WO2000064985A1 - Preparation d'un elastomere thermoplastique de faible durete - Google Patents
Preparation d'un elastomere thermoplastique de faible durete Download PDFInfo
- Publication number
- WO2000064985A1 WO2000064985A1 PCT/NL2000/000177 NL0000177W WO0064985A1 WO 2000064985 A1 WO2000064985 A1 WO 2000064985A1 NL 0000177 W NL0000177 W NL 0000177W WO 0064985 A1 WO0064985 A1 WO 0064985A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- rubber
- oil
- process according
- thermoplastic elastomer
- polar groups
- Prior art date
Links
- 229920002725 thermoplastic elastomer Polymers 0.000 title claims abstract description 24
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 239000005060 rubber Substances 0.000 claims abstract description 65
- 229920001971 elastomer Polymers 0.000 claims abstract description 64
- 238000000034 method Methods 0.000 claims abstract description 42
- 229920001169 thermoplastic Polymers 0.000 claims abstract description 37
- 239000000203 mixture Substances 0.000 claims description 23
- 230000006835 compression Effects 0.000 claims description 11
- 238000007906 compression Methods 0.000 claims description 11
- 229920002943 EPDM rubber Polymers 0.000 claims description 9
- 229920001400 block copolymer Polymers 0.000 claims description 8
- 150000002148 esters Chemical class 0.000 claims description 8
- 229920000728 polyester Polymers 0.000 claims description 7
- 239000004952 Polyamide Substances 0.000 claims description 6
- -1 SIPS Polymers 0.000 claims description 6
- 229920002647 polyamide Polymers 0.000 claims description 6
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 5
- 229920001935 styrene-ethylene-butadiene-styrene Polymers 0.000 claims 2
- 229920006342 thermoplastic vulcanizate Polymers 0.000 description 33
- 239000003921 oil Substances 0.000 description 30
- 238000004073 vulcanization Methods 0.000 description 10
- 239000004416 thermosoftening plastic Substances 0.000 description 9
- 239000004636 vulcanized rubber Substances 0.000 description 7
- 238000002474 experimental method Methods 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 4
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000005062 Polybutadiene Substances 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000005011 phenolic resin Substances 0.000 description 3
- 229920002857 polybutadiene Polymers 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 239000002174 Styrene-butadiene Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000012463 white pigment Substances 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- WSQZNZLOZXSBHA-UHFFFAOYSA-N 3,8-dioxabicyclo[8.2.2]tetradeca-1(12),10,13-triene-2,9-dione Chemical compound O=C1OCCCCOC(=O)C2=CC=C1C=C2 WSQZNZLOZXSBHA-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- OWYWGLHRNBIFJP-UHFFFAOYSA-N Ipazine Chemical compound CCN(CC)C1=NC(Cl)=NC(NC(C)C)=N1 OWYWGLHRNBIFJP-UHFFFAOYSA-N 0.000 description 1
- OKOBUGCCXMIKDM-UHFFFAOYSA-N Irganox 1098 Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)NCCCCCCNC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 OKOBUGCCXMIKDM-UHFFFAOYSA-N 0.000 description 1
- 229920000571 Nylon 11 Polymers 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 239000010692 aromatic oil Substances 0.000 description 1
- 238000000071 blow moulding Methods 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 229920006341 elastomeric alloy Polymers 0.000 description 1
- BXOUVIIITJXIKB-UHFFFAOYSA-N ethene;styrene Chemical group C=C.C=CC1=CC=CC=C1 BXOUVIIITJXIKB-UHFFFAOYSA-N 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920000346 polystyrene-polyisoprene block-polystyrene Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229920006132 styrene block copolymer Polymers 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
- C08L67/025—Polyesters derived from dicarboxylic acids and dihydroxy compounds containing polyether sequences
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/005—Processes for mixing polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L101/00—Compositions of unspecified macromolecular compounds
- C08L101/02—Compositions of unspecified macromolecular compounds characterised by the presence of specified groups, e.g. terminal or pendant functional groups
-
- 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
- C08L23/16—Ethene-propene or ethene-propene-diene copolymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
Definitions
- the invention relates to a process for the preparation of a thermoplastic elastomer containing a thermoplastic polymer with polar groups, a rubber and an oil, m which process the thermoplastic polymer with polar groups is mixed with the rubber and the oil and the rubber is dynamically vulcanized.
- thermoplastic elastomers with dynamically vulcanized rubber are described in the "Handbook of Thermoplastic Elastomers, by B.M. Walker / C.P. Rader, chapter 4, Elastomeric Alloy Thermoplastic Vulcanisates Van Nostrand Remhold, New York 1988".
- thermosettmg material When a rubber is vulcanized in the normal way, a product having the properties of a thermosettmg material is formed.
- thermoplastic elastomers with dynamically vulcanized rubber contain vulcanized rubber, which is dispersed m the form of fine particles m a continuous phase of a thermoplastic polymer.
- TPVs are special in that they have a number of properties of the thermoplastic polymer that forms the continuous phase. Thus, TPVs can be processed as thermoplastics and use can oe made of the customary techniques for shaping and reprocessing.
- an oil is often added to the composition.
- a drawback of the use of oil m a TPV containing a thermoplastic polymer with polar groups is that TPVs are formed in whicn the vulcanized rubber is poorly dispersed. It is even possible for the continuous phase to be formed not by the thermoplastic with polar groups, but by the rubber, so that the advantageous properties of the TPVs as a thermoplastic with respect to processability are lost.
- the object of the present invention is to provide a process for the preparation of a thermoplastic elastomer containing a thermoplastic polymer with polar groups, a rubber and an oil m which the rubber is dynamically vulcanized, that does not have said drawback.
- This object is achieved m that at least a part of the oil is added after the rubber has at least partly vulcanized.
- the process according to tne present invention use can oe made of paraffmic, naphthenic as well as aromatic oils or of mixtures of these oils .
- the total quantity of oil that is present m tne TPV after the process according to the invention has been carried out ranges, for instance, from 0.05 to 2.5 times the quantity of rubber present m the TPV.
- the total quantity of ruiober amounts to between 0.1 and 1.6 times the quantity of rubber present m the TPV.
- the total quantity of oil amounts to between 0.5 and 1.2 times the quantity of rubber present m the TPV.
- the quantity of oil that is added after the rubber has at least partly vulcanized is between 50 and 100% of the total quantity of oil.
- m which 100% of the oil is added after the rubber has at least partly vulcanized.
- thermoplastic polymer with polar groups m the TPVs of the invention use can be made of all known thermoplastic polymers with polar groups. Examples of thermoplastic polymers with polar groups that are suitable for use m the process according to the present invention are: polyamides, polyesters, polyacrylates , polycaroonates and copoly ⁇ ther ester block polymers or mixtures of these polymers .
- a polyamide or a polyester is used as thermoplastic polymer with polar groups.
- polyamides that can be used m the process according to the present invention are: polyamide 6, polyamide 4,6, polyamide 6,6 and polyamide 11.
- polyesters that can be used m the process according to the present invention are . polyethylene terephthalate and polybutylene terephthalate .
- copolyether ester block copolymers with polar groups as thermoplastic polymer with polar groups, or to the use of a mixture of a copolyether ester block copolymer and a polyester.
- TPVs can be prepared that have a very low hardness and a good compression set.
- copolyether ester block copolymers that can be used m the process according to the invention are: copolybutylether butylene terephthalate block copolymer and copoly (1- methyl) ethylether butylene terephthalate block copolymer .
- the quantity of the thermoplastic polymer with polar groups that is used m the process according to the invention ranges from 0.2 to 5.0 times the quantity of rubber present m the TPV.
- the quantity of the thermoplastic polymer with polar groups ranges from 0.5 to 2.0 times the quantity of rubber present m the TPV.
- Use can for instance be ma ⁇ e of the following rubbers or a mixture thereof.
- SBR styrene butadiene rubber, copolymer of styrene and butadiene
- NBR non ⁇ le rubber, copolymer of butadiene and acrylonitrile
- IIR butyl ruboer, copolymer of isobutene and isoprene
- BR butadiene rubber
- SBS styrene butadiene block copolymer
- SEBS styrene ethylene/butadiene styrene block copolymer
- SIPS styrene isoprene block copolymer
- the ⁇ -olefin can for instance be propylene, m these cases the rubber is called EPDM and EPM.
- BR or a mixture of these rubbers is used as rubber m the process according to the invention.
- EPDM rubber or a mixture of EPDM and EPM rubber or a mixture of EPDM, EPM and one or more of the following rubbers: SBS, SEBS and SIPS.
- the TPV prepared according to the process of the invention for instance contains 5 - 250 parts of oil and 20 - 500 parts of thermoplastic polymer with polar groups per 100 parts of rubber.
- the TPV according to the process of the invention contains 10 - 160 parts of oil and 50 - 200 parts of thermoplastic polymer with polar groups per 100 parts of rubber.
- the TPV prepared according to the process of the invention can for instance contain additives.
- sucn additives are fillers, reinforcing agents, dyestuffs, stabilizers and vulcanization agents.
- the TPV prepared according to the process of the invention exists of the thermoplastic polymer with polar groups, the rubber, the oil and the additives.
- the TPV prepared according to the invention substances can for instance be present to increase the compatibility between the rubber and the thermoplastic polymer with polar groups used.
- these substances are maleic anhydride- modified, alkoxy silane-modifled, epoxy-modifled, acid- modified thermoplastic polymers and/or rubbers.
- the dynamic vulcanization of the rubber used m the process according to the invention is carried out m the presence of a vulcanization agent, which is added to the mixture m a quantity known to one skilled m the art.
- vulcanization agent m the dynamic vulcanization use can be made of the vulcanization agents that are known in literature.
- a peroxide, a sulphur compound, a hydrosilane or a phenol resin is used as vulcanization agent .
- At least part of the oil is added after the rubber has at least partly vulcanized.
- tne quantity of vulcanized rubber is for instance between 50 - 100% of the total quantity of rubber present.
- the rubber present is 100% vulcanized.
- the extent to wnich tne rubber is vulcanized at the moment that at least part of the oil is added is determined by measuring the quantity of soluble rubber m boiling xylene.
- the extent to wnicn the rubber is vulcanized is calculated using formula I : B
- B the quantity of rubber dissolved m boiling xylene.
- the process according to the invention can take place using the equipment known from literature for mixing rubbers with thermoplastics and oil m continuous and discontinuous processes.
- the equipment for the process according to the present invention is an extruder or a batch kneader .
- thermoplastic elastomers obtained by the use of the process according to the invention are suitable for all kinds of applications in shaped articles made from thermoplastic elastomers containing a thermoplastic polymer with polar groups, a rubber and an oil.
- thermoplastic elastomers m which a low hardness and a good compression set over a wide temperature range are important .
- thermoplastic elastomer with polar groups By the choice of the thermoplastic elastomer with polar groups to be used, the rubber and the oil and the quantities to be used of the substances, it is ensured that the TPV according to the invention has the material properties that are needed for the application.
- nardness of tne TPV for this application preferably amounts to between 20 Shore A and 40 Shore D. Special preference is given to a TPV of which the hardness amounts to between 30 and 70 Shore A.
- the compression set (ISO 815) of the TPV for this application amounts to between 10 and 50%.
- the compression set (DIN 35517,
- the shaped articles of the applications are made using the customary processing methods such as for instance: extrusion, blow moulding and injection moulding.
- the TPVs according to the invention can be used m applications for the automotive industry, for instance: door profiles, bellows, cable sheathmgs, hoses, air bag covers, dashboard films, handles and soft-touch applications.
- the quantity of oil (Sunpar ® 150) is added according to Table 2.
- This composition is heated and mixed for 2 minutes at 230°C, then a quantity of 10 parts of phenol resin (SP 1045) is added, after which mixing is continued for 5 minutes. As soon as the phenol resin is added, the dynamic vulcanization of the rubber starts.
- thermoplastic elastomer made has a lower hardness and a better compression set m comparison with A.
- thermoplastic polymer that is present forms the continuous phase.
Landscapes
- 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)
Abstract
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU34646/00A AU3464600A (en) | 1999-04-27 | 2000-03-17 | Preparation of a thermoplastic elastomer having a low hardness |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL1011896A NL1011896C2 (nl) | 1999-04-27 | 1999-04-27 | Bereiding van een thermoplastisch elastomeer met lage hardheid. |
NL1011896 | 1999-04-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2000064985A1 true WO2000064985A1 (fr) | 2000-11-02 |
Family
ID=19769089
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NL2000/000177 WO2000064985A1 (fr) | 1999-04-27 | 2000-03-17 | Preparation d'un elastomere thermoplastique de faible durete |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU3464600A (fr) |
NL (1) | NL1011896C2 (fr) |
WO (1) | WO2000064985A1 (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1299662B2 (fr) † | 2000-07-10 | 2009-05-06 | Dichtungstechnik G. Bruss GmbH & Co. KG | Bague d'etancheite |
US8028656B2 (en) | 2002-12-20 | 2011-10-04 | Delaval Holding Ab | Milking devices |
GB2545326A (en) * | 2015-11-11 | 2017-06-14 | Hexcel Composites Ltd | Composite material |
CN110294927A (zh) * | 2018-03-23 | 2019-10-01 | 苏州纳绎博纳米科技有限公司 | 热塑性尼龙弹性体及其制备方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3985702A (en) * | 1975-05-27 | 1976-10-12 | Shell Oil Company | Dry blending and molding process |
US4141863A (en) * | 1976-06-11 | 1979-02-27 | Monsanto Company | Thermoplastic compositions of rubber and polyester |
EP0659824A1 (fr) * | 1993-12-21 | 1995-06-28 | Hüls Aktiengesellschaft | Matériaux composites formés de polyester thermoplastique et d'élastomère thermoplastique de polyester sans couche adhésive |
EP0742268A2 (fr) * | 1995-05-12 | 1996-11-13 | Advanced Elastomer Systems, L.P. | Elastomères thermoplastiques ayant une résistance améliorée aux températures élevées |
-
1999
- 1999-04-27 NL NL1011896A patent/NL1011896C2/nl not_active IP Right Cessation
-
2000
- 2000-03-17 AU AU34646/00A patent/AU3464600A/en not_active Abandoned
- 2000-03-17 WO PCT/NL2000/000177 patent/WO2000064985A1/fr active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3985702A (en) * | 1975-05-27 | 1976-10-12 | Shell Oil Company | Dry blending and molding process |
US4141863A (en) * | 1976-06-11 | 1979-02-27 | Monsanto Company | Thermoplastic compositions of rubber and polyester |
EP0659824A1 (fr) * | 1993-12-21 | 1995-06-28 | Hüls Aktiengesellschaft | Matériaux composites formés de polyester thermoplastique et d'élastomère thermoplastique de polyester sans couche adhésive |
EP0742268A2 (fr) * | 1995-05-12 | 1996-11-13 | Advanced Elastomer Systems, L.P. | Elastomères thermoplastiques ayant une résistance améliorée aux températures élevées |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1299662B2 (fr) † | 2000-07-10 | 2009-05-06 | Dichtungstechnik G. Bruss GmbH & Co. KG | Bague d'etancheite |
US8028656B2 (en) | 2002-12-20 | 2011-10-04 | Delaval Holding Ab | Milking devices |
GB2545326A (en) * | 2015-11-11 | 2017-06-14 | Hexcel Composites Ltd | Composite material |
CN110294927A (zh) * | 2018-03-23 | 2019-10-01 | 苏州纳绎博纳米科技有限公司 | 热塑性尼龙弹性体及其制备方法 |
Also Published As
Publication number | Publication date |
---|---|
AU3464600A (en) | 2000-11-10 |
NL1011896C2 (nl) | 2000-10-30 |
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