Title of Invention

BLEND FOR USE IN AUTOMOBILE APPLICATION

Abstract The present invention relates to a blend comprising metallocene polypropylene and an elastomer for automobile parts, characterized in that said blend has low volatile organic compounds emissions. The invention also relates to the use of said blend in parts for automobiles.
Full Text BLEND FOR USE IN AUTOMOBILE APPLICATION
Field of the invention
The present invention relates to a blend comprising polypropylene and an
elastomer component for use in automotive applications, especially for use in
interior automobile applications.
Background of the invention
Polypropylene has taken on an important role as base material for the
automotive industry. Today, it is widely used for exterior automotive applications,
such as bumpers and side sills, as well as interior automotive applications, such
as dashboards and interior trim. Polypropylene offers the advantages of having
a low density, good mechanical strength, good heat resistance, good chemical
resistance etc. as well as that of being a low-cost material in comparison to
other suitable materials.
Originally the limited impact strength of polypropylene Was a limiting factor in its
use for automotive applications. This problem has, however, been overcome by
blending polypropylene with elastomers. The elastomer component of the blend
results in improved impact strength and an increased brittle temperature. Blends
of this type are for example disclosed in document US 6,797,779. Among a
large number of possible polypropylenes metallocene-catalyzed polypropylenes
are included as well.
Further, US-A-2004/0044107 discloses interior automotive parts comprising
(A) a crystalline homopolypropylene,
(B) a crystalline homopolypropylene and an ethylene-propylene copolymer
rubber, said rubber having an intrinsic viscosity on 4.0 to 7.0 dl/g (decalin,
135°C), ethylene content from 45 % to 80 % by mass and the rubber being
present in at least 10 % by mass of the homopolypropylene,
(C) a crystalline homopolypropylene and an ethylene-propylene copolymer
rubber, said rubber having an intrinsic viscosity on 5.0 to 10 dl/g (decalin,
135°C), ethylene content from 45 % to 80 % by mass and the rubber being
present in at least 10 % by mass of the homopolypropylene, and
(D) an ethylene/ a-olefin rubber.
The resulting interior automotive parts are characterized by good molding
properties and a good balance of physical properties, as well as good
appearance, lower gloss and scratch resistance. The homopolypropylene (A)
has a fraction soluble in boiling p-xylene, which suitably is 6.0 % by mass or
less, preferably 3.0 % by mass or less, more preferably 0.1 to 2.0 % by mass.
US-A-2007/0037914 discloses automotive parts formed from filled thermoplastic
polyolefin compositions, wherein the filled thermoplastic compositions comprise
a highly crystalline isotactic propylene homopolymer, an ethylene/a-olefin
elastomeric impact modifier, and a reinforcing grade of a platy filler, for example
talc. The invention aims at providing automotive parts that have excellent
thermal and mechanical properties. The document makes not mention of
emissions originating from such automotive parts.
In light of an overall reduction of emissions from cars the emission of volatile
organic compounds (VOC) coming from polypropylene-based automotive parts
has recently attracted special attention.
None of the above-cited documents addresses this problem. It is noted in this
respect that a low level of solubles e.g. in boiling p-xylene cannot be taken as an
indication of low VOC emissions. It has to be kept in mind that the volatile
organic compounds (VOC) are removed together with the p-xylene when the p-
xylene is removed for the isolation of the solubles.
It is therefore an object of the present invention to provide polypropylene-based
blends showing good mechanical properties and in particular good rigidity and
impact strength while at the same time having low emissions of volatile organic
compounds (VOC).
Summary of the invention
Accordingly, the present invention provides an automobile part comprising a
blend, said blend comprising
(a) 99.1 - 20 wt% of a polypropylene produced in the presence of a
metallocene-based catalyst, and
(b) 0.1 - 50 w% of an elastomer,
said blend having less than 45 ppm of volatile organic compounds (determined
in accordance with VDA-278).
The invention also relates to the use of a blend comprising
(a) 99.1 - 20 wt% of a polypropylene produced in the presence of a
metallocene-based catalyst, and
(b) 0.1 - 50 w% of an elastomer,
for producing automobile parts having less than 45 ppm of volatile organic
compounds (determined in accordance with VDA-278).
Detailed description of the invention
The blends used in the present invention comprise
(a) 99.1 - 20 wt% of a polypropylene produced in the presence of a
metallocene-based catalyst, and
(b) 0.1 - 50 w% of an elastomer.
The metallocene polypropylenes, i.e. the polypropylenes produced in presence
of a metallocene-based catalyst, used in the present invention can be
homopolymers or copolymers of propylene and at least one comonomer. Said
comonomers can be selected from the group consisting of ethylene and C4-C10
alpha-olefins, such as 1-butene, 1-pentene, 1-hexene, 1-octene. The
copolymers can be random copolymers or heterophasic copolymers.
The metallocene random copolymers of the present invention comprise at least
0.1 wt% of comonomer(s), preferably at least 0.2 wt%, more preferably at least
0.5 wt%, even more preferably at least 1 wt%, most preferably at least 2 wt%.
They comprise up to 10 wt% of comonomer(s), preferably up to 8 wt%, and most
preferably up to 6 wt.%. Preferably, the metallocene random copolymers are
copolymers of propylene and ethylene.
The metallocene heterophasic copolymers of the present invention comprise a
matrix, which in turn is made of a metallocene propylene homopolymer or
random copolymer as defined above, and a rubber phase. Preferably, the
metallocene heterophasic copolymers are copolymers of propylene and
ethylene. They have an ethylene content in the range from 4 wt% to 15 wt%.
The metallocene heterophasic copolymers comprise from 5 wt% to 35 wt% of
rubber phase. Preferably, the rubber phase is an ethylene propylene rubber
(EPR).
Metallocene propylene homopolymers are the most preferred metallocene
polypropylenes used in the present invention.
The polymerization of propylene and one or more optional comonomers is
performed in the presence of one or more metallocene-based catalytic systems
comprising one or more metallocenes, a support and an activating agent. Such
metallocene-based catalytic systems are known to the person skilled in the art
and need not be explained in detail.
The metallocene component used to prepare the metallocene polypropylene can
be any bridged metallocene known in the art. Preferably it is a metallocene
represented by the following general formula.

wherein
the bridge R1 is -(CR10R11)P- or -(SiR10R11)p- with p = 1 or 2, preferably it is -
(SiR10R11)-;
M is a metal selected from Ti, Zr and Hf, preferably it is Zr;
X1 and X2 are independently selected from the group consisting of halogen,
hydrogen, C1-C10 alkyl, C6-C15 aryl, alkylaryl with C1-C10 alkyl and C6-C15 aryl;
R2, R3, R4, R5, R6, R7, R8, R9, R10 and R11 are each independently selected from
the group consisting of hydrogen, C1-C10 alkyl, C5-C7 cycloalkyl, C6-C15 aryl,
alkylaryl with C1-C10 alkyl and C6-C15 aryl, or any two neighboring R may form a
cyclic saturated or non-saturated C4-C10 ring; each R2, R3, R4, R5, R6, R7, R8, R9,
R10 and R11 may in turn be substituted in the same way.
The preferred metallocene components are represented by the general formula
(I), wherein
the bridge R1 is SiR10R11;
M is Zr;
X1 and X2 are independently selected from the group consisting of halogen,
hydrogen, and C1-C10 alkyl; and
(C5R2R3R4R5) and (C5R6R7R8R9) are indenyl of the general formula
C9R12R13R14R15R16R17R18R19, whereinR12, R13, R14, R15, R16, R17, R18 and R19
are each independently selected from the group consisting of hydrogen, C1-C10
alkyl, C5-C7 cycloalkyl, C6-C15 aryl, and alkylaryl with C1-C10 alkyl and C6-C15
aryl, or any two neighboring R may form a cyclic saturated or non-saturated C4-
C10 ring;
R10 and R11 are each independently selected from the group consisting of C1-C10
alkyl, C5-C7 cycloalkyl, and C6-C15 aryl, or R10 and R11 may form a cyclic
saturated or non-saturated C4-C10 ring; and
each R10, R11, R12, R13, R14, R15, R16, R17, R18 and R19 may in turn be substituted
in the same way.
The polypropylenes produced with the preferred metallocene compounds have
surprisingly been identified as having a very low content of volatile organic
compounds (VOC).
Particularly suitable metallocenes are those having C2-symmetry.
Examples of particularly suitable metallocenes are:
dimethylsilanediyl-bis(cyclopentadienyl)zirconium dichloride,
dimethylsilanediyl-bis(2-methyl-cyclopentadienyl)zirconium dichloride,
dimethylsilanediyl-bis(3-methyl-cyclopentadienyl)zirconium dichloride,
dimethylsilanediyl-bis(3-tert-butyl-cyclopentadienyl)zirconium dichloride,
dimethylsilanediyl-bis(3-tert-butyl-5-methyl-cyclopentadienyl)zirconium
dichloride,
dimethylsilanediyl-bis(2,4-dimethyl-cyclopentadienyl)zirconium dichloride,
dimethylsilanediyl-bis(indenyl)zirconium dichloride,
dimethylsilanediyl-bis(2-methyl-indenyl)zirconium dichloride,
dimethylsilanediyl-bis(3-methyl-indenyl)zirconium dichloride,
dimethyisiianediyi-bis(3-tert-butyi-indenyi)zirconium dichloride,
dimethylsilanediyl-bis(4,7-dimethyl-indenyl)zirconium dichloride,
dimethylsilanediyl-bis(tetrahydroindenyl)zirconium dichloride,
dimethylsilanediyl-bis(benzindenyl)zirconium dichloride,
dimethylsilanediyl-bis(3,3'-2-methyl-benzindenyl)zirconium dichloride,
dimethylsilanediyl-bis(4-phenyl-indenyl)zirconium dichloride,
ethylene-bis(indenyl)zirconium dichloride,
ethylene-bis(tetrahydroindenyl)zirconium dichloride,
isopropylidene-(3-tert-butyl-5-methyl-cyclopentadienyl)(fluorenyl) zirconium
dichloride.
The polymerization of propylene and one or more optional comonomers in
presence of a metallocene-based catalytic system can be carried out according
to known techniques in one or more polymerization reactors. The metallocene
polypropylenes of the present invention are preferably produced by
polymerization in liquid propylene at temperatures in the range from 20°C to
100°C. Preferably, temperatures are in the range from 60°C to 80°C. The
pressure can be atmospheric or higher. It is preferably between 25 and 50 bar.
The molecular weight of the polymer chains, and in consequence the melt flow
of the metallocene polypropylene, is regulated by the addition of hydrogen to the
polymerization medium.
The metallocene polypropylenes of the present invention are characterized by a
melt flow index in the range from 1 to 100 dg/min (as measured according to
ISO 1133, condition L, at 230°C under 2.16 kg). Preferably, the melt flow index
is at least 5 dg/min, and more preferably it is at least 10 dg/min. Preferably, the
melt flow index is at most 80 dg/min, more preferably at most 60 dg/min, even
more preferably at most 50 dg/min, and most preferably at most 40 dg/min.
The metallocene propylene homopolymers used in the present invention are
characterized by a melting temperature in the range from 135°C to 165°C,
preferably in the range from 140°C to 160°C, and most preferably in the range
from 145X to 155°C. The determination of melting temperatures is well known
to the person skilied in the art. Generally, in order to erase the thermal history of
the samples they are first heated to a temperature above the melting
temperature, e.g. to 200°C, and kept there for a time, e.g. for 3 minutes. After
cooling the sample are then reheated for the measurement of the melting
temperature.
The metallocene propylene homopolymers used in the present invention are
characterized by a xylene solubles content of less than 3 wt%, preferably of less
than 2.5 wt%, and most preferably of less than 2 wt%. The xylene solubles
content is determined by dissolving the polypropylene in refluxing xylene,
cooling of the solution to 25°C, filtering the solution, and subsequent evaporation
of the solvent. The residue, which is the xylene soluble portion of the
polypropylene, is then dried and weighed.
The metallocene polypropylenes used in the present invention are characterized
by a high isotacticity, for which the content of mmmm pentads is a measure. The
content of mmmm pentads is at least 95 %, preferably at least 97 %. The
isotacticity is determined by NMR analysis according to the method described by
G.J. Ray et al. in Macromolecules, vol. 10, n° 4, 1977, p. 773-778. It is
performed on the dried product resulting from the extraction by boiling hexane of
the xylene insoluble fraction.
Whilst not wishing to be bound by theory it is believed that the degradation of
polypropylene and in consequence the formation of volatile organic compounds
is partly due to metallic residues from the polymerization catalyst. It is therefore
desirable to have a low content of metallic residues in the polypropylene. The
metallocene polypropylene used in the present invention is therefore
characterized by a zirconium content in the range from 0.01 ppm to 5 ppm. The
zirconium content is preferably at least 0.1 ppm. The zirconium content is
preferably 4 ppm or less, more preferably 3 ppm or less, even more preferably 2
ppm or less and most preferably 1 ppm or less. The zirconium content can be
measured by an inductively coupled plasma technique with atomic emission
spectroscopy.
The elastomer, also referred to as "rubber", used in the present invention can be
any elastomer known in the art. The elastomer can for example be selected from
the group consisting of natural rubber, butadiene elastomer, isoprene elastomer,
chloroprene elastomer, hydrogenated styrene-butadiene elastomer, styrene-
ethylene/butene-styrene block copolymer, hydrogenated styrene-isoprene
elastomer, hydrogenated styrene-ethylene/isoprene-styrene block copolymer,
acrylic rubber, butyl elastomer, ethylene-propylene elastomer, ethylene-octene
elastomer, ethylene-butylene elastomer, styrene-butadiene-styrene elastomer,
butylene-propylene elastomer, pentene-propylene elastomer, hexene-propylene
elastomer, octene-propylene elastomer, ethylene-propylene-ethylidene
norbomene elastomer, ethylene-propylene-vinyl norbornene elastomer,
ethylene-propylene-unconjugated diene elastomer, hydrogenated ethylene-
butadiene elastomer, styrene butadiene styrene, and mixtures thereof. The
preferred elastomers are ethylene-propylene elastomers, ethylene-octene
elastomers, ethylene-butylene elastomers, styrene-butadiene-styrene
elastomers and mixtures thereof.
According to another embodiment of the present invention, the blend comprises
from 0 wt% to 50 wt% of a mineral filler, said mineral filler being preferably
selected from the group consisting of talc, wollastonite, mica, glass fibers,
calcium carbonate and mixtures thereof. The preferred amount of mineral filler
is in the range from 5 wt% to 40 wt% of the blend, and more preferably in the
range from 10 wt% to 30 wt%. Surprisingly, it has been found that the narrower
molecular weight distribution of a metallocene polypropylene as compared to a
Ziegler-Natta polypropylene does not negatively influence the distribution of the
mineral filler in the blend.
According to yet another embodiment of the present invention, said blend
comprises from 0 wt% to 79.9 wt% of a propylene polymer selected from the
group consisting of Ziegler-Natta catalyzed propylene homopolymers and
copolymers and mixtures thereof, that is, propylene polymers polymerized in the
presence of a non-metallocene-based catalyst.
The blend according to the present invention may also comprise from 0 wt% to
10 wt%, preferably' from 0.1 wt% to 5 wt% of additives such as, by way of
example, antioxidants, light stabilizers, acid scavengers, lubricants, antistatic
additives, nucleating/clarifying agents, colorants, as long as the addition of the
additive does not obstruct the above-mentioned objects of the present invention.
An overview of such additives may be found in Plastics Additives Handbook, ed.
H. Zweifel, 5th edition, 2001, Hanser Publishers.
The blend is prepared in any known manner, such as by mechanical blending in
an extruder. According to one embodiment, the metallocene polypropylene, the
elastomer, the optional mineral filler, the optional Ziegler-Natta polypropylene
and the optional additives are introduced into the extruder in the form of a
powder or of pellets. The optional mineral filler is preferably introduced in the
middle of the extruder. In a preferred embodiment, the extruder is equipped with
a vacuum pump on an extruder vent that allows removal of volatile organic
compounds (VOC) from the blend.
It has been surprisingly noted that even though a vacuum pump was used to
remove volatile organic compounds (VOC) during extrusion of a blend
comprising Ziegler-Natta polypropylene the residual content of volatile organic
compounds (VOC) was drastically reduced when said Ziegler-Natta
polypropylene was substituted by metallocene polypropylene. In fact, the
reduction in volatile organic compounds (VOC) was surprisingly high in view of
the percentage of polypropylene in the blend.
The mechanical properties of the blends of the present invention comprising
metallocene polypropylene resemble those of the respective blends wherein the
metallocene polypropylene is substituted by a Ziegler-Natta polypropylene. In a
preferred aspect the flexural modulus of a blend comprising the metallocene
polypropylene is at least 70 %, preferably at least 80 % and most preferably at
least 90 % of the flexural modulus of the respective blend, wherein the
metallocene polypropylene is substituted by a Ziegler-Natta polypropylene. In
another preferred aspect the impact strength of the blend comprising the
metallocene polypropylene is at least 70 % and preferably at least 80 % of the
impact strength of the respective blend, wherein the metallocene polypropylene
is substituted by a Ziegler-Natta polypropylene.
The present invention also relates to the use of a blend according to the present
invention for manufacturing automobile parts. In particular, it relates to the use of
a blend according to the present invention for producing automobile parts having
less than 45 ppm of volatile organic compounds (determined in accordance with
VDA-278).
The details and embodiments described above in connection with the blend
also apply to the use according to the present invention.
The automobile parts of the invention are preferably produced by molding the
propylene-based resin composition in any conventional injection molding
method such as injection molding, extrusion, compressed injection molding and
vapor-blowing injection molding. The preferred method is injection molding.
The blends of the present invention can be used to produce automobile parts
such as interior parts like door panels, instrument panels, consoles, A,B,C pillar
trims, seat protectors, air ducts, door lists, door trims, air-bag containers and
others. The automobile parts also include exterior parts like body panels,
bumpers, rocker panels, door lists, side sills, cowl covers and others.
Examples
The invention is illustrated with the following examples.
BLEND COMPONENTS
mPP Metallocene propylene homopolymer with a melt flow index of 25
dg/min (ISO 1133, 230°C, 2.16 kg). It is characterized by a flexural
modulus of 1300 MPa (ISO 178) and a melting point of 151°C (ISO
3146).
Elast Ethylene-butene copolymer with a melt index of 5 dg/min (ASTM D
1238), a density of 0.865 g/cm3 (ASTM D 792) and a Mooney
viscosity ML1+4 at 121°C of 7 (ASTM D 1646). It is characterized by a
Shore A hardness of 64 (ASTM D 2240) and a flexural modulus (1 %
secant) of 7.8 MPa (ASTM D 790). Commercially available from Dow
Chemical Company as Engage ENR 7447.00.
Talc Talc with a particle size distribution of 97 % for under 10 µm, 82 % for
under 5 µm and 45 % for under 2 µm. It is characterized by an oil
absorption of 50 g / 100 g. Such a talc is for example commercially
available from Mondo Minerals OY as Finntalc M05.
ZNPP-1 Heterophasic propylene copolymer comprising about 12 wt% of
ethylene-propylene rubber with a melt flow index of 25 dg/min (ISO
1133, 230°C, 2.16 kg). It is characterized by a flexural modulus of
1300 MPa (ISO 178), an Izod impact strength of 7 kJ/m2 at 23°C and
5 kJ/m2 at -20°C (ISO 180), a Charpy impact strength (notched) of 8
kJ/m2 at 23°C and 5.5 kJ/m2 at -20°C (ISO 179) and a melting point
of 165°C (ISO 3146).
ZNPP-2 Nucleated antistatic heterophasic propylene copolymer comprising
about 12 wt% of ethylene-propylene rubber with a melt flow index of
44 dg/min (ISO 1133, 230°C, 2.16 kg). It is characterized by a flexural
modulus of 1500 MPa (ISO 178), an Izod impact strength of 7.5 kJ/m2
at 23°C and 4 kJ/m2 at -20°C (ISO 180), a Charpy impact strength
(notched) of 7 kJ/m2 at 23°C and 4.5 kJ/m2 at -20°C (ISO 179) and a
meiting point of 165°C (ISO 3146).
B225 Irganox B225 is a 1 : 1 blend by weight of Irganox 1010 and Irgafos
168. It is commercially available from Ciba Specialty Chemicals.
PEB3089 Black color masterbatch with 40 wt% of carbon black, having a
carbon black particle size between 20 nm and 25 nm in a LDPE
carrier, supplied by Hubron Manufacturing Division Ltd.
BLENDS
These blend components were used to prepare blends according to the present
invention and also comparative blends outside of the scope of the present
invention. Blend compositions are shown in table 1 with the amounts given in
wt% of the total blend. The blends were compounded on a Leistritz Micro27
GL36D extruder and the test samples needed for performing mechanical and
other testing were injection molded on an Engel ES 500 / 125 HL injection
molding machine.

TEST METHODS
The melt flow index was measured according to norm ISO 1133, condition L,
using a weight of 2.16 kg and a temperature of 230 °C.
The coefficient of linear thermal expansion (CLTE) was determined according to
ASTM D696..
Flexural modulus was measured according to ISO 178. Tensile modulus was
measured according to ISO 527. The same measurement gave values for stress
at yield, strain at yield and elongation at break.
Cut-notched Izod impact strength was measured according to ISO 180-1A at 23
°C. Cut-notched Charpy impact strength was measured according to ISO 179-
1eA at 23°C and -20°C.
Furthermore, two tests were performed in order to measure the total desorption
as well as the amount of volatile organic compounds (VOC) and the fogging
(FOG), according to the German automobile standard VDA-278. In this latter
test, in order to measure the amount of VOC, the material is heated to 90 °C and
maintained at this temperature for 30 minutes. The vapors are then condensed
at -150 °C, and the composition of the condensate is determined by gas
chromatography. After the VOC has been measured, the sample is further
heated up to 120 °C and maintained in this temperature for 60 minutes, in order
to measure the FOG. The vapors are then condensed and the content of the
condensate is determined in the same manner as for VOC.
RESULTS
Results of the analyses for the example blends and the comparative example
blends are given in table 2 for mechanical properties. Results of the test
according to VD1-278 are shown in table 3.
The results in table 2 show that similar mechanical properties are obtained when
replacing the Ziegler-Natta catalyzed polypropylenes partially or totally with
metallocene catalyzed polypropylenes.
In summary the results show that the use of metallocene polypropylenes in
blends for automotive applications leads to a drastic reduction in the emission of
volatile organic compounds. Surprisingly, the use of metallocene polypropylene
in blends for automotive applications does not lead to a loss in mechanical
properties as compared to the respective blends with Ziegler-Natta
polypropylenes.
Claims
1. Automobile part comprising a blend, said blend comprising
(a) 99.1 - 20 wt% of a polypropylene produced in the presence of a
metallocene-based catalyst, and
(b) 0.1 - 50 w% of an elastomer,
said blend having less than 45 ppm of volatile organic compounds
(determined in accordance with VDA-278).
2. Automobile part according to claim 1, wherein the polypropylene has a melt
flow index in the range from 1 dg/min to 100 dg/min (measured according
to ISO 1133, condition L, 230°C, 2.16 kg).
3. Automobile part according to any of the preceding claims, wherein the
polypropylene has a melting temperature in the range from 135°C to
165°C.
4. Automobile part according to any of the preceding claims, wherein the
polypropylene is a homopolymer.
5. Automobile part according to any of the preceding claims, wherein the
polypropylene has a xylene solubles content of less than 3 wt%.
6. Automobile part blend according to any of the preceding claims, wherein
the polypropylene has a content of mmmm pentads of at least 95 %.
7. Automobile part according to any of the preceding claims, wherein the
isotactic polypropylene produced in the presence of a metallocene-based
catalyst has a zirconium content in the range from 0.01 ppm to 5 ppm.
8. Automobile part according to any of the preceding claims, characterized in
that said blend comprises from 0 wt% to 50 wt% of a mineral filler.
9. Automobile part according to any of the preceding claims, wherein said
blend comprises from 0 wt% to 79.9 wt% of a propylene polymer selected
from the group consisting of Ziegler-Natta catalyzed propylene
homopolymers and copolymers and mixtures thereof.
10. Automobile part according to any of the preceding claims, wherein the
flexural modulus is at least 70 % of the flexural modulus of the respective
blend wherein the metallocene polypropylene is substituted by a Ziegler-
Natta polypropylene.
11. Automobile part according to any of the preceding claims, wherein the
impact strength is at least 70 % of the impact strength of the respective
blend wherein the metallocene polypropylene is substituted by a Ziegler-
Natta polypropylene.
12. Automobile parts according to any of the preceding claims, wherein the
automobile parts are interior automobile parts.
13. Use of a blend comprising
(a) 99.1 - 20 wt% of a polypropylene produced in the presence of a
metallocene-based catalyst, and
(b) 0.1 - 50 w% of an elastomer,
for producing automobile parts having less than 45 ppm of volatile organic
compounds (determined in accordance with VDA-278).


The present invention relates to a blend comprising metallocene polypropylene and an elastomer for automobile
parts, characterized in that said blend has low volatile organic compounds emissions. The invention also relates to the use of said
blend in parts for automobiles.

Documents:

3759-KOLNP-2009-(06-02-2014)-CLAIMS.pdf

3759-KOLNP-2009-(06-02-2014)-EXAMINATION REPORT REPLY RECIEVED.pdf

3759-KOLNP-2009-(06-02-2014)-FORM-3.pdf

3759-KOLNP-2009-(06-02-2014)-OTHERS.pdf

3759-KOLNP-2009-(29-07-2013)-ANNEXURE TO FORM 3.pdf

3759-KOLNP-2009-(29-07-2013)-CORRESPONDENCE.pdf

3759-KOLNP-2009-(29-07-2013)-OTHERS.pdf

3759-KOLNP-2009-(29-07-2013)-PA.pdf

3759-kolnp-2009-abstract.pdf

3759-KOLNP-2009-ASSIGNMENT.pdf

3759-kolnp-2009-claims.pdf

3759-KOLNP-2009-CORRESPONDENCE 1.1.pdf

3759-kolnp-2009-correspondence.pdf

3759-kolnp-2009-description (complete).pdf

3759-kolnp-2009-form 1.pdf

3759-KOLNP-2009-FORM 18.pdf

3759-kolnp-2009-form 3.pdf

3759-kolnp-2009-form 5.pdf

3759-kolnp-2009-gpa.pdf

3759-kolnp-2009-international publication.pdf

3759-kolnp-2009-pct priority document notification.pdf

3759-kolnp-2009-pct request form.pdf

3759-kolnp-2009-specification.pdf


Patent Number 260005
Indian Patent Application Number 3759/KOLNP/2009
PG Journal Number 14/2014
Publication Date 04-Apr-2014
Grant Date 31-Mar-2014
Date of Filing 29-Oct-2009
Name of Patentee TOTAL PETROCHEMICALS RESEARCH FELUY
Applicant Address ZONE INDUSTRIELLE C, B-7181 SENEFFE (FELUY) BELGIUM
Inventors:
# Inventor's Name Inventor's Address
1 KOSCHER, EMMANUELLE RUE WAYEZ, 16, B-1420 BRAINE L'ALLEUD BELGIUM
2 TER, WOORT, CHRISTIAN BURG TAYMANSLAAN 31, B-3090 OVERIJSE BELGIUM
3 VANDOORNE, FILIP OUDE SLAGMANSTRAAT 10, B-9080 LOCHRISTI BELGIUM
PCT International Classification Number C08L 23/08
PCT International Application Number PCT/EP2008/055315
PCT International Filing date 2008-04-30
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 07107551.9 2007-05-04 EUROPEAN UNION