WO2008072792A1 - ポリプロピレン系樹脂組成物 - Google Patents
ポリプロピレン系樹脂組成物 Download PDFInfo
- Publication number
- WO2008072792A1 WO2008072792A1 PCT/JP2007/074601 JP2007074601W WO2008072792A1 WO 2008072792 A1 WO2008072792 A1 WO 2008072792A1 JP 2007074601 W JP2007074601 W JP 2007074601W WO 2008072792 A1 WO2008072792 A1 WO 2008072792A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- resin composition
- ethylene
- polypropylene resin
- random copolymer
- propylene homopolymer
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
- C08L23/0815—Copolymers of ethene with aliphatic 1-olefins
Definitions
- the present invention relates to a polypropylene resin composition. More specifically, the present invention relates to a polypropylene resin composition useful as a material for a molded article having excellent rigidity and impact resistance. '' Background technology
- Molded products made of polypropylene are used in various applications because of their excellent rigidity, heat resistance and surface gloss.
- An object of the present invention is to provide a polypropylene resin composition having excellent rigidity and impact resistance.
- the present invention relates to a propylene homopolymer 60 to 85% by weight and an ethylene- ⁇ -olefin random in which the weight ratio of ethylene to olefin is within the range of 45/5/5 to 70/30.
- Polypropylene resin composition containing 15 to 40% by weight of a copolymer and satisfying the following requirement (1) to the following requirement (5) (however, both the weight percent is the same for the homopolymer and the above) Based on the total amount of copolymer).
- the melting temperature of the propylene homopolymer as measured by DSC is 16 3 ° C or higher and 1700 ° C or lower.
- Requirement (2) l3 C- 2 in the total propylene units of the propylene homopolymer NMR measured by spectrum, 1 over ⁇ and 1, the ratio of different bonds due to 3- ⁇ is 0.0 1% It is as follows.
- Requirement (3) When the amount of ethylene-olefin random copolymer in the polypropylene resin composition is A wt%, and the amount of room temperature xylene soluble in the polypropylene resin composition is B wt% The ratio B / A is 0.9 or more.
- the molecular weight distribution of the ethylene monolithic refin random copolymer is not less than 2.0 and not more than 4.0.
- the propylene homopolymer contained in the polypropylene resin composition of the present invention has a melting temperature measured by differential scanning calorimetry (DSC) in the range of 163 ° C. or higher and 170 ° C. or lower, and 13 C nucleus Propylene whose proportion of heterogeneous bonds due to 2, 1-insertion and 1,3-insertion in all propylene units measured by magnetic resonance (' 3 C-NMR) spectrum is less than 0.01% It is a homopolymer. Also, the room temperature xylene soluble content in the propylene homopolymer is
- the melting temperature of propylene homopolymer measured by DSC is preferably 164 ° C. or higher and 170 or lower, and more preferably 165 ° G or higher and 170 ° C. or lower. If the melting temperature is less than 163 C, the molded article made of the resin composition may have insufficient rigidity.
- the propylene monomer is usually added in 1, 2—, but in rare cases, 1, 1— may be added.
- 1, 2— in which the propylene monomer is usually added.
- 1, 1— in which the propylene monomer is usually added.
- “Proportion of heterogeneous bonds due to 2,1—insertion and 1,3—insertion in all propylene units” of propylene homopolymer is described in Tsutsui et al., POLYMER, 30, 1350 (1989). The proportion of heterogeneous bonds due to 2,1 insertion reactions and the presence of heterogeneous bonds due to 1,3-insertion reactions in polypropylene molecular chains measured by 13 C-NMR spectra based on the proposed method It is the sum of the percentages.
- the proportion of heterogeneous bonds resulting from 2, 1-insertion and 1,3-insertion in all propylene units is 0.01% or less, preferably 0 . 00
- the rigidity may be insufficient when formed into a molded body.
- the polypropylene homopolymer applicable to the present invention is a stereoregular polymerization catalyst comprising a known solid titanium catalyst component, an organometallic compound catalyst component, and an electron donor used as necessary, or a known meta Manufactured by a known polymerization method using a stereoregular polymerization catalyst consisting of a compound that forms a stable anion by reacting with a metal complex and an organoaluminum compound, which is used as necessary. can do.
- Preferred polymerization An example of the catalyst is preferably a catalyst comprising a solid titanium catalyst component, an organometallic compound catalyst component, and an electron donor used as necessary.
- Applicable polymerization methods include slurry polymerization using an inert hydrocarbon solvent such as propane, butane, isobutane, pentane, hexane, heptane and octane, solution polymerization using the solvent, and liquid at the polymerization temperature. Examples thereof include a bulk polymerization method using olefin and a gas phase polymerization method.
- an inert hydrocarbon solvent such as propane, butane, isobutane, pentane, hexane, heptane and octane
- the polymerization is preferably carried out in a temperature range of usually 20 to 100 ° C., particularly preferably 40 to 90 ° C., and a pressure range of normal pressure to 6 MPa.
- the polymerization time may be appropriately determined depending on the kind of the target polymer and the reaction apparatus, and is usually 1 minute to 20 hours.
- a chain transfer agent such as hydrogen may be added to adjust the molecular weight of polypropylene.
- the melt flow rate (hereinafter referred to as MFR) of the propylene homopolymer is preferably 0.1 to 500 g / 10 min, and more preferably 0.3 to 300 gZl 0 min. However, MFR is measured under 230 ° C and 21 N load according to JIS K7210. [Ethylene-a-olefin-random copolymer]
- the ethylene 10; -year-old refin random copolymer contained in the polypropylene-based resin composition of the present invention is obtained by copolymerizing ethylene and ⁇ -year-old refin, and has a structural unit derived from ethylene and ⁇ -olefin. It is a copolymer containing the derived structural unit.
- Ethylene one ⁇ of the present invention - old amount of structural units derived from Les fins contained in the random copolymer "Orefin, i.e., a- O Les fins content as measured by 13 C-NMR spectra 30-55 wt%
- it is 35 to 50% by weight. If the a-olefin content is less than 30% by weight, the compatibility with the propylene homopolymer may not be sufficiently high, and the impact strength may be insufficient due to the formation of polyethylene crystal components. If it exceeds wt%, it may be excessively compatible with the propylene homopolymer, resulting in insufficient rigidity.
- the intrinsic viscosity ([77]) measured in 135 ° C tetralin of the ethylene-a-year-old lefin random copolymer of the present invention is preferably greater than 1.0 dlZg, more preferably Is greater than 1.5 d lZg, particularly preferably greater than 2.0 d lZg.
- the ethylene-a-year-old olefin random copolymer is a polypropylene resin composition comprising a propylene homopolymer and the random copolymer
- the above polypropylene-based polymer measured by a 13 C-NMR spectrum is used.
- the ratio BZA is 0.9 or more, where the amount of ethylene-a-old refin random copolymer in the resin composition is A wt% and the amount of room temperature xylene soluble in the polypropylene resin composition is B wt%. More preferably, it is 0.95 or more.
- this ratio is less than 0.9, random copolymerization of the ethylene-a-year-old refin copolymer
- the impact resistance strength may be inferior when formed into a molded product of a polypropylene resin composition.
- GPC gel permeation chromatography
- AwZA n is the weight average molecular weight measured by GPC.
- Mw is equal to the number average molecular weight (Mn) ratio (Mw / Mn)
- the ratio Mw / Mn is commonly referred to as the "molecular weight distribution" and thus the ratio Aw / A n also means the molecular weight distribution. To do.
- the polypropylene resin composition of the present invention can be subjected to hot press molding for 3 minutes from the composition at a temperature of 190 ° C. and a pressure of 35 kgf Z cm 2 .
- the volume average circle equivalent particle diameter (D) of ethylene monolithic lefin random copolymer particles observed in the cross section (D) is such that v) is 1.0 or less, preferably 0.9 m or less. When 0 is larger than 1.0 m, the impact strength of the polypropylene resin composition may be inferior.
- the ethylene- ⁇ -olefin random copolymer applicable to the present invention is a known solid titanium catalyst component and organometallic compound catalyst component similar to those described in [Propylene Homopolymer]. Or a catalyst comprising a known meta-orthocene complex and an organoaluminum compound, and a compound that reacts with the meta-orthocene complex to form a stable anion. And a method of producing by a known polymerization method. As an example of a preferable polymerization catalyst, a catalyst comprising a meta-octene complex can be mentioned.
- the Dv of the dispersed particles of the ethylene / one-year-old olefin random copolymer contained in the poly'propylene resin composition can be adjusted by melt-kneading the polypropylene resin composition under appropriate conditions. .
- An ethylene-based refin random copolymer applicable to the present invention can be preferably produced by polymerization using a catalyst comprising a metacene complex.
- the polypropylene resin composition of the present invention comprises a propylene homopolymer of 60 to 85 ′% by weight and a polypropylene containing the ethylene- ⁇ -aged refin random copolymer of 15 to 40% by weight. (Both the weight% is based on the total amount of the homopolymer and the copolymer).
- the impact strength is insufficient.
- the propylene homopolymer content is less than 60% by weight (ie, before (If the ethylene-a-year-old refin random copolymer exceeds 40% by weight), the rigidity may be insufficient.
- the content of the propylene homopolymer is preferably 65 to 85% by weight, and the ethylene-a-aged refin random copolymer is preferably 15 to 35% by weight.
- the polypropylene resin composition of the present invention may contain an inorganic filler as necessary. When the inorganic filler is contained, the content is preferably 5 to 20% by weight (however, the total amount of the polypropylene resin composition is 100% by weight).
- the polypropylene resin composition of the present invention includes, as necessary, a heat stabilizer, an aromatic carboxylic acid aluminum salt, an aromatic phosphate ester salt, a nucleating agent such as dibenzylidene sorbitol, an ultraviolet absorber, a lubricant, Antistatic agents, flame retardants, pigments, dyes, phenolic, phenolic, phosphorus-based antioxidants, dispersants, copper damage inhibitors, neutralizing agents, foaming agents, plasticizers, anti-bubble agents, crosslinking agents, Additives such as flowability improvers such as peroxides, light resistance stabilizers and weld strength improvers may be included. Their content is usually from 0.001 to 10 parts by weight based on 100 parts by weight of the polypropylene resin composition of the present invention.
- the composition contains a polymer other than propylene homopolymer and ethylene-a-olefin random copolymer, for example, polyethylene, propylene, as necessary. You may mix
- the blending amount is usually about 5 to 20 parts by weight per 100 parts by weight of the polypropylene resin composition.
- a propylene homopolymer and an ethylene a-year-old refin random copolymer are dissolved and mixed using a substance that dissolves the mixture, and the mixture is mixed with the propylene homopolymer and ethylene one-year-old refin random.
- a method for producing a polypropylene resin composition by putting both of the copolymers into a substance that does not dissolve,
- the method (4) excellent in dispersibility of the ethylene mono-olefin random copolymer in the polypropylene resin composition is preferable.
- Examples of substances that dissolve both propylene homopolymers and ethylene-one-year-old refin random copolymers include high-boiling hydrocarbon compounds represented by tetralin, decalin, toluene, xylene, orthodichlorobenzene, etc. it can.
- Examples of the substance that does not dissolve both the propylene homopolymer and the ethylene- ⁇ -year-old olefin random copolymer include methanol, ethanol, isopropyl alcohol, ptanol, and acetone.
- Applications of the polypropylene resin composition of the present invention include, for example, various automobile materials,. More preferably, it is a polypropylene resin composition in which the above-mentioned filler is contained in the polypropylene resin composition of the present invention as various automobile materials or household electrical appliance materials.
- Propylene homopolymer hot press molding (preheat for 5 minutes at 230 ° C, pressurize to 5 O kgf / cm 2 over 3 minutes, hold pressure for 2 minutes, then 30 ° C, 30 kg i / cm 2 for 5 minutes
- the sheet was 0.5 mm thick.
- a differential scanning calorimeter (TA Instruments, D SC Q 100) 1 Omg of the prepared sheet was heat-treated at 220 ° C for 5 minutes in a nitrogen atmosphere and then cooled to 15 Ot at a cooling rate of 30 OZ.
- a sample was prepared by uniformly dissolving 0 Omg of propylene homopolymer in 3 ml 1 of ortho-diclonal benzene, and the 13 C-NMR spectrum of the sample was measured under the following conditions.
- Pulse repetition time 10 seconds
- Pulse repetition time 10 seconds Pulse width: 45 °
- Xylene 20 OmL was added to 1 g of the polypropylene resin composition, and the mixture was boiled and completely dissolved, then the temperature was lowered, and the condition was adjusted at 20 ° C for 1 hour or longer. Then, it separated into the soluble part and the insoluble part using the filter paper. The solvent was removed from the filtrate to dryness to obtain a soluble part sample, and the weight of the sample was measured to determine the content.
- the weight average molecular chain length (Aw) and the number average molecular chain length (An) were determined under the following conditions, and the ratio (AwZAn) was calculated.
- i is an integer of l to n, and D i is the equivalent-circle diameter of each particle.
- Tensile modulus and tensile impact strength were measured by methods according to ASTM D 1822-L. 190 ° C temperature 190 ° C, pressure 35 kg f / cm 2 , test piece made from 0.5 mm thick press sheet made by hot press molding for 3 minutes, single column type tensile compression tester STA — Measured using 1225 (A & D).
- Catalyst component (A) (Dimethylsilanediylbis (2-methyl-4-mononaphthylindenyl) Zirconium dichloride) 6.6 mg, Triisobutylaluminum toluene adjusted to lmmo 1 ZmL LmL of solution was added.
- the catalyst component (B) (synthesized by the method described in Example 1 (2) of JP-A-2003-171412) was suspended to prepare a toluene slurry of the polymerization catalyst component.
- the catalyst component (C) (dimethylsilylene (tetramethyl (Cyclocyclopentaenyl) (3-tert-petitu 5-methyl-2-phenoxy) titan dimethoxide: metal complex described in Reference Example 1 of JP 2006-193749) 5 mg, concentration 1 mm 0 1 / mL
- a toluene solution was prepared by adding 1 mL of the adjusted triisobutylaluminum toluene solution.
- the mixed gas was continuously fed to the above 3 liter autoclave, and polymerization was carried out for 3 hours at a polymerization pressure of 0.3 MPa and a polymerization temperature of 70 ° C. to obtain 118 g of a polymer.
- the polymer obtained had a olefin (propylene) content of 32 wt% and an intrinsic viscosity of 2.61.
- BCPP-2 a polypropylene resin composition
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/515,135 US8119738B2 (en) | 2006-12-15 | 2007-12-14 | Polypropylene resin composition |
CN2007800464466A CN101558116B (zh) | 2006-12-15 | 2007-12-14 | 聚丙烯树脂组合物 |
DE112007003020.8T DE112007003020B4 (de) | 2006-12-15 | 2007-12-14 | Polypropylenharzzusammensetzung und Formteil umfassend diese |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006338994 | 2006-12-15 | ||
JP2006-338994 | 2006-12-15 |
Publications (1)
Publication Number | Publication Date |
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WO2008072792A1 true WO2008072792A1 (ja) | 2008-06-19 |
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ID=39511792
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2007/074601 WO2008072792A1 (ja) | 2006-12-15 | 2007-12-14 | ポリプロピレン系樹脂組成物 |
Country Status (5)
Country | Link |
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US (1) | US8119738B2 (ja) |
JP (1) | JP5141230B2 (ja) |
CN (1) | CN101558116B (ja) |
DE (1) | DE112007003020B4 (ja) |
WO (1) | WO2008072792A1 (ja) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010076774A (ja) * | 2008-09-24 | 2010-04-08 | Mitsui Chemicals Inc | 食品用シール容器 |
JP2011241284A (ja) * | 2010-05-18 | 2011-12-01 | Sumitomo Chemical Co Ltd | ポリプロピレン系樹脂組成物およびそれを含むフィルム |
DE102012018608A1 (de) * | 2011-09-22 | 2013-03-28 | Sumitomo Chemical Company, Limited | Harzzusammensetzung, Verfahren zur Herstellung derselben und Formgegenstand, der diese verwendet |
CN106596624A (zh) * | 2016-12-21 | 2017-04-26 | 深圳市星源材质科技股份有限公司 | 一种聚烯烃树脂的分级结晶分析方法 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5817139A (ja) * | 1981-07-23 | 1983-02-01 | Sumitomo Chem Co Ltd | 新規なポリプロピレン樹脂組成物 |
JPH08208904A (ja) * | 1995-02-01 | 1996-08-13 | Showa Denko Kk | ポリプロピレン系樹脂組成物およびその製造方法 |
JPH08311271A (ja) * | 1995-05-19 | 1996-11-26 | Nippon Petrochem Co Ltd | ポリプロピレン系樹脂シート |
JPH11293062A (ja) * | 1998-02-10 | 1999-10-26 | Mitsui Chem Inc | ポリプロピレン樹脂組成物および無延伸フィルム |
JPH11291279A (ja) * | 1998-04-06 | 1999-10-26 | Mitsui Chem Inc | ポリプロピレン射出成形体 |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5134209A (en) * | 1990-12-26 | 1992-07-28 | Shell Oil Company | Process of producing ethylene-propylene rubbery copolymer |
EP0534776A1 (en) | 1991-09-27 | 1993-03-31 | Sumitomo Chemical Company, Limited | Block copolymers of ethylene and propylene |
JPH0812827A (ja) * | 1994-06-28 | 1996-01-16 | Ube Ind Ltd | ポリプロピレン組成物 |
JPH09151282A (ja) | 1995-11-28 | 1997-06-10 | Tonen Corp | ポリプロピレン系樹脂組成物 |
JPH1087714A (ja) | 1996-09-13 | 1998-04-07 | Nippon Poriorefuin Kk | プロピレン重合体組成物の製造方法 |
KR100495176B1 (ko) * | 1998-02-10 | 2005-06-14 | 미쓰이 가가쿠 가부시키가이샤 | 폴리프로필렌 수지 조성물 및 그 비연신 필름 |
JP4021042B2 (ja) * | 1998-03-23 | 2007-12-12 | 三菱化学株式会社 | ポリプロピレン樹脂組成物 |
US6469100B2 (en) * | 1998-06-04 | 2002-10-22 | Japan Polychem Corporation | Propylene block copolymer and resin composition |
JPH11349746A (ja) * | 1998-06-04 | 1999-12-21 | Mitsubishi Chemical Corp | 樹脂組成物 |
JP4501872B2 (ja) | 1998-09-09 | 2010-07-14 | 住友化学株式会社 | 変性アルミニウムオキシ化合物、付加重合用触媒成分、付加重合用触媒、オレフィン重合体の製造方法、アルケニル芳香族炭化水素重合体の製造方法、および共重合体 |
JP3937696B2 (ja) | 2000-06-30 | 2007-06-27 | 住友化学株式会社 | ポリプロピレン系樹脂組成物 |
US20020119268A1 (en) * | 2000-12-25 | 2002-08-29 | Shin Gakuji | Air bag housing cover |
JP3960039B2 (ja) | 2000-12-26 | 2007-08-15 | 住友化学株式会社 | 改質された粒子およびその製造方法、担体、付加重合用触媒成分、付加重合用触媒ならびに付加重合体の製造方法 |
JP4705698B2 (ja) | 2001-11-09 | 2011-06-22 | 日本ポリプロ株式会社 | プロピレン系ブロック共重合体 |
JP4903360B2 (ja) | 2002-11-19 | 2012-03-28 | 住友化学株式会社 | プロピレンブロック共重合体製造用固体触媒成分、プロピレンブロック共重合体製造用触媒、およびプロピレンブロック共重合体の製造方法 |
EP1896538B1 (en) * | 2005-06-24 | 2012-05-23 | Dow Global Technologies LLC | Automotive articles prepared from filled tpo compositions, and methods of making the same |
-
2007
- 2007-12-14 JP JP2007323135A patent/JP5141230B2/ja active Active
- 2007-12-14 WO PCT/JP2007/074601 patent/WO2008072792A1/ja active Application Filing
- 2007-12-14 US US12/515,135 patent/US8119738B2/en active Active
- 2007-12-14 DE DE112007003020.8T patent/DE112007003020B4/de active Active
- 2007-12-14 CN CN2007800464466A patent/CN101558116B/zh active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5817139A (ja) * | 1981-07-23 | 1983-02-01 | Sumitomo Chem Co Ltd | 新規なポリプロピレン樹脂組成物 |
JPH08208904A (ja) * | 1995-02-01 | 1996-08-13 | Showa Denko Kk | ポリプロピレン系樹脂組成物およびその製造方法 |
JPH08311271A (ja) * | 1995-05-19 | 1996-11-26 | Nippon Petrochem Co Ltd | ポリプロピレン系樹脂シート |
JPH11293062A (ja) * | 1998-02-10 | 1999-10-26 | Mitsui Chem Inc | ポリプロピレン樹脂組成物および無延伸フィルム |
JPH11291279A (ja) * | 1998-04-06 | 1999-10-26 | Mitsui Chem Inc | ポリプロピレン射出成形体 |
Also Published As
Publication number | Publication date |
---|---|
US20100048822A1 (en) | 2010-02-25 |
CN101558116B (zh) | 2012-02-01 |
US8119738B2 (en) | 2012-02-21 |
JP5141230B2 (ja) | 2013-02-13 |
JP2008169387A (ja) | 2008-07-24 |
CN101558116A (zh) | 2009-10-14 |
DE112007003020T5 (de) | 2009-11-05 |
DE112007003020B4 (de) | 2021-05-12 |
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