WO2002052059A1 - Flame retardant polypropylene resin composition - Google Patents

Flame retardant polypropylene resin composition Download PDF

Info

Publication number
WO2002052059A1
WO2002052059A1 PCT/KR2000/001523 KR0001523W WO02052059A1 WO 2002052059 A1 WO2002052059 A1 WO 2002052059A1 KR 0001523 W KR0001523 W KR 0001523W WO 02052059 A1 WO02052059 A1 WO 02052059A1
Authority
WO
WIPO (PCT)
Prior art keywords
flame retardant
polypropylene resin
resin composition
weight
silane
Prior art date
Application number
PCT/KR2000/001523
Other languages
French (fr)
Inventor
In-Sik Jung
Jong-Soo Hong
Sung-Man Lee
Man-Seang Her
Original Assignee
Samsung General Chemicals Co., Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Samsung General Chemicals Co., Ltd. filed Critical Samsung General Chemicals Co., Ltd.
Priority to US10/451,710 priority Critical patent/US7067576B2/en
Priority to PCT/KR2000/001523 priority patent/WO2002052059A1/en
Priority to CNB008200866A priority patent/CN1220789C/en
Priority to EP00989011A priority patent/EP1362131A4/en
Priority to JP2002553535A priority patent/JP3921448B2/en
Publication of WO2002052059A1 publication Critical patent/WO2002052059A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00Fireproofing materials
    • C09K21/14Macromolecular materials
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K3/2279Oxides; Hydroxides of metals of antimony
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/54Silicon-containing compounds
    • C08K5/541Silicon-containing compounds containing oxygen
    • C08K5/5415Silicon-containing compounds containing oxygen containing at least one Si—O bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2237Oxides; Hydroxides of metals of titanium
    • C08K2003/2241Titanium dioxide

Definitions

  • the present invention relates to a flame retardant polypropylene resin composition having polypropylene resin as a main component, and more particularly, to a polypropylene resin composition which comprises a polypropylene resin with melt flow rate of 4A8g 10minutes, a flame retardant additive of halogen with low melting point, an antimony oxide, an ultraviolet stabilizer, a coupling agent of silane, and a titanium dioxide as a light blocking agent, and has good weather proof, maintains the same level of flame retardant property and physical properties after hydrothermal dipping treatment.
  • Polypropylene resins are widely used in home electronic appliances, building members, interior decorating materials and automobile parts due to their excellent processing characteristics, chemical resistance and mechanical strength. These resins, however, lack flame retardant property and are difficult to use in automobile parts or electronic components which requires flame retardant property to prepare against the danger of fire. Therefore, much study has been made to impart flame retardant property to polyolefin resin by adding various organic, inorganic or phosphorus flame retardant additives. Japanese laid open Patent Publication No. 53-92855, 54-29350, 54-77658, 56-26954, 57-
  • the object of the invention is to solve the problems mentioned above and to provide a flame retardant polypropylene resin composition which has good flame retardant property at thin width and can produce secondary products which is able to maintain initial good flame retardant property at long outdoor exposure and hydrothermal dipping treatment, as well as maintain good weather proof and physical property.
  • the flame retardant polypropylene resin composition of the present invention comprises
  • the polypropylene resin used is a crystalline polypropylene homopolymer, or a copolymer of a polypropylene which is the main component, and one or more compounds or a mixture of two or more of compounds, the compounds being selected from the group consisting of ethylene, 1- butene, 1-pentene, 1-hexene, 4-metl ⁇ ylpentene, 1-heptene, 1-octene, and 1-decene.
  • the preferable polypropylene resin is a crystalline polypropylene homopolymer.
  • the melt flow rate of the polypropylene resin is 4-18g 10minutes, or more preferably 5 ⁇ 15g 10tninutes.
  • the content of polypropylene resin is 40-90% by weight, or more preferably 50-87% by weight in the entire resin composition.
  • the flame retardant additive of halogen with low melt point may be tetrabromobisphenol A bis- (dibromopropylether) or tetrabromo dimethysulfone dipropylether, or mixture thereof.
  • examples of commercially available products are PE-68(manufactured by Great Lake Corporation) or P680G(manufactured by Suzuhiro Chemicals, Co.).
  • Preferable content of tetrabromobisphenol A bis-(dibromoprophylether) or tetrabromodimethylsulfone dipropylether is 9-16% by weight per 100%) by weight of composition.
  • the coupling agent of silane in the flame retardant polypropylene resin composition of the present invention is expressed by the following general formula:
  • R is a hydrocarbon including vinyl, chloro, amino and mercapto
  • X an organic group that can be hydrolyzed
  • R' may be R or X.
  • R' is R
  • the material of R and R' can be different, and the materials of X can be different from each other, and the examples are vinyl trimethoxy silane, vinyl triethoxy silane, 3-aminopropyl triethoxy silane, ⁇ -(2-aminoethyl)-3- aminopropyltrimethoxy silane, 3-glycydoxypropyl trimethoxy silane, 3-chloropropyl trimethoxy silane, 3-metacryloxypropyl trimethoxy silane and 3-mercaptopropyltrimethoxy silane.
  • vinyl trimethoxy silane vinyl triethoxy silane or 3-mercaptopropyltrimethoxy silane.
  • the content of coupling agents of silane per 100%> by weight of composition is 0.1 ⁇ 5%> by weight, preferably 0.15-3% by weight, and more preferably 0.3-1% by weight.
  • the content is below 0.1 % by weight, the dispersive strength and adhesive strength with the antimony trioxide or flame retardant additives of halogen is not improved and cannot prevent blooming of flame retardant additive during dipping in hydrothermal test, making it difficult to maintain N-0 grade of flame retardant property at the width of l/32inch.
  • the content is above 5% by weight, the blooming of flame retardant additive is no more improved.
  • the flame retardant polypropylene resin composition of the present invention it is preferable to use UN absorbent and HALS stabilizer simultaneously as ultraviolet stabilizers, and preferable HALS stabilizer has molecular weight of more than 2,000. When molecular weight is below 2, 000, ultraviolet stabilizers easily bloom out of the secondary product, making it difficult to maintain long term ultraviolet stability.
  • the content of each UN absorbent and HALS ultraviolet stabilizer are preferably 0.1-1.5% by weight respectively.
  • N-0 grade of flame retardant property may be obtained but it is difficult to obtain a environment resistant resin composition which meets FI standard of for low rate of maintaining tensile impact strength after UN exposure treatment.
  • titanium dioxide is used as a light blocking agent to obtain FI grade of environment resistance, and the preferable content is 0.2 ⁇ 5%> by weight.
  • the content of titanium dioxide used is below 0.2%) by weight, there is no synergistic effect with ultraviolet stabilizer, and when the content is above 5% by weight, there is no further effect of blocking the light.
  • the antimony oxide used is antimony trioxide or antimony pentaoxide, or mixture thereof, and the content is 4-15% ⁇ by weight and preferably 5-12% by weight in the entire resin composition.
  • the flame retardant polypropylene resin composition of the present invention exhibits excellent flame retardancy of N-0 grade at the width of 1/32 inch in the vertical burning test (hereinafter referred to as UL94 vertical burning test) carried out according to the Tlammability Test of Plastic Materials for Parts of Mechanical device" of UL Subject 94. Further, in the test of weather proof and water proof (hereinafter referred to as UL746C weather proof test) carried out according to the "Test for Flammability of Plastic Materials for Parts in Electric Device" of UL subject 746C, the resin composition maintains the same grade of flame retardancy after long times of outdoor exposure and hydrothem al dipping treatment, and exhibits ability of maintaining physical properties. Therefore, the resin composition of the present invention can advantageously used in the production of electric appliances, building members, interior or exterior decorating materials, and automotive parts.
  • the mixture produced is molten and extruded at 190 ° C in the form of pellets.
  • the yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested and the results are shown in Table 1.
  • test pieces are UN exposure treated by the method of ASTM 2565 Type A under the condition of weather proof according to "Tests for Flammability of Plastic Materials for Parts in Electrical device" of UL subject 746C(Underwrites Laboratories Incorporation) (UN irradiation quantity: 0.35W/m 2 (340nm), black board temperature: 63 ° C, Water spray method).
  • the test pieces are dipped in hydrothermal tank of 70 ° C and maintained for 7 days, and then the flame retardancy and physical properties of the test pieces are tested.
  • the evaluation of flame retardancy is carried out based on the vertical (NO) burning tests according to the "Tests for Flammability of Plastic Materials for Parts in Mechanical device" of UL Subject 94(Underwriters Laboratories, Inc.).
  • the thickness of used test piece is 1/32 inch.
  • the tensile impact strength and maintenance rate are evaluated under the impact strength test standard ASTM D-1822, and the measuring instrument is product from TOYOSEIKI with sample of S-type and thickness 1/8 inch.
  • the pellets are prepared in the same way as in example 1 except that the amount of R- 103 as a light blocking agent in the composition is modified as shown in Table 1.
  • the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength.
  • the flame retardancy and physical properties are measured and the results are shown in Table 1.
  • the mixture produced is molten and extruded at 190 ° C in the form of pellets.
  • the yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested.
  • the methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 1.
  • pellets are prepared in the same way as in example 1 except that the amount of antimony trioxide as a flame retardant coagent in the composition is modified as shown in
  • the mixture produced is molten and extruded at 190°C in the form of pellets.
  • the yielded pellets are dried for three hours at 100°C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 °C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested.
  • the methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 1.
  • the pellets are prepared in the same way as in example 1 except that the polypropylene resin is modified to the polypropylene resin of different melt flow rate (the melt flow amount of molten resin for 10 minutes at 230°C with 2.16kg of load) as shown in Table 1. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 1.
  • the melt flow rate of polypropylene resin has much effect on the properties of the composition according to UN exposure test and hydrothermal dipping treatment.
  • the melt flow rate of polypropylene resin is below 4g l Ominitues, initial property is excellent, but after the UN disclosure test, the rate of maintaining physical properties becomes low.
  • the melt flow rate is above 20g/l Ominitues, the initial flame retardancy and the flame retardancy after UN disclosure test and the hydrothermal dipping treatment do not meet the NO grade of flame retardancy at the thickness of l/32inch. Therefore, the preferable melt flow rate of polypropylene is 4 ⁇ 18g ⁇ l0 minutes range to maintain FI grade of flame retardancy and physical properties.
  • IRGAFOS 168 produced by CIBA GEIGY
  • UN absorbent Tinuvin 326 produced by CIBA GEIGY
  • HALS ultraviolet stabilizer Chimabsorber 944FD produced by
  • the pellets are prepared in the same way as in example 1 except that the amount of coupling agents of silane, A- 174, in the composition is modified as shown in Table 2.
  • the pellets yielded in examples 9 and 10 are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested and the results are shown in Table 2.
  • Example 11 Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 7.9kg of crystalline polypropylene homopolymer with 8g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230 ° C with 2.16kg of load) as a polypropylene resin, 1.4kg of PE-68(produced by Great Lakes Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 700g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2 m), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of IRGAFOS 168(produced by CIBA GEIGY), 70g of UN absorbent (Tinuvin 326 produced by CIBA GEIGY), 70g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by CIBA GEIGY
  • the mixture produced is molten and extruded at 190 ° C in the form of pellets.
  • the yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested.
  • the methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 2.
  • the pellets are prepared in the same way as in example 1 except that the mixing content of UN absorbent and HALS ultraviolet stabilizer in the composition is modified as shown in Table 2. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 2.
  • the pellets are prepared in the same way as in example 14 except that the amount of PE-68 as a flame retardant agent of tetrabromobisphenol A bis-(dibromopropylether) and antimony trioxide(Sb 203) as a flame retardant coagent in the composition is modified as shown in Table 2. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 2.
  • n o ompos on omponen g , : omopoymer o poypropyene w o g mn , : omopoymer o poypropyene w o 4g/10min
  • A2 Homopolymer of polypropylene with MFR of 18g/10min
  • A3 Homopolymer of polypropylene with MFR of 2g/10min
  • A4 Homopolymer of polypropylene with MFR of 20g/10min
  • B Flame retardant agen
  • C antimony trioxide
  • D UV absorbent
  • E HALS ultraviolet stabilizer
  • F Titanium Dioxide
  • G silane coupling agent
  • FI in Final Grade indicates maintaining N-0 grade of flame retardancy and the ratio of more than 70% of maintaining tensile impact strength in UN exposure test and hydrotheimal dipping test
  • F2 indicates maintaining N-0 grade of flame retardancy and the ratio of more than 70% of maintaining tensile impact strength in UN exposure test or hydrothermal dipping test.
  • ⁇ G( ⁇ o Grade) indicates that the grade is neither FI nor F2.
  • M(Maintained) in Maintenance of FR indicates that flame retardancy is maintained after treatment
  • B(Below) indicates that flame retardancy is N-2 both before and after treatment
  • D(Deteriorated) indicates that initial flame retardancy of V-0 is reduced to N-2 after treatment.
  • the polypropylene resin composition of the present invention which comprises 40-90 % by weight of polypropylene resins with melt flow rate 4 ⁇ 18g/10minutes, 9-16 % by weight of flame retardant additives of halogen with low melt point, 4-15% by weight of antimony oxides in white granules, 0.2 ⁇ 3.0%o by weight of ultraviolet stabilizers, 0.1-5% by weight of coupling agents of silane, and 0.2-5% by weight of titanium dioxide, exhibits excellent weather proof, maintains initial N-0 grade of flame retardancy after hydrothermal dipping test, and also maintains physical properties.
  • the polypropylene resin composition according to the present invention has excellent flame retardancy, maintains initial high flame retardancy and excellent physical properties after long-term outdoor exposure and long hydrothermal treatment at the width of l/32inches, making it possible to obtain FI grade in UL746C environment-resistance test.
  • Secondary products of the resin of the present invention can be used in such products as light bulb socket of Christmas tree which is exposed outdoor for a longtime.

Abstract

The present invention provides a polypropylene resin composition comprising a polypropylene resin having 4 ∩ 18g/min of melt flow rate (MFR), flame retardant additive having low melting point, antimony oxide, UV stabilizer, coupling agent of silanes and titanium dioxide as light blocking agent. The resin composition of this invention provides secondarily processed products which have excellent flame retarding properties, even with its thin thickness and stability against the weather and maintainability of mechanical materials properties by maintaining its excellent original flame retarding properties after the long period of outdoor exposures and hydrothermal dipping treatment.

Description

FLAME RETARDANT POLYPROPYLENE RESIN COMPOSITION
TECHNICAL FIELD
The present invention relates to a flame retardant polypropylene resin composition having polypropylene resin as a main component, and more particularly, to a polypropylene resin composition which comprises a polypropylene resin with melt flow rate of 4A8g 10minutes, a flame retardant additive of halogen with low melting point, an antimony oxide, an ultraviolet stabilizer, a coupling agent of silane, and a titanium dioxide as a light blocking agent, and has good weather proof, maintains the same level of flame retardant property and physical properties after hydrothermal dipping treatment.
BACKGROUND ART
Polypropylene resins are widely used in home electronic appliances, building members, interior decorating materials and automobile parts due to their excellent processing characteristics, chemical resistance and mechanical strength. These resins, however, lack flame retardant property and are difficult to use in automobile parts or electronic components which requires flame retardant property to prepare against the danger of fire. Therefore, much study has been made to impart flame retardant property to polyolefin resin by adding various organic, inorganic or phosphorus flame retardant additives. Japanese laid open Patent Publication No. 53-92855, 54-29350, 54-77658, 56-26954, 57-
87462 and 60-110738 disclose preparation method of flame retardation polypropylene resin composition by adding inorganic flame retardant additives such as magnesium hydroxide, aluminum hydroxide or hydrotalcite to impart the resin flame retardant property. But, in order to obtain flame retardant grade V-0, more than 50% of inorganic filler is needed, resulting in deterioration of processability, generation of gas and decrease in impact strength. Japanese Patent Publication No. 53-30739 discloses flame retardant polypropylene resin composition produced by adding organic flame retardant additive of halogen compound such as decabromodiphenylether and dodecachloro-dodecahydromethanodibenzocyclooctane. hi addition, fpreparation method of flame retardant polypropylene resin composition by adding tetrabromobisphenol A bis-(dibromoprophylether), bis-
(tribromophenoxyethyl)tetrabromobisphenol A ether, hexabromo cyclododecan and tetrabomobisphenol A. Though these resin compositions are excellent in flame retardant property and processability, resistance to weather and hot water is inferior and it is difficult to maintain physical properties and initial flame retardant property making it difficult to use the resin in products which are exposed outdoor such as light bulb socket of Christmas tree.
DISCLOSURE OF INVENTION
The object of the invention is to solve the problems mentioned above and to provide a flame retardant polypropylene resin composition which has good flame retardant property at thin width and can produce secondary products which is able to maintain initial good flame retardant property at long outdoor exposure and hydrothermal dipping treatment, as well as maintain good weather proof and physical property.
The flame retardant polypropylene resin composition of the present invention comprises
40-90% by weight of polypropylene resins with melt flow rate 4~18g/10minutes, 9-16% by weight of flame retardant additives of halogen with low melt point, 4-15% by weight of antimony oxides in white granules, 0.2-3.0% by weight of ultraviolet stabilizers, 0.1-5% by weight of coupling agents of silane, and 0.2-5% by weight of titanium dioxide.
In the flame retardant polypropylene resin composition of the present invention, the polypropylene resin used is a crystalline polypropylene homopolymer, or a copolymer of a polypropylene which is the main component, and one or more compounds or a mixture of two or more of compounds, the compounds being selected from the group consisting of ethylene, 1- butene, 1-pentene, 1-hexene, 4-metlιylpentene, 1-heptene, 1-octene, and 1-decene. The preferable polypropylene resin is a crystalline polypropylene homopolymer. The melt flow rate of the polypropylene resin is 4-18g 10minutes, or more preferably 5~15g 10tninutes. The content of polypropylene resin is 40-90% by weight, or more preferably 50-87% by weight in the entire resin composition.
In the flame retardant polypropylene resin composition of the present invention, the flame retardant additive of halogen with low melt point may be tetrabromobisphenol A bis- (dibromopropylether) or tetrabromo dimethysulfone dipropylether, or mixture thereof. Examples of commercially available products are PE-68(manufactured by Great Lake Corporation) or P680G(manufactured by Suzuhiro Chemicals, Co.). Preferable content of tetrabromobisphenol A bis-(dibromoprophylether) or tetrabromodimethylsulfone dipropylether is 9-16% by weight per 100%) by weight of composition. When the content of flame retardant additive is below 9 %> by weight, flame retardation grade of N-0 cannot be obtained with thickness of 1/32 inch, and when the content of flame retardant additive is above 16% by weight, weather proof is reduced resulting in the undesirable effect of making it difficult to maintain physical properties.
The coupling agent of silane in the flame retardant polypropylene resin composition of the present invention is expressed by the following general formula:
RR' SiX2 where R is a hydrocarbon including vinyl, chloro, amino and mercapto, X an organic group that can be hydrolyzed, and R' may be R or X. When R' is R, the material of R and R' can be different, and the materials of X can be different from each other, and the examples are vinyl trimethoxy silane, vinyl triethoxy silane, 3-aminopropyl triethoxy silane, Ν-(2-aminoethyl)-3- aminopropyltrimethoxy silane, 3-glycydoxypropyl trimethoxy silane, 3-chloropropyl trimethoxy silane, 3-metacryloxypropyl trimethoxy silane and 3-mercaptopropyltrimethoxy silane. In order to improve the dispersive strength and adhesive strength with antimony trioxide and flame retardant additives of halogen, it is preferable to use vinyl trimethoxy silane, vinyl triethoxy silane or 3-mercaptopropyltrimethoxy silane.
The content of coupling agents of silane per 100%> by weight of composition is 0.1~5%> by weight, preferably 0.15-3% by weight, and more preferably 0.3-1% by weight. When the content is below 0.1 % by weight, the dispersive strength and adhesive strength with the antimony trioxide or flame retardant additives of halogen is not improved and cannot prevent blooming of flame retardant additive during dipping in hydrothermal test, making it difficult to maintain N-0 grade of flame retardant property at the width of l/32inch. When the content is above 5% by weight, the blooming of flame retardant additive is no more improved.
In the flame retardant polypropylene resin composition of the present invention, it is preferable to use UN absorbent and HALS stabilizer simultaneously as ultraviolet stabilizers, and preferable HALS stabilizer has molecular weight of more than 2,000. When molecular weight is below 2, 000, ultraviolet stabilizers easily bloom out of the secondary product, making it difficult to maintain long term ultraviolet stability. The content of each UN absorbent and HALS ultraviolet stabilizer are preferably 0.1-1.5% by weight respectively. When only one of UN absorbent or HALS ultraviolet stabilizer is added, N-0 grade of flame retardant property may be obtained but it is difficult to obtain a environment resistant resin composition which meets FI standard of for low rate of maintaining tensile impact strength after UN exposure treatment. In the flame retardant polypropylene resin composition of the present invention, titanium dioxide is used as a light blocking agent to obtain FI grade of environment resistance, and the preferable content is 0.2~5%> by weight. When the content of titanium dioxide used is below 0.2%) by weight, there is no synergistic effect with ultraviolet stabilizer, and when the content is above 5% by weight, there is no further effect of blocking the light. In the flame retardant polypropylene resin composition of the present invention, the antimony oxide used is antimony trioxide or antimony pentaoxide, or mixture thereof, and the content is 4-15%ι by weight and preferably 5-12% by weight in the entire resin composition.
The flame retardant polypropylene resin composition of the present invention exhibits excellent flame retardancy of N-0 grade at the width of 1/32 inch in the vertical burning test (hereinafter referred to as UL94 vertical burning test) carried out according to the Tlammability Test of Plastic Materials for Parts of Mechanical device" of UL Subject 94. Further, in the test of weather proof and water proof (hereinafter referred to as UL746C weather proof test) carried out according to the "Test for Flammability of Plastic Materials for Parts in Electric Device" of UL subject 746C, the resin composition maintains the same grade of flame retardancy after long times of outdoor exposure and hydrothem al dipping treatment, and exhibits ability of maintaining physical properties. Therefore, the resin composition of the present invention can advantageously used in the production of electric appliances, building members, interior or exterior decorating materials, and automotive parts.
The present invention will be further described in detail with reference to the examples and comparative examples as below. The examples, however, are for the purpose of illustration and are not intended to limit the scope of the invention.
BEST MODE FOR CARRYING OUT THE INVENTION
Example 1
Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 7.9kg of crystalline polypropylene homopolymer with 8g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230 ° C with 2.16kg of load) as a polypropylene resin, 1.4kg of PE-68(produced by Great Lakes Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 700g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2μm), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of IRGAFOS 168(produced by CIBA GEIGY), 30g of UV absorbent (Tinuvin 326 produced by CIBA GEIGY), 30g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by CIBA GEIGY), 200g of light blocking agent TiO2(R-103 produced by Dupont, Inc.), and 70g of silane coupling agent (A- 174 produced by Union carbide). By using a two-axis stirring extruder with diameter of 30mm, the mixture produced is molten and extruded at 190 ° C in the form of pellets. The yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested and the results are shown in Table 1.
Method of treatment
The test pieces are UN exposure treated by the method of ASTM 2565 Type A under the condition of weather proof according to "Tests for Flammability of Plastic Materials for Parts in Electrical device" of UL subject 746C(Underwrites Laboratories Incorporation) (UN irradiation quantity: 0.35W/m2(340nm), black board temperature: 63 °C, Water spray method). The test pieces are dipped in hydrothermal tank of 70 °C and maintained for 7 days, and then the flame retardancy and physical properties of the test pieces are tested.
Method of evaluation
The evaluation of flame retardancy is carried out based on the vertical (NO) burning tests according to the "Tests for Flammability of Plastic Materials for Parts in Mechanical device" of UL Subject 94(Underwriters Laboratories, Inc.). The thickness of used test piece is 1/32 inch. The tensile impact strength and maintenance rate are evaluated under the impact strength test standard ASTM D-1822, and the measuring instrument is product from TOYOSEIKI with sample of S-type and thickness 1/8 inch.
Examples 2-3 and comparative examples 1-3
The pellets are prepared in the same way as in example 1 except that the amount of R- 103 as a light blocking agent in the composition is modified as shown in Table 1.
Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 1.
Comparing the results of examples 1-3 and the results of comparative examples 1-3 as shown in Table 1, it can be shown that when appropriate amounts of TiO2 are added as a light blocking agent, synergistic effect with UN absorbent and HALS ultraviolet stabilizer arises, making it possible to maintain high tensile impact strength as well as flame retardancy of N-0 grade at UN exposure test. In addition, after hydrothermal dipping treatment, flame retardancy and tensile impact strength are maintained excellently and exhibits high weather proof so that FI grade of the 764C on outdoor and indoor electrical device.
Example 4
Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 8.2kg of crystalline polypropylene homopolymer with 8g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230 ° C with 2.16kg of load) as a polypropylene resin, 1.4kg of PE-68(produced by Great Lakes Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 400g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2 m), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of IRGAFOS 168(ρroduced by CIBA GEIGY), 30g of UN absorbent (Tinuvin 326 produced by CIBA GEIGY), 30g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by CIBA GEIGY), 200g of light blocking agent TiO2(R-103 produced by Dupont, Inc.), and 70g of silane coupling agent (A- 174 produced by Union carbide). By using a two-axis stirring extruder with diameter of 30mm, the mixture produced is molten and extruded at 190 ° C in the form of pellets. The yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested. The methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 1.
Examples 5-6 and comparative examples 4-5
The pellets are prepared in the same way as in example 1 except that the amount of antimony trioxide as a flame retardant coagent in the composition is modified as shown in
Table 1. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 1.
Comparing the results of examples 5-6 and the results of comparative examples 4-5 as shown in Table 1, it can be shown that only when more than certain amounts of flame retardant coagent should be added in order to generate synergistic effect of flame retardancy and to maintain flame retardancy after UN exposure test and hydrothermal dipping treatment. When antimony trioxides are added excessively more than 17%, there is no more synergistic effect in fame retardancy and the rate of maintaining physical property is low, making it impossible to obtain FI grade. Example 7
Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 7.9kg of crystalline polypropylene homopolymer with 4g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230°C with 2.16kg of load) as a polypropylene resin, 1.4kg of PE-68(produced by Great Lakes Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 700g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2 m), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of IRGAFOS 168(ρroduced by CIBA GEIGY), 30g of UN absorbent (Tinuvin 326 produced by CIBA GEIGY), 30g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by CIBA GEIGY), 200g of light blocking agent TiO2(R-103 produced by Dupont, Inc.), and 70g of silane coupling agent (A- 174 produced by Union carbide). By using a two-axis stirring extruder with diameter of 30mm, the mixture produced is molten and extruded at 190°C in the form of pellets. The yielded pellets are dried for three hours at 100°C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 °C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested. The methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 1.
Example 8 and comparative examples 6-7
The pellets are prepared in the same way as in example 1 except that the polypropylene resin is modified to the polypropylene resin of different melt flow rate (the melt flow amount of molten resin for 10 minutes at 230°C with 2.16kg of load) as shown in Table 1. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 1.
As shown in Table 1, the melt flow rate of polypropylene resin has much effect on the properties of the composition according to UN exposure test and hydrothermal dipping treatment. When the melt flow rate of polypropylene resin is below 4g l Ominitues, initial property is excellent, but after the UN disclosure test, the rate of maintaining physical properties becomes low. And when the melt flow rate is above 20g/l Ominitues, the initial flame retardancy and the flame retardancy after UN disclosure test and the hydrothermal dipping treatment do not meet the NO grade of flame retardancy at the thickness of l/32inch. Therefore, the preferable melt flow rate of polypropylene is 4~18g^l0 minutes range to maintain FI grade of flame retardancy and physical properties.
Example 9
Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 7.9kg of crystalline polypropylene homopolymer with 8g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230 ° C with
2.16kg of load) as a polypropylene resin, 1.4kg of PE-68(produced by Great Lakes
Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 700g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2 m), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of
IRGAFOS 168(produced by CIBA GEIGY), 30g of UN absorbent (Tinuvin 326 produced by CIBA GEIGY), 30g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by
CIBA GEIGY), 200g of light blocking agent TiO2(R-103 produced by Dupont, h e), and
15g of silane coupling agent (A-174 produced by Union carbide). By using a two-axis stirring extruder with diameter of 30mm, the mixture produced is molten and extruded at 190 ° C in the form of pellets. The yielded pellets are dried for three hours at 100 " C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested. The methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 2.
Example 10 and comparative examples 8-10
The pellets are prepared in the same way as in example 1 except that the amount of coupling agents of silane, A- 174, in the composition is modified as shown in Table 2.
The pellets yielded in examples 9 and 10 are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested and the results are shown in Table 2.
As shown in Table 2, when appropriate amounts of coupling agent of silane are added, the adhesiveness and dispersibility between retardant agent or retardant coagent and the polypropylene resin, the main composition of the resin, become better, NO grade of flame retardancy is maintained, and tensile strength is highly maintained, improving resistance to environment to FI grade. The preferable amount of coupling agent of silane is seen to be 0.3-3% by weight.
Example 11 Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 7.9kg of crystalline polypropylene homopolymer with 8g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230 ° C with 2.16kg of load) as a polypropylene resin, 1.4kg of PE-68(produced by Great Lakes Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 700g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2 m), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of IRGAFOS 168(produced by CIBA GEIGY), 70g of UN absorbent (Tinuvin 326 produced by CIBA GEIGY), 70g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by CIBA GEIGY), 200g of light blocking agent TiO2(R-103 produced by Dupont, Inc.), and 70g of silane coupling agent (A-174 produced by Union carbide). By using a two-axis stirring extruder with diameter of 30mm, the mixture produced is molten and extruded at 190 ° C in the form of pellets. The yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested. The methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 2.
Examples 12-13 and comparative examples 11-16
The pellets are prepared in the same way as in example 1 except that the mixing content of UN absorbent and HALS ultraviolet stabilizer in the composition is modified as shown in Table 2. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 2.
As shown in Table 2, by using mixture of UN absorbent and HALS ultra violet stabilizer in appropriate amounts, the flame retardancy and resistance to environment are shown to be improved.
Example 14
Following components are introduced into the Hensel mixer and mixed by stirring for 3 minutes: 8.1kg of crystalline polypropylene homopolymer with 8g/10minutes of melt flow rate (the melt flow amount of molten resin for 10 minutes at 230 ° C with 2.16kg of load) as a polypropylene resin, 1.3kg of PE-68(produced by Great Lakes Corporation) as a tetrabromobisphenol A bis-(dibromopropylether), 650g of antimony trioxide (Sb203 produced by Cheil Flame Retardant, Ltd., 1.2 m), and as additives, lOg of calcium stearate, lOg of antioxidant (1010 Produced by CIBA GEIGY), 20g of IRGAFOS 168(produced by CIBA GEIGY), 30g of UN absorbent (Tinuvin 326 produced by CIBA GEIGY), 30g of HALS ultraviolet stabilizer (Chimabsorber 944FD produced by CIBA GEIGY), 200g of light blocking agent TiO2(R-103 produced by Dupont, hie), and 70g of silane coupling agent (A-174 produced by Union carbide). By using a two-axis stirring extruder with diameter of 30mm, the mixture produced is molten and extruded at 190 ° C in the form of pellets. The yielded pellets are dried for three hours at 100 ° C and molded by using an injection-molding machine with maximum temperature of a cylinder fixed at 200 ° C to provide test pieces for test flame retardancy. Then, the flame retardancy and physical properties of the test pieces are tested. The methods of treatment and evaluation are the same as in example 1 and the results are shown in Table 2. Examples 15-16 and comparative examples 17-18
The pellets are prepared in the same way as in example 14 except that the amount of PE-68 as a flame retardant agent of tetrabromobisphenol A bis-(dibromopropylether) and antimony trioxide(Sb 203) as a flame retardant coagent in the composition is modified as shown in Table 2. Then, the yielded pellets are molded by using an injection-molding machine to provide test pieces for testing flame retardancy and tensile impact strength. The flame retardancy and physical properties are measured and the results are shown in Table 2.
As shown in Table 2, by using mixture of flame retardant agent and coagent in specific amounts, the flame retardancy and resistance to environment are shown to be improved.
rJ1
cπ 1
Figure imgf000016_0001
* unit of tensile impact strength : kg.cm/cm square
* NG : No Gtade
* FR: Flame Retardancy, TIS: Tensile Impact Strength, NG: No Grade
* M: Maintained, D: Deteriorated, B: Below the standard
CT>
Figure imgf000017_0001
n o ompos on omponen: g , : omopoymer o poypropyene w o g mn , : omopoymer o poypropyene w o 4g/10min , A2: Homopolymer of polypropylene with MFR of 18g/10min , A3: Homopolymer of polypropylene with MFR of 2g/10min , A4: Homopolymer of polypropylene with MFR of 20g/10min , B: Flame retardant agen , C: antimony trioxide , D: UV absorbent , E: HALS ultraviolet stabilizer , F: Titanium Dioxide , G: silane coupling agent
In Tables 1 and 2, FI in Final Grade indicates maintaining N-0 grade of flame retardancy and the ratio of more than 70% of maintaining tensile impact strength in UN exposure test and hydrotheimal dipping test, and F2 indicates maintaining N-0 grade of flame retardancy and the ratio of more than 70% of maintaining tensile impact strength in UN exposure test or hydrothermal dipping test. ΝG(Νo Grade) indicates that the grade is neither FI nor F2. M(Maintained) in Maintenance of FR indicates that flame retardancy is maintained after treatment, B(Below) indicates that flame retardancy is N-2 both before and after treatment, and D(Deteriorated) indicates that initial flame retardancy of V-0 is reduced to N-2 after treatment.
As can be seen in Tables 1 and 2, the polypropylene resin composition of the present invention, which comprises 40-90 % by weight of polypropylene resins with melt flow rate 4~18g/10minutes, 9-16 % by weight of flame retardant additives of halogen with low melt point, 4-15% by weight of antimony oxides in white granules, 0.2~3.0%o by weight of ultraviolet stabilizers, 0.1-5% by weight of coupling agents of silane, and 0.2-5% by weight of titanium dioxide, exhibits excellent weather proof, maintains initial N-0 grade of flame retardancy after hydrothermal dipping test, and also maintains physical properties.
As readily can be seen in the above description, the polypropylene resin composition according to the present invention has excellent flame retardancy, maintains initial high flame retardancy and excellent physical properties after long-term outdoor exposure and long hydrothermal treatment at the width of l/32inches, making it possible to obtain FI grade in UL746C environment-resistance test. Secondary products of the resin of the present invention can be used in such products as light bulb socket of Christmas tree which is exposed outdoor for a longtime.

Claims

WHAT IS CLAIMED IS:
1. A flame retardant polypropylene resin composition comprising 40-90 % by weight of polypropylene resin with melt flow rate of 4-18g/10minutes, 9-16 % by weight of flame retardant additive of halogen with low melting point, 4-15%» by weight of antimony oxide in white granules, 0.2-3.0% by weight of ultraviolet stabilizer, 0.1-5% by weight of silane coupling agents, and 0.2-5% by weight of titanium dioxide.
2. The flame retardant polypropylene resin composition according to claim 1, wherein said polypropylene resin is a, polypropylene homopolymer or a crystalline polypropylene copolymer.
3. The flame retardant polypropylene resin composition according to claim 1, wherein said flame retardant additive of halogen with low melting point is tetrabromobisphenol A bis- (dibromopropylether) or tetrabromodimethysulfone dipropylether, or mixture thereof.
4. The flame retardant polypropylene resin composition according to claim 1, wherein said antimony oxide is an antimony trioxide or antimony pentaoxide, or mixture thereof.
5. The flame retardant polypropylene resin composition according to claim 1, wherein said ultraviolet stabilizer us a mixture of HALS ultraviolet stabilizer with molecular weight of more than 2,000 and UN absorbent.
6. The flame retardant polypropylene resin composition according to claim 1, wherein said silane coupling agent is a vinyl trimethoxy silane, vinyl trietiioxy silane, 3-aminopropyl triethoxy silane, N-(2-amfooethyl)-3-aminopropyltrimethoxy silane, 3-glycydoxypropyl trimethoxy silane, 3-chloropropyl trimethoxy silane, 3-metacryloxypropyl trimethoxy silane or 3- mercaptopropyltrimethoxy silane.
PCT/KR2000/001523 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition WO2002052059A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
US10/451,710 US7067576B2 (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition
PCT/KR2000/001523 WO2002052059A1 (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition
CNB008200866A CN1220789C (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition
EP00989011A EP1362131A4 (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition
JP2002553535A JP3921448B2 (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/KR2000/001523 WO2002052059A1 (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition

Publications (1)

Publication Number Publication Date
WO2002052059A1 true WO2002052059A1 (en) 2002-07-04

Family

ID=19198315

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2000/001523 WO2002052059A1 (en) 2000-12-22 2000-12-22 Flame retardant polypropylene resin composition

Country Status (5)

Country Link
US (1) US7067576B2 (en)
EP (1) EP1362131A4 (en)
JP (1) JP3921448B2 (en)
CN (1) CN1220789C (en)
WO (1) WO2002052059A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101456994B (en) * 2007-12-14 2011-05-11 金发科技股份有限公司 Flame retardant polypropylene resin blend and preparation method thereof
CN110951169A (en) * 2019-12-13 2020-04-03 上海日之升科技有限公司 Light-shading low-linear-expansion-coefficient polypropylene composite material and preparation method thereof

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100901949B1 (en) * 2003-01-15 2009-06-10 삼성토탈 주식회사 Flame retardant polypropylene resin composition with excellent weatherability
US7959998B2 (en) * 2005-03-02 2011-06-14 Eastman Chemical Company Transparent, oxygen-scavenging compositions containing polyesters comprising a cyclobutanediol and articles prepared therefrom
WO2007061883A2 (en) * 2005-11-18 2007-05-31 Research Foundation Of State University Of New York Flame retardant plastic compositions
JP5174252B1 (en) * 2012-01-27 2013-04-03 出光ライオンコンポジット株式会社 Flame-retardant resin composition, molded body, and laminated structure
KR101602634B1 (en) * 2014-05-23 2016-03-14 덕양산업 주식회사 Manufacturing method of skin for crash pad
CN105037944B (en) * 2015-08-21 2017-06-20 天津市顺康科技发展有限公司 The preparation method and application of soft base curing process construction material
CN111978634A (en) * 2020-08-18 2020-11-24 天津市久大塑料制品有限公司 Waterproof and sun-proof plastic woven bag
CN113845724B (en) * 2021-10-18 2023-12-15 上海金发科技发展有限公司 Heat-aging-resistant shading polypropylene material and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5530739A (en) * 1978-08-25 1980-03-04 Toshiba Corp Automatic transaction unit
JPS5787462A (en) * 1980-11-20 1982-05-31 Kyowa Chem Ind Co Ltd Flame-retardant resin composition containing magnesium oxide with its surface treated

Family Cites Families (101)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3332927A (en) * 1966-02-14 1967-07-25 Cabot Corp Process for polymerization
US3632620A (en) * 1968-06-26 1972-01-04 Olin Mathieson Preparation of isocyanates from carbodiimides
CA920299A (en) * 1968-08-01 1973-01-30 Mitsui Petrochemical Industries Process for the polymerization and/or copolymerization of olefins with use of ziegler-type catalytsts supported on carrier
US3642772A (en) * 1968-09-04 1972-02-15 Boehringer Mannheim Gmbh Process for preparing s-adenosyl homocysteine
NL163522B (en) * 1970-07-20 1980-04-15 Montedison Spa PROCESS FOR PREPARING A CATALYST FOR THE POLYMERIZATION OF OLEFINS-1.
US4226963A (en) * 1971-06-25 1980-10-07 Montedison S.P.A. Process for the stereoregular polymerization of alpha-olephins
US4187196A (en) * 1971-06-25 1980-02-05 Montedison S.P.A. Process for the stereoregular polymerization of alpha-olefins
US4156063A (en) * 1971-06-25 1979-05-22 Montecanti Edison, S.p.A. Process for the stereoregular polymerization of alpha olefins
NL160286C (en) * 1971-06-25
US4107414A (en) * 1971-06-25 1978-08-15 Montecatini Edison S.P.A. Process for the stereoregular polymerization of alpha olefins
US4107413A (en) * 1971-06-25 1978-08-15 Montedison S.P.A. Process for the stereoregular polymerization of alpha olefins
BE785673A (en) * 1971-06-30 1973-01-02 Naphtachimie Sa POLYMERIZATION CATALYZERS OF OLEFINS PREPARED FROM DECOMPOSED ORGANOMAGNESIANS
US4013823A (en) * 1972-06-09 1977-03-22 The B. F. Goodrich Company Process for preparing elastomeric copolymers of ethylene and higher alpha-olefins
US3953414A (en) * 1972-09-13 1976-04-27 Montecatini Edison S.P.A., Catalysts for the polymerization of olefins to spherically shaped polymers
US4071674A (en) * 1972-09-14 1978-01-31 Mitsui Petrochemical Industries Ltd. Process for polymerization or copolymerization of olefin and catalyst compositions used therefor
US4107415A (en) * 1972-09-26 1978-08-15 Montecatini Edison S.P.A. Process for the stereospecific polymerization of alpha-olefins
US4071672A (en) * 1972-11-10 1978-01-31 Mitsui Petrochemical Industries Ltd. Process for polymerizing or copolymerizing olefins
US3899477A (en) * 1973-02-16 1975-08-12 Monsanto Co Polymerization of ethylene
US4157435A (en) * 1974-08-10 1979-06-05 Mitsui Petrochemical Industries, Ltd. Process for preparing highly stereoregular polyolefins and catalyst used therefor
US4076924A (en) * 1974-09-03 1978-02-28 Mitsui Petrochemical Industries Ltd. Process for polymerization or copolymerizing olefins containing at least 3 carbon atoms
US4614727A (en) * 1975-01-23 1986-09-30 Montecatini Edison S.P.A. Polymerization catalyst
JPS565404B2 (en) * 1975-02-14 1981-02-04
IT1042667B (en) * 1975-09-18 1980-01-30 Montedison Spa CATALYSTS FOR THE POLYMERIZATION OF SEROIDAL POLYMER OLEFINS
US4069169A (en) * 1975-11-24 1978-01-17 Mitsui Petrochemical Industries Ltd. Process for preparation of catalyst component supported on high performance carrier
IT1062072B (en) * 1976-06-03 1983-06-25 Montedison Spa CATALYSTS FOR THE POLYMERIZATION OF ETHYLENE
US4158642A (en) * 1977-04-25 1979-06-19 Exxon Research & Engineering Co. Trialkyl aluminum cocatalyst
US4148756A (en) * 1977-04-25 1979-04-10 Exxon Research & Engineering Co. Novel trialkyl aluminum cocatalyst
GB1603724A (en) * 1977-05-25 1981-11-25 Montedison Spa Components and catalysts for the polymerisation of alpha-olefins
IT1114822B (en) * 1977-07-04 1986-01-27 Montedison Spa COMPONENTS OF CATALYSTS FOR THE POLYMERIZATION OF ALPHA-OLEFINS
IT1113129B (en) * 1978-04-12 1986-01-20 Montedison Spa CATALYSTS AND COMPONENTS OF CATALYSTS FOR THE POLYMERIZATION OF OLEFINS
JPS5919566B2 (en) * 1978-07-28 1984-05-07 東亜燃料工業株式会社 Method for producing catalyst component for α-olefin polymerization
IT1098272B (en) * 1978-08-22 1985-09-07 Montedison Spa COMPONENTS, CATALYSTS AND CATALYSTS FOR THE POLYMERIZATION OF ALPHA-OLEFINS
FR2436794A1 (en) * 1978-09-22 1980-04-18 Naphtachimie Sa PROCESS FOR THE POLYMERIZATION OF ETHYLENE AND PRODUCTS THEREOF
JPS6314246Y2 (en) * 1979-07-26 1988-04-21
JPS6037804B2 (en) * 1979-04-11 1985-08-28 三井化学株式会社 Method for manufacturing carrier for olefin polymerization catalyst
JPS56811A (en) * 1979-06-18 1981-01-07 Mitsui Petrochem Ind Ltd Preparation of olefin polymer or copolymer
US4482687A (en) * 1979-10-26 1984-11-13 Union Carbide Corporation Preparation of low-density ethylene copolymers in fluid bed reactor
US4277372A (en) * 1980-01-09 1981-07-07 Hercules Incorporated Solid catalyst component for olefin polymerization
JPS6023764B2 (en) * 1980-02-27 1985-06-10 チッソ株式会社 Method for producing α-olefin polymer
US4384983A (en) * 1981-05-26 1983-05-24 Standard Oil Company (Indiana) Catalyst and process for production of polyolefins of improved morphology
JPS5842639A (en) * 1981-09-07 1983-03-12 Toa Nenryo Kogyo Kk Polyolefin composition
JPS5883006A (en) * 1981-11-13 1983-05-18 Mitsui Petrochem Ind Ltd Polymerization of olefin
FR2529207A1 (en) * 1982-06-24 1983-12-30 Bp Chimie Sa PROCESS FOR THE PREPARATION OF CATALYST SUPPORTS FOR THE POLYMERIZATION OF ALPHA-OLEFINS AND SUPPORTS OBTAINED
FR2532649B1 (en) * 1982-09-07 1986-08-29 Bp Chimie Sa COPOLYMERIZATION OF ETHYLENE AND HEXENE-1 IN A FLUIDIZED BED
IT1195953B (en) * 1982-09-10 1988-11-03 Montedison Spa COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE
US4518706A (en) * 1982-09-30 1985-05-21 E. I. Du Pont De Nemours And Company Hydrocarbon soluble catalyst supports and resultant polymerization catalysts
US4434282A (en) * 1982-10-04 1984-02-28 The Dow Chemical Company Process for polymerizing olefins
JPS59117508A (en) * 1982-12-24 1984-07-06 Mitsui Petrochem Ind Ltd Olefin polymerization
US4477639A (en) * 1983-05-27 1984-10-16 Shell Oil Company Olefin polymerization catalyst component and composition and method of preparation
JPS601241A (en) * 1983-06-17 1985-01-07 Kyowa Chem Ind Co Ltd Flame-retardant resin composition
JPS60110738A (en) * 1983-11-22 1985-06-17 Asahi Glass Co Ltd Flame-retarding polyolefin composition
FR2560200B1 (en) * 1984-02-23 1986-06-27 Bp Chimie Sa PROCESS FOR THE PREPARATION OF SUPPORTED CATALYSTS BASED ON VANADIUM COMPOUNDS FOR THE POLYMERIZATION AND COPOLYMERIZATION OF ETHYLENE
US4988656A (en) * 1984-03-23 1991-01-29 Amoco Corporation Olefin polymerization catalyst
US4866022A (en) * 1984-03-23 1989-09-12 Amoco Corporation Olefin polymerization catalyst
US5013702A (en) * 1984-03-23 1991-05-07 Amoco Corporation Olefin polymerization catalyst
JPS60228504A (en) * 1984-04-26 1985-11-13 Sumitomo Chem Co Ltd Production of olefin polymer
GB2176443B (en) * 1985-06-10 1990-11-14 Canon Kk Liquid jet recording head and recording system incorporating the same
US4812074A (en) 1985-08-30 1989-03-14 Minigrip, Inc. Apparatus for making bag material
JPH06104693B2 (en) * 1986-01-06 1994-12-21 東邦チタニウム株式会社 Catalyst for olefin polymerization
DE3777339D1 (en) * 1986-05-06 1992-04-16 Toho Titanium Co Ltd CATALYST FOR THE POLYMERIZATION OF OLEFINS.
JPS62267305A (en) * 1986-05-15 1987-11-20 Sumitomo Chem Co Ltd Production of olefinic polymer
JPH0832737B2 (en) * 1986-10-08 1996-03-29 東邦チタニウム株式会社 Solid catalyst component for olefin polymerization
US4777639A (en) * 1986-12-15 1988-10-11 Prc Corporation Laser optical element mounting arrangement and method
IT1203330B (en) * 1987-02-06 1989-02-15 Enichem Base Spa Catalyst and catalyst component for the polymerization of ethylene or the co-polymerization of ethylene with alpha-Olefin
JP2502624B2 (en) * 1987-09-22 1996-05-29 東燃株式会社 Catalyst component for olefin polymerization
JPH0717709B2 (en) * 1987-11-13 1995-03-01 日本石油株式会社 Method for producing ultra high molecular weight polyethylene
FR2623812B1 (en) * 1987-11-30 1992-02-21 Bp Chimie Sa CATALYST FOR POLYMERIZATION OF ZIEGLER NATTA-TYPE OLEFINS AND PROCESS FOR THE PREPARATION THEREOF FROM MAGNESIUM DIALCOXIDE
EP0322798B1 (en) * 1987-12-26 1994-03-02 Toho Titanium Co. Ltd. A solid catalyst component for the polymerization of olefins and an olefin polymerization catalyst
US4912074A (en) * 1988-01-15 1990-03-27 Mobil Oil Corporation Catalyst composition for preparing high density or medium density olefin polymers
EP0350170B2 (en) * 1988-06-17 2001-09-12 Mitsui Chemicals, Inc. Process for polymerising olefins and polymerisation catalyst therefor
US5134104A (en) * 1988-06-28 1992-07-28 Sumitomo Chemical Company, Limited Liquid catalyst component, catalyst system containing said component and process for producing ethylene-α-olefin copolymer using said catalyst system
US5064798A (en) * 1988-08-19 1991-11-12 Exxon Chemical Patents Inc. Catalyst for olefin polymerization
IT1227259B (en) * 1988-09-30 1991-03-28 Himont Inc CATALYSTS FOR THE POLYMERIZATION OF OLEFINE.
JP2893743B2 (en) * 1989-08-10 1999-05-24 三菱化学株式会社 Production of α-olefin polymer
FR2651001B1 (en) * 1989-08-17 1993-03-12 Bp Chemicals Sa PROCESS FOR THE PREPARATION OF A ZIEGLER-NATTA CATALYST BASED ON VANADIUM AND TITANIUM
US4946816A (en) * 1989-08-21 1990-08-07 Amoco Corporation Morphology-controlled olefin polymerization catalyst
FR2656314B1 (en) * 1989-12-22 1992-04-17 Bp Chemicals Snc ZIRCONIUM CATALYST SUPPORTED ON MAGNESIUM CHLORIDE, PROCESS FOR THE PREPARATION AND USE OF THE CATALYST IN OLEFIN POLYMERIZATION.
IT1241062B (en) * 1990-01-10 1993-12-29 Himont Inc COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE
US5021382A (en) * 1990-02-28 1991-06-04 Exxon Chemical Patents Inc. Diene activated ziegler transition metal catalyst components for ethylene polymerization
JP3049569B2 (en) * 1990-03-23 2000-06-05 東ソー株式会社 Method for producing polyolefin
DE69111354T2 (en) * 1990-04-18 1995-12-21 Mitsui Petrochemical Ind HOT MELT ADHESIVE.
JP2958923B2 (en) * 1990-04-27 1999-10-06 東邦チタニウム株式会社 Solid catalyst components and catalysts for olefin polymerization
US5081090A (en) * 1990-07-23 1992-01-14 Amoco Corporation Dry olefin polymerization catalyst
US5124297A (en) * 1990-12-07 1992-06-23 Amoco Corporation Olefin polymerization and copolymerization catalyst
US5218052A (en) * 1991-02-04 1993-06-08 Amoco Corporation Olefin polymerization and copolymerization process
EP0516458B2 (en) * 1991-05-31 2007-12-19 Mitsui Chemicals, Inc. Olefin polymerization solid catalyst, olefin polymerization catalyst and olefin polymerization
US5182245A (en) * 1991-06-26 1993-01-26 Amoco Corporation Olefin polymerization and copolymerization catalyst
DE69210480T2 (en) * 1991-06-27 1996-11-28 Nippon Oil Co Ltd Catalyst component for olefin polymerization
US5175332A (en) * 1991-12-16 1992-12-29 Dow Corning Corporation Cycloalkoxysilanes
IT1262934B (en) * 1992-01-31 1996-07-22 Montecatini Tecnologie Srl COMPONENTS AND CATALYSTS FOR THE POLYMERIZATION OF OLEFINE
US5587436A (en) * 1992-11-12 1996-12-24 Quantum Chemical Corporation Process for controlling the polymerization of propylene and ethylene and copolymer products
US5346872A (en) * 1993-01-29 1994-09-13 Quantum Chemical Corporation Cocatalyst for vanadium/titanium containing polymerization catalyst
US5459116A (en) * 1993-05-07 1995-10-17 Samsung General Chemicals Co., Ltd. Highly active catalyst for the polymerization of olefins and method for the preparation of the same
US5419116A (en) * 1993-07-02 1995-05-30 The United States Of America As Represented By The Secretary Of The Navy Miniscale ballistic motor testing method for rocket propellants
US5420183A (en) * 1993-07-06 1995-05-30 Hpg International, Inc. Flame retardant polypropylene composition
TW354792B (en) * 1993-08-13 1999-03-21 Mitsui Petrochemical Ind Olefin polymerization catalyst and process for preparing polypropylene and propylene block copolymer
JP3457358B2 (en) * 1993-08-20 2003-10-14 株式会社デンソー Resin composition for distributor cap
DE4332786A1 (en) * 1993-09-27 1995-03-30 Hoechst Ag Process for the production of ultra high molecular weight polyethylene with high bulk density
JPH07126459A (en) * 1993-10-29 1995-05-16 Mitsui Petrochem Ind Ltd Flame-retardant polyolefin composition
JPH07292029A (en) * 1994-04-28 1995-11-07 Toho Titanium Co Ltd Catalyst and method for polymerizing olefin
US5502128A (en) * 1994-12-12 1996-03-26 University Of Massachusetts Group 4 metal amidinate catalysts and addition polymerization process using same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5530739A (en) * 1978-08-25 1980-03-04 Toshiba Corp Automatic transaction unit
JPS5787462A (en) * 1980-11-20 1982-05-31 Kyowa Chem Ind Co Ltd Flame-retardant resin composition containing magnesium oxide with its surface treated

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1362131A4 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101456994B (en) * 2007-12-14 2011-05-11 金发科技股份有限公司 Flame retardant polypropylene resin blend and preparation method thereof
CN110951169A (en) * 2019-12-13 2020-04-03 上海日之升科技有限公司 Light-shading low-linear-expansion-coefficient polypropylene composite material and preparation method thereof
CN110951169B (en) * 2019-12-13 2022-05-10 上海日之升科技有限公司 Light-shading low-linear-expansion-coefficient polypropylene composite material and preparation method thereof

Also Published As

Publication number Publication date
EP1362131A1 (en) 2003-11-19
US7067576B2 (en) 2006-06-27
EP1362131A4 (en) 2005-03-02
CN1220789C (en) 2005-09-28
US20040220312A1 (en) 2004-11-04
JP2004517170A (en) 2004-06-10
CN1479803A (en) 2004-03-03
JP3921448B2 (en) 2007-05-30

Similar Documents

Publication Publication Date Title
EP1907473B1 (en) Flame retardant polymeric compositions
KR101601286B1 (en) Highly flame-resistant polymer composition for electrical wire insulation and electrical wire produced therewith
US20060151758A1 (en) Fire resistant intumescent thermoplastic or thermoset compositions
EP1362131A1 (en) Flame retardant polypropylene resin composition
CN108026339B (en) Flame-retardant resin composition, and metal cable, optical fiber cable and molded article using same
KR100901949B1 (en) Flame retardant polypropylene resin composition with excellent weatherability
KR101696928B1 (en) Modified polyphenylene oxide-polyolefin composition with improved mechanical properties and processability and electrical cable produced therewith
KR100688643B1 (en) Composition for production flame retardant insulating material of halogen free type
GB2190384A (en) Halogen free flame retardant compositions
JPH0745595B2 (en) Halogen-free flame-retardant thermoplastic synthetic resin composition
KR100407723B1 (en) Flame retardent polypropylene resin composition
JP3648032B2 (en) Flame retardant resin composition
JPS5918743A (en) Flame-retardant composition
JP2001151950A (en) Flame-retardant resin composition and molded article thereof
JPS6212005A (en) Flame resisting electric insulator compositioin
JPH06184372A (en) Flame-retardant polypropylene resin composition
JP2001151949A (en) Flame-retardant resin composition and molded article thereof
JPH03197539A (en) Flame-retardant resin composition
KR100702977B1 (en) Polypropylene resin composition with fire retardancy having improved luster and thermal resistance
JPS61252256A (en) Flame-retardant propylene polymer composition
KR100654015B1 (en) Composition and for production flame retardant insulating material of halogen free type which has superior extrusion property
JPH0299540A (en) Frame retardant electrical insulation composition
KR20020077579A (en) Polypropylene resin composition for nondripping extensible fiber
JPS63128041A (en) Flame-retardant resin composition
JPH04253748A (en) Flame-retarding electrical-insulating composition

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CR CU CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
WWE Wipo information: entry into national phase

Ref document number: 2002553535

Country of ref document: JP

Ref document number: 008200866

Country of ref document: CN

WWE Wipo information: entry into national phase

Ref document number: 2000989011

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 10451710

Country of ref document: US

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

WWP Wipo information: published in national office

Ref document number: 2000989011

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 2000989011

Country of ref document: EP

DPE2 Request for preliminary examination filed before expiration of 19th month from priority date (pct application filed from 20040101)