Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – At least one aryl ring which is part of a fused or bridged...
Reexamination Certificate
1999-10-04
2002-11-26
Szekely, Peter (Department: 1714)
Synthetic resins or natural rubbers -- part of the class 520 ser
Synthetic resins
At least one aryl ring which is part of a fused or bridged...
C524S271000, C524S474000, C524S499000, C525S133000, C525S210000, C525S211000, C525S240000, C156S176000, C156S334000, C428S009000
Reexamination Certificate
active
06486246
ABSTRACT:
BACKGROUND OF THE INVENTION
The present invention relates to a hot melt adhesive polyolefin composition. The polyolefin composition comprises both thermoplastic and elastomeric polyolefins. It also relates to articles prepared with the said adhesive composition.
The adhesive composition of the present invention can be used in several fields. It is particularly suitable for acting as a glue in tufted or needle punched carpets, the fibres of which are fixed to the primary carpet backing by the said hot melt adhesive composition. The adhesive compositions of the present invention are more particularly suitable for tufted nylon or polyester or polyolefin pile carpets wherein the primary backing is made of polyester or polyolefin.
Hot melt adhesive compositions comprising thermoplastic polyolefins are known in the art. Examples of hot melt adhesive compositions are described in published European patent application 671431 (Himont Incorporated). Said compositions are suitable for producing films and bonding the layers to each other, but are not specifically suitable for being employed as adhesives in the field of tufted or needle punched carpets.
The main drawback shown by the above hot melt composition is the too low adhesive force, in particular when they are used in non-polyolefin carpets (polyamide for instance).
In addition, although the exemplified compositions have a low viscosity, i.e. 10,000 mPa·sec, the method to obtain this viscosity is disadvantageous. The high amount of peroxides to be used makes the compositions described hardly suitable from an industrial and economical viewpoint.
It would be desirable to make it possible to have polyolefin compositions with a low viscosity but without the above-mentioned drawbacks due to the high amount of peroxides and also showing good adhesive properties.
SUMMARY OF THE INVENTION
The Applicant has now found a hot melt adhesive polyolefin composition consisting essentially of thermoplastic and elastomeric polyolefins, showing higher adhesive properties than the ones of the above-mentioned compositions.
The compositions now developed do not present the above-mentioned drawbacks and show good tuft-lock force as well as good abrasion resistance.
Another advantage of the hot melt composition of the present invention relates to their high flexibility and good dimensional stability.
An object of the present invention therefore is a hot melt adhesive polyolefin composition having viscosity from 7,000 to less than 500,000 mPa·sec, according to ASTM D 3236-73, at 190° C., preferably from 10,000 to 80,000 mPa·sec, comprising (by weight):
I. 5-85%, preferably 15-60%, most preferably 15-45%, of a crystalline propylene polymer selected from a homopolypropylene and copolymer of propylene with ethylene or a C
4
-C
10
&agr;-olefin or blends thereof, having a isotactic index from 80 to 98;
II. 5-85%, preferably 15-60%, most preferably 15-45%, of a heterophasic polyolefin composition comprising (i) a crystalline propylene polymer and (ii) an amorphous copolymer of ethylene with propylene or a C
4
-C
10
&agr;-olefin or blends thereof; said copolymer (ii) containing less than 40% of ethylene, preferably from 25 to 38%;
III. 10-75%, preferably 10-40%, of a material selected from aliphatic hydrocarbon resin, terpene/phenolic resin, polyterpenes, rosin, rosin esters and derivatives thereof and a blend thereof; and optionally
IV. a mineral paraffinic or naphtalenic oil or an amorphous poly(&agr;-olefin) having low molecular weight or a mixture thereof.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Preferably the present composition has the above propylene polymer (I) and composition (II) in ratio from 1.3 to 0.7.
Component (I) is preferably a propylene homopolymer. In the case where component (I) is a copolymer, the comonomer content ranges preferably from 1 to 10% by weight.
Preferably component (I) has a melt flow rate (MFR), according to the method of ASTM D 1238, condition L, in the range from 250 to 2000 dg/min.
Component (II) has preferably MFR higher than 5 dg/min, more preferably from 20 to 150 dg/min, in particular from 5 to 150 dg/min.
A preferred example of heterophasic polyolefin composition (II) is as follows (percentage by weight):
(A) 5-50%, preferably 10-40%, of a crystalline propylene homopolymer with an isotactic index greater than 80%, preferably from 85 to 98%, or crystalline copolymer of propylene with ethylene or a C
4
-C
10
&agr;-olefin or a mixture thereof; said copolymers containing more than 85% of propylene and having an isotactic index greater than 80%;
(B) 0-20%, preferably 0-15%, of a crystalline copolymer fraction containing prevailingly ethylene, such as ethylene copolymer with propylene or a C
4
-C
10
&agr;-olefin or a mixture thereof;
said fraction being insoluble in xylene at ambient temperature, i.e. 25° C.; and
(C) 40-95%, preferably 50-75%, of an elastomeric copolymer fraction of ethylene with propylene or with a C
4
-C
10
&agr;-olefin or a mixture thereof, and optionally with minor amounts of a diene; said copolymer fraction containing ethylene in an amount smaller than 40%, preferably from 20 to 38%, and being soluble in xylene at ambient temperature.
Examples of the preferred heterophasic composition are described in published European patent application EP-A-0 472946 (Himont Inc.).
As a way of example the total amount of ethylene in heterophasic composition (II) is 15 to 35% by weight.
Preferably the propylene content in the crystalline copolymers (I) as well as in the crystalline copolymers present in (II) is 90 to 99% by weight. The isotactic index is determined as the insoluble fraction in xylene at 25° C. (see note 1 below).
The amount of ethylene in fraction (B) can vary broadly. Examples of copolymer (B) have 75% by weight or more, preferably at least 80% by weight, of ethylene content with respect to the total weight of (B). For example, the copolymer is an essentially linear copolymer of ethylene with propylene, such as a linear low density polyethylene (LLDPE).
Examples of C
4
-C
10
&agr;-olefins that can be present in crystalline copolymers (I) as well as in heterophasic composition (II) are 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene and 1-octene.
When present, the diene units in fraction (C) of (II) are preferably in an amount from 1% to 10% by weight with respect to the total weight of (C). Examples of dienes are butadiene, 1,4-hexadiene, 1,5-hexadiene and ethylene-1-norbornene.
The above-mentioned heterophasic composition (II) can be prepared by melt blending the polymer components such as fractions (A), (B) and (C) in the fluid state, that is at temperatures higher than their softening or melting point, or by sequential polymerisation in two or more stages in the presence of a highly stereospecific Ziegler-Natta catalyst. In particular the catalyst system used comprises (i) a solid catalyst component including a titanium compound and an electron-donor compound, both supported on magnesium chloride and (ii) an Al-trialkyl compound and an electron-donor compound.
Preferably heterophasic composition (II) has melt flow rate in the range of about 5-150 dg/min.
The desired values of MFR of components (I) and (II) within the limits defined by the present invention are obtained according to methods known in the art, for instance directly in the polymerisation process or by chemical visbreaking, i.e. a process of controlled free radical degradation of the polymer during the extrusion process, for example. Said visbreaking process is carried out, for instance, by mixing the components in the presence of radical initiators such as organic peroxides. Examples of suitable radical initiators are: dicumyl peroxide, 2,5-dimethyl-2,5-bis(butylperoxy)hexane, 2,5-dimethyl-2,5-bis(butylperoxy)hexyne-3. The process is carried out by using the proper quantities of a degrading agent as is well known in the art.
Typical component (III), also commonly called tackifier, used in the adhesive compositions of the invention is added to act as compatibilizer between the apolar polyolefin and the polar substrate (
Montell Technology Company BV
Szekely Peter
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