Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/16—Making expandable particles
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
  • C08K5/005—Stabilisers against oxidation, heat, light, ozone
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
  • C08F110/04—Monomers containing three or four carbon atoms
  • C08F110/06—Propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
  • C08F210/04—Monomers containing three or four carbon atoms
  • C08F210/06—Propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2203/00—Foams characterized by the expanding agent
  • C08J2203/12—Organic compounds only containing carbon, hydrogen and oxygen atoms, e.g. ketone or alcohol
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/10—Homopolymers or copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/04—Oxygen-containing compounds
  • C08K5/13—Phenols; Phenolates
  • C08K5/134—Phenols containing ester groups
  • C08K5/1345—Carboxylic esters of phenolcarboxylic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/16—Nitrogen-containing compounds
  • C08K5/20—Carboxylic acid amides
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/49—Phosphorus-containing compounds
  • C08K5/51—Phosphorus bound to oxygen
  • C08K5/52—Phosphorus bound to oxygen only
  • C08K5/524—Esters of phosphorous acids, e.g. of H3PO3
  • C08K5/526—Esters of phosphorous acids, e.g. of H3PO3 with hydroxyaryl compounds
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S521/00—Synthetic resins or natural rubbers -- part of the class 520 series
  • Y10S521/909—Blowing-agent moderator, e.g. kickers

Definitions

• the present invention relates to a composition based on propylene polymer, which can be converted into expanded granules and particularly to a composition having an improved resistance to fogging. It also relates to a process for obtaining such composition as well as to its use for the manufacture 5 of expanded granules. Finally it relates to cellular articles fashioned from said expanded granules.
• JP-A-06-234898 suggests the use of blends of grafted polyolef ⁇ n with polyamide and specific inorganic fibers such as glass fiber.
• these blends being different from the conventional propylene polymers used in the other parts of the vehicle, are not easily recycled.
• EP-A-0905175 or JP-A-11- 263863 proposes the addition of fogging inhibitors such as aluminium sulfate or
• the aim of the present invention is to provide a polypropylene based composition having an improved fogging resistance and which can be used for the preparation of expanded granules.
• the present invention therefore relates to a composition for expanded granules based on semi-crystalline propylene polymer comprising, per 100 parts by weight, less than 0.025 part by weight of volatile compounds.
• the content of volatile compounds contained in a composition is determined as follows :
• composition under to form of particle of mean dimensions of from 1 to 2 mm are disposed in a vessel as a strip of 80 to 70 mm under at 120°C during one hour.
• a helium stream passes on the strip with a flow rate of 15 ml/min before being cooled at -196°C to trap the desorbed compounds.
• the content of volatile compounds is the quantity of compounds trapped having an elution time of at most 40 min determined by gas phase chromatography by means of a semi capillary column equipped with a FID detector (column CP-Sil 24 CB, diameter : 0.53 mm, length : 15 m, helium flow : 10 ml/min, temperature : 120 °C during the 2 first minutes, then increase at 8 °C/min till 265 °C).
• the volatile compounds contribute to the fogging because of their relatively high volatility. Accordingly their content should be maintained as low as possible. For economic reasons, however, it is generally higher than 0.0005, particularly higher than 0.001 part by weight per 100 parts by weight of composition. Contents of at most 0.02 part by weight gives advantageous results. Contents of at most 0.01 part by weight are particularly preferred.
• volatile compounds are mainly formed by volatile hydrocarbon compounds contained in the propylene polymer and, eventually, by the polymer additive(s) and/or by the degradation products thereof.
• the volatile hydrocarbon compounds are generally oligomers of propylene formed during the polymerization reaction. They usually contain from 9 to 39 carbon atoms.
• Additives who contribute to the volatile compounds by themselves or through their degradation product(s) are for instance sterically hindered phenol having a molecular weight lower than 500 daltons (phenol (a)) or organic phosphite of formula P(OR)3 wherein each R represents, independently from each other, alkyl radicals or non sterically hindered aryl radicals (phosphite (a)).
• phenol (a) examples include 2,4-dimethyl,6-tert-butylphenol, 2,6- ditertbutyl para cresol, and octyl beta- (3,5-ditertbutyl-4-hydroxyphenyl) - propionate.
• phosphites (a) are tris(para-nonylphenyl)phosphite and distearylpentaerythrityldiphosphite.
• compositions according to the invention containing, per 100 parts by weight, less than 0.05 part by weight of the sterically hindered phenol (a) and less than 0.05 part by weight of the organic phosphite (a) are particularly preferred.
• compositions according to the invention free of phenol (a) and of phosphite (a) give good anti-fogging properties.
• the propylene polymers used in the composition according to the invention are semi-crystalline polymers in the sense of the meaning given in
• the propylene polymers used in the present invention are generally chosen from the propylene homopolymers and the copolymers of this latter containing at most 50 weight % of at least one comonomer chosen from ethylene and ⁇ -olefins containing from 4 to 8 carbon atoms and their mixtures.
• the copolymers of propylene are preferably chosen from copolymers of propylene with up to 20 mol % ethylene and/or 1-butene.
• Copolymers of propylene containing from 1 to 6 mol % of ethylene are particularly preferred because they provide a good compromise between expansion and molding behavior and rigidity.
• the comonomer contents mentioned in the present description are determined by Fourier transform IR spectroscopy on the polymer converted into a 200 ⁇ m pressed film. It is the absorption bands at 732 and 720 cm"l that are used to determine the ethylene content and the absorption band at 767 to determine the 1-butene content.
• the propylene polymer used in the composition according to the invention has generally a melt flow index (MFI), measured according to ASTM D 1238 (1986) under a load of 2.16 kg at 230 °C in the range from 0.3 to 30 g/10 min. This value is more preferably at least 1 g/10 min. Values of at most 20 g/10 min give satisfactory results.
• MFI melt flow index
• compositions according to the invention contain usually additives to improve their stability.
• additives generally used for propylene polymers it has been found that, some of them are better in terms of fogging resistance.
• the content of phenol (b) is usually of at least 0.05 part per 100 parts of the composition. Contents of at least 0.1 part give the best results. Compositions containing at most 0.4 part of phenol (b) are very suitable.
• the phenols (b) having a molecular weight of at least 700 daltons are preferred because of they lead to polymers having better compromise stability / fogging resistance.
• phenols (b) examples include the pentaerythrityl tetrakis(3,5- ditertbutyl-4-hydroxyphenyl) propionate and the bis(beta-3,5-ditertbutyl-4- hydroxyphenyl-ethyl)suberate.
• compositions containing, per 100 parts by weight, at least 0.02 part per 100 parts of phosphite (b) are preferred.
• Compositions containing at least 0.04 part of phosphite (b) have a good compromise of properties.
• the content of phosphite (b) is furthermore usually of at most 0.2, preferably of at most 0.1 part by weight.
• the tris(2,4-ditertbutylphenyl)phosphite is particularly suitable.
• the amounts of phenol (b) and of phosphite (b) are such that their weight ratio is in the range of 2 to 10.
• compositions according to the invention may comprise, as occasion demands, known other conventional additives such as stabilizers, pigments, colorants, fillers, fire retardants, antistatic agents, antiacid agents, lubricants, slip-promoting agents, etc.
• additives are added in amounts such that the above mentioned conditions are satisfied.
• Antiacid agents and lubricants are specially preferred. Their contents are usually of from 0.05 to 0.2 part by weight per 100 parts of the composition.
• Other preferred additives are the thiosynergists such as the 3,3'-thio-bis propanoic acid or the dilauryl thiodipropionate. These additives are usually used in quantities of 0.001 to 0.5 part per 100 parts of the composition.
• composition according to the invention contains by way of polymers only the propylene polymer(s) defined hereabove.
• Composition in which the propylene polymer(s) is (are) neither grafted nor cross-linked is usually preferred due to a better compromise of properties.
• composition according to the invention may be obtained by any known process.
• a propylene polymer is obtained by using polymerization conditions such that it incorporates few volatile hydrocarbon compounds is used.
• Example of such conditions is the polymerization of the propylene and of the optional comonomer(s) in a hydrocarbon diluent chosen from liquid alcanes and cycloalcanes wherein the molar fraction of propylene is at most 0.9.
• the diluent is usually hexane or heptane.
• the temperature and pressure are those generally used by the man skilled in the art. Temperature between 50 and 90°C and pressures between 10 and 30 atmospheres are particularly suitable.
• the catalytic system may be any catalytic system known to be sufficiently productive and stereospecific permitting the propylene to be polymerized in isotactic form and capable of incorporating the desired comonomer(s).
• the propylene polymer issued from said polymerization reaction is then separated from the polymerization medium by any known techniques such as filtration or centrifugation and usually dried to eliminate the polymerization diluent. It is particularly advantageous that the polymer is dried until the content of polymerization diluent is less than 0.1, specifically less than 0.01 weight %.
• the drying is carried out at a temperature of from 70 to 110°C. The duration of the drying depends on the temperature. Its is usually from 0.1 to 2 h, preferably from 0.25 to 1 h.
• the dried propylene polymer is then usually melt blended with the additives mentioned hereabove.
• the melt blending is carried out by any known techniques. It may be for example first carried out at ambient temperature followed by a second mixing at a temperature above the melting point of the propylene polymer, for example in a mechanical mixer or in an extruder.
• the temperature of the second stage is generally from 100 to 300°C, in particular from 120 to 210°C.
• An alternative method consists in introducing the additives into the polymer that is already molten. It is preferred to proceed according to the first technique.
• a propylene polymer issued from the polymerization reaction and containing preferably, per 100 parts by weight, more than 0.025 part by weight of volatile compounds is brought into contact with an aliphatic or cycloaliphatic hydrocarbon diluent containing from 4 to 7 carbon atoms at a temperature in the range of 5 to 60°C for a period of 0.1 to 4 h in an amount of from 0.1 to 5 g of polymer per g of hydrocarbon diluent, and separated from said diluent.
• the contact of the propylene polymer and the hydrocarbon diluent is generally carried out at a pressure of 10 ⁇ to 3 10 ⁇ Pa.
• the temperature is preferably in the range of 10 to 60°C, temperatures of 15 to 40°C giving the best results.
• the relative amounts of the propylene polymer to the hydrocarbon diluent are often of from 0.2 to 1, ratio of from 0.25 to 0.75 giving the best results at reasonable costs.
• the duration of said treatment is advantageously from 0.2 to 2 h; duration of from 0.3 to 1 h giving the best compromise.
• the propylene polymer issued from said treatment is then usually separated from the hydrocarbon diluent by any known process such as filtration or centrifugation. The filtration is preferably chosen for economic reasons.
• the propylene polymer thus obtained is then preferably dried by any known process.
• the drying is carried out at a temperature of from 70 to 120 °C.
• the duration of the drying depends on the temperature. Its is usually from 0.1 to 2 h, preferably from 0.25 to 1.5 h.
• the treated propylene polymer is then advantageously mixed with the above mentioned additives.
• the mixing conditions (concentrations, temperature ...) are usually those described hereabove with respect to the propylene polymer issued from the polymerization.
• a propylene polymer issued from the polymerization reaction and containing preferably, per 100 parts by weight, more than 0.025 part by weight of volatile compounds is first melt mixed with the additive(s) described hereabove to obtain granules which are contacted with a gas stream which may be a stream of hot air, a gas stream containing steam or a stream of steam at a temperature of from 60 to 160 °C for a duration of from 30 minutes to 100 hours. Treatment of the propylene polymer with gas stream containing steam gives good results.
• the gas stream is generally composed of a gas such as nitrogen or air being preferred.
• the temperature of this process is generally at least 70°C and more precisely at least 80 °C, values of at least 90 °C being the most common.
• the temperature is furthermore preferably of at most 120°C. Good results are obtained when the temperature is of approximately 100°C.
• the duration of said treatment usually do not exceed 80 hours and more particularly 60 hours.
• the total amount of steam is generally of at least 0.01 kg, preferably at least 0.05 kg and more particularly at least 0.1 kg per kg of propylene polymer. In general, this amount is less than or equal to 20 kg, most often less than or equal to 10 kg and more particularly less than or equal to 5 kg of steam per kg of polymer.
• a propylene polymer issued from the polymerization reaction and containing, per 100 parts by weight, more than 0.025 part by weight of volatile compounds treated with the hydrocarbon diluent, mixed with the additive and treated with the gas stream gives composition having particularly good fogging resistance.
• compositions wherein the propylene polymer is obtained by using polymerization conditions wherein the content of volatile hydrocarbon compounds is low and mixed with the additives and treated with the gas stream are advantageously used.
• the treatment of the polymer may be carried out continuously or batchwise.
• the device(s) used for the polymer treatments may be any receptacle into which the polymer issued from the polymerization, the hydrocarbon diluent or the gas stream are introduced.
• the melt blending of the propylene polymer and the additives is carried out in any device known for that purpose giving sufficiently high shear rate to induce the melting of the propylene polymer. It is thus possible to work with external and internal mixers. Internal mixers are the most appropriate and amongst them extruders are the most preferred.
• the additives used in the above described process are usually of, per 100 part by weight of the propylene polymer, at least from 0.03 to 0.5 part by weight of the phenol (b), and up to 0.3 part by weight of the phosphite (b).
• the preferred quantities of these additives and the quantity of the other additives that may be used are in accordance with that described hereabove with respect of the composition according to the invention.
• compositions of the invention are particularly suitable for the manufacture of expanded granules and for the subsequent manufacture, starting from these latters, of cellular articles. Due to their improved resistance to fogging, the composition of the present invention may be successfully used in the automotive industry and particularly as interior trim such as dashboard, sunvisor, headrest, interior material of the ceiling, or of the doors. It should be furthermore noted that the improvement of the fogging resistance is obtained without loss and even without modifications in the mechanical and chemical properties of the propylene polymer.
• Example 1 (given by way of comparison) A random propylene copolymer containing 2.3 weight % of ethylene and having a MFI of 9.8 g/10 min and a melting temperature of 145.2 is melt blended with 2 g/kg of pentaerythrityltetrakis(3,5- ditertbutylparacresol)propionate (IRGANOX® 1010), 0.3 g/kg of 2,6-ditertbut- 4-methylphenol, 1 g/kg of bis(2,4-ditertbutylphenyl)pentaerythritol diphosphite (ULTRANOX® 626), 0.6 g/kg or erucic acid amide (CRODAMINE ER) and 1 g/kg of calcium stearate has been pelletized on a ZSK 40 extruder at a temperature of 210 °C to obtain a composition containing, per 100 parts by weight, 0.075 part by weight of volatile compounds. Processed in expanded
• Example 1 is reproduced but by melting the random propylene copolymer with 2 g/kg of the LRGANOX 1010 product, 0.5 g/kg of tris(2,4- ditertbutylphenyl) posphite) (IRGAFOS® 168), 2 g/kg of distearylthiodipropionate, 0.6 g/kg of erucic acid amide and 1 g/kg of hydrotalcite to obtain a composition containing, per 100 parts, 0.055 part by weight of volatile compounds.
• Example 3 (according to the invention)
• Example 2 is reproduced after having contacted the composition with a stream of steam at 100 °C during 15 h (0.5 kg of steam per kg of composition).
• the volatile compounds content of the obtained composition is, per 100 parts, of 0.019 part by weight. Used as interior material for automobile, said composition generates dramatically less fogging than that of Examples 1 and 2.
• Example 4 (according to the invention)
• Example 2 is reproduced after having contacted the random copolymer with hexane at 30 °C during 1 h (0.5 kg of composition per kg of hexane).
• the volatile compounds content of the obtained composition is, per 100 parts, of 0.009 part by weight.

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• Chemical & Material Sciences (AREA)
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• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
• Compositions Of Macromolecular Compounds (AREA)

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• 2001
  • 2001-06-20 WO PCT/EP2001/007017 patent/WO2003000752A1/en not_active Ceased
• 2002
  • 2002-06-17 DE DE60202001T patent/DE60202001T2/de not_active Revoked
  • 2002-06-17 AT AT02747395T patent/ATE282646T1/de not_active IP Right Cessation
  • 2002-06-17 JP JP2003507155A patent/JP2004534125A/ja active Pending
  • 2002-06-17 US US10/481,555 patent/US6914085B2/en not_active Expired - Lifetime
  • 2002-06-17 WO PCT/EP2002/006635 patent/WO2003000753A1/en not_active Ceased
  • 2002-06-17 ES ES02747395T patent/ES2231715T3/es not_active Expired - Lifetime
  • 2002-06-17 CN CNB028123697A patent/CN1247626C/zh not_active Expired - Fee Related

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