar comonomer content of copolymer (B) is at least 15 percent by weight higher than the polar comonomer content of copolymer (A); (b) said plasticizer is present in an amount of from about 2 to about 15 percent by weight wherein from 0 to about 50% by weight of said plasticizer is a plasticizer other than processing oil; (c) said filler is present in an amount of from about 55 to about 90 percent by weight, (d) said surface active agent is present in an amount of from about 0.1 to about 2.5% by weight;
(f) said elastomeric polymer is present in an amount of from 0 to about 25% by weight; and (g) said tackifier is present in an amount of from 0 to about 20% by weight.

5. The composition of Claim 4, wherein the ratio of copolymer (A) to copolymer (B) is from about 97/3 to about 60/40.

6. The composition of Claim 2 wherein (a) said copolymer of ethylene is present in an amount of from about 8 to about 35 percent by weight, the ethylene content of said copolymer being from about 45 to about 91% by weight, the comonomer content of said copolymer being from about 9 to about 55 percent by weight and the melt index of said copolymer being from about 0.1 to about 50;
(b) said plasticizer is present in an amount of from about 2 to about 15 percent by weight wherein from 0 to about 50% by weight of said plasticizer is a plasticizer other than processing oil:
(c) said filler is present in an amount of from about 55 to about 90 percent by weight; (d) said surface active agent is present in an amount of from about 0.1 to about 2.5% by weight; and (g) said tackifier is present in an amount of from 0 to about 20% by weight.

7. The composition of Claim 6 wherein said filler is selected from the group consisting of calcium carbonate, barium sulfate, hydrated alumina, clay, magnesium carbonate, calcium sulfate, silica, iron, lead, or oxides thereof, mica, talc and wollastonite, flyash, cement dust, yarns, wood flour, nut shells, ground rice hulls and mixtures thereof.

8. The composition of Claim 7 wherein said filler is selected from the group consisting of calcium carbonate, barium sulfate, hydrated alumina, and mixtures thereof.

9. The composition of Claim 8 containing up to about 15% by weight of a polymer selected from the group consisting of ethylene/carbon monoxide, and ethylene/sulfur dioxide.

10. The composition of Claim 8 wherein said surface active agent is selected from the group consisting of sulfonated derivatives consisting essentially of alkyl sulfonates, alkyl-aryl sulfonates, amine and amide sulfonates, sulfonated fatty acid esters, sulfonates of ethoxylated alkyl phenyls and of oils and of fatty acids, naphtholene and alkyl naphtholene sulfonates, and condensed naphtholene sulfonates; sulfates of alcohols, of ethoxylated alcohols, of fatty acids, alkaryl sulfates, and sodium, ammonium and amine salts thereof; and phosphate esters.

11. The composition of Claim 10 wherein said copolymer of ethylene is selected from the group consisting of ethylene/vinyl acetate, ethylene/acrylic acid and its ionomers, ethylene/methacrylic acid and its ionomers, ethylene/methyl acrylate, ethylene/ethyl acrylate, ethylene/isobutyl acrylate, ethylene/normal butyl acrylate, ethylene/isobutyl acrylate/methacrylic acid and its ionomers, ethylene/normal butyl acrylate/methacrylic acid and its ionomers, ethylene/isobutyl acrylate/acrylic acid and its ionomers, ethylene/normal butyl acrylate/acrylic acid and its ionomers, ethylene/methyl methacrylate, ethylene/vinyl acetate/methacrylic acid and its ionomers, ethylene/vinyl acetate/acrylic acid and its ionomers, ethylene/vinyl acetate/carbon monoxide ethylene/methyl acrylate/carbon monoxide, ethylene/normal butyl acrylate/carbon monoxide, ethylene/isobutyl acrylate/carbon monoxide, ethylene/vinyl acetate/monoethyl maleate and ethylene/methyl acrylate/monoethyl maleate.

12. The composition of Claim 11 wherein said copolymer of ethylene is selected from the group consisting of ethylene/vinyl acetate, ethylene/ethyl acrylate, ethylene/methyl acrylate, ethylene/isobutyl acrylate, ethylene/methyl methacrylate, and ethylene/vinyl acetate/methacrylic acid.

13. The composition of Claim 12, wherein (a) said copolymer of ethylene is present in an amount of from about 12 to about 25 percent by weight; the ethylene content of said copolymer being from about 72 to about 88 percent by weight, the comonomer content of said copolymer being from about 12 to about 28 percent by weight, and the melt index of said copolymer being from about 1 to about 10;
(b) said plasticizer is present in an amount of from about 4 to about 10 percent by weight when the filler is selected from the group consisting of calcium carbonate and hydrated alumina and from about 3 to about 10 percent by weight when the filler is barium sulfate, wherein from 0 to about 20% by weight of said plasticizer is a plasticizer other than processing oil;
(c) said filler is present in an amount of from about 65 to about 85 percent by weight when the filler is selected from the group consisting of calcium carbonate and hydrated alumina and from about 70 to about 90 percent by weight when the filler is barium sulfate; (d) said surface active agent is present in an amount of from about 0.12 to about 0.75% by weight; (f) said elastomeric polymer is present in an amount of from 0 to about 12% by weight; and (g) said tackifier is present in an amount of from 0 to about 15% by weight.

14. The composition of Claim 13 wherein said copolymer of ethylene is present in an amount of from about 12 to about 25% by weight, and is a mixture of at least two copolymers of ethylene, copolymer (A) and copolymer (B), each copolymer having at least one polar comonomer selected from the group consisting of vinyl esters of saturated carboxylic acids wherein the acid moiety has up to 4 carbon atoms, unsaturated mono- or dicarboxylic acids of 3 to 5 carbon atoms, the salts of said unsaturated acids, and esters of said unsaturated acids wherein the alcohol moiety has 1 to 8 carbon atoms, copolymer (A) having a polar comonomer content of from about 10 to about 25 percent by weight, an ethylene content of from about 75 to about 90 percent by weight and a melt index of from about 0.5 to about 2 and wherein copolymer (B) has a polar comonomer content of from about 33 to about 60 percent by weight, an ethylene content of from about 40 to about 67 percent by weight and a melt index of from about 15 to about 100, and wherein the ratio of copolymer (A) to copolymer (B) is from 95/5 to about 65/35, provided that the polar comonomer content of copolymer (B) is at least 18 percent by weight higher than the polar comonomer content of copolymer A.

15. The composition of any one of Claim 1, Claim 2 and Claim 10, in the form of a sound-deadening sheet.

16. The composition of Claim 13 or Claim 14, in the form of a sound-deadening sheet.

17. A carpet having a backside coating consisting essentially of the composition of any one of Claim 1, Claim 2 and Claim 10.

18. A carpet having a backside coating consisting essentially of the composition of Claim 13 or Claim 14.

19. An automotive carpet having a backside coating consisting essentially of the composition of any one of Claim 1, Claim 2 and Claim 10.

20. An automotive carpet having a backside coating consisting essentially of the composition of Claim 13 or Claim 14.

21. A foam, fabric, or scrim having a backside coating consisting essentially of the composition of any one of Claim 1, Claim 2 and Claim 10.

22. A foam, fabric, or scrim having a backside coating consisting essentially of the composition of Claim 13 or Claim 14.