CA2741969C - Pvc profiles with high contents of mineral filler and their uses - Google Patents
Pvc profiles with high contents of mineral filler and their uses Download PDFInfo
- Publication number
- CA2741969C CA2741969C CA2741969A CA2741969A CA2741969C CA 2741969 C CA2741969 C CA 2741969C CA 2741969 A CA2741969 A CA 2741969A CA 2741969 A CA2741969 A CA 2741969A CA 2741969 C CA2741969 C CA 2741969C
- Authority
- CA
- Canada
- Prior art keywords
- polyvinyl chloride
- granulate
- naturally occurring
- mineral filler
- chloride polymer
- Prior art date
- Legal status (The legal status 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 status listed.)
- Active
Links
- 239000012764 mineral filler Substances 0.000 title claims abstract description 83
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 177
- 229920000915 polyvinyl chloride Polymers 0.000 claims abstract description 173
- 229920000642 polymer Polymers 0.000 claims abstract description 86
- 239000000203 mixture Substances 0.000 claims description 76
- 239000008187 granular material Substances 0.000 claims description 56
- 239000000454 talc Substances 0.000 claims description 36
- 229910052623 talc Inorganic materials 0.000 claims description 36
- 238000000034 method Methods 0.000 claims description 31
- 238000002156 mixing Methods 0.000 claims description 28
- 239000010445 mica Substances 0.000 claims description 26
- 229910052618 mica group Inorganic materials 0.000 claims description 26
- 230000002787 reinforcement Effects 0.000 claims description 22
- 238000002360 preparation method Methods 0.000 claims description 14
- 238000002844 melting Methods 0.000 claims description 11
- 230000008018 melting Effects 0.000 claims description 11
- 239000010455 vermiculite Substances 0.000 claims description 11
- 229910052902 vermiculite Inorganic materials 0.000 claims description 11
- 235000019354 vermiculite Nutrition 0.000 claims description 11
- 229910052882 wollastonite Inorganic materials 0.000 claims description 11
- 239000010456 wollastonite Substances 0.000 claims description 11
- 239000006057 Non-nutritive feed additive Substances 0.000 claims description 10
- 239000003017 thermal stabilizer Substances 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 3
- 239000002557 mineral fiber Substances 0.000 claims 3
- 239000003381 stabilizer Substances 0.000 description 32
- 238000009472 formulation Methods 0.000 description 27
- 239000000945 filler Substances 0.000 description 18
- 239000000463 material Substances 0.000 description 16
- 150000001875 compounds Chemical class 0.000 description 13
- 239000012760 heat stabilizer Substances 0.000 description 11
- 150000003573 thiols Chemical class 0.000 description 11
- -1 Ca-organic Inorganic materials 0.000 description 10
- 230000008901 benefit Effects 0.000 description 10
- 239000003365 glass fiber Substances 0.000 description 10
- 229910004860 CaZn Inorganic materials 0.000 description 9
- 238000005469 granulation Methods 0.000 description 9
- 230000003179 granulation Effects 0.000 description 9
- 239000000314 lubricant Substances 0.000 description 9
- 238000001125 extrusion Methods 0.000 description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 239000011707 mineral Substances 0.000 description 7
- 230000003014 reinforcing effect Effects 0.000 description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- 235000014113 dietary fatty acids Nutrition 0.000 description 6
- 239000000194 fatty acid Substances 0.000 description 6
- 229930195729 fatty acid Natural products 0.000 description 6
- 239000012745 toughening agent Substances 0.000 description 6
- 239000000654 additive Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000000155 melt Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 4
- 239000004611 light stabiliser Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000000996 additive effect Effects 0.000 description 3
- 159000000007 calcium salts Chemical class 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000007822 coupling agent Substances 0.000 description 3
- 150000004665 fatty acids Chemical class 0.000 description 3
- 239000002657 fibrous material Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 229920002994 synthetic fiber Polymers 0.000 description 3
- 229910052718 tin Inorganic materials 0.000 description 3
- 239000004408 titanium dioxide Substances 0.000 description 3
- 239000001993 wax Substances 0.000 description 3
- 150000003751 zinc Chemical class 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004150 EU approved colour Substances 0.000 description 2
- 241000208202 Linaceae Species 0.000 description 2
- 235000004431 Linum usitatissimum Nutrition 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 229920002522 Wood fibre Polymers 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229920003235 aromatic polyamide Polymers 0.000 description 2
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 229910003455 mixed metal oxide Inorganic materials 0.000 description 2
- 229940006093 opthalmologic coloring agent diagnostic Drugs 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000012763 reinforcing filler Substances 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- HJIAMFHSAAEUKR-UHFFFAOYSA-N (2-hydroxyphenyl)-phenylmethanone Chemical compound OC1=CC=CC=C1C(=O)C1=CC=CC=C1 HJIAMFHSAAEUKR-UHFFFAOYSA-N 0.000 description 1
- BPXVHIRIPLPOPT-UHFFFAOYSA-N 1,3,5-tris(2-hydroxyethyl)-1,3,5-triazinane-2,4,6-trione Chemical compound OCCN1C(=O)N(CCO)C(=O)N(CCO)C1=O BPXVHIRIPLPOPT-UHFFFAOYSA-N 0.000 description 1
- QBWKPGNFQQJGFY-QLFBSQMISA-N 3-[(1r)-1-[(2r,6s)-2,6-dimethylmorpholin-4-yl]ethyl]-n-[6-methyl-3-(1h-pyrazol-4-yl)imidazo[1,2-a]pyrazin-8-yl]-1,2-thiazol-5-amine Chemical compound N1([C@H](C)C2=NSC(NC=3C4=NC=C(N4C=C(C)N=3)C3=CNN=C3)=C2)C[C@H](C)O[C@H](C)C1 QBWKPGNFQQJGFY-QLFBSQMISA-N 0.000 description 1
- LLQHSBBZNDXTIV-UHFFFAOYSA-N 6-[5-[[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]methyl]-4,5-dihydro-1,2-oxazol-3-yl]-3H-1,3-benzoxazol-2-one Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)CC1CC(=NO1)C1=CC2=C(NC(O2)=O)C=C1 LLQHSBBZNDXTIV-UHFFFAOYSA-N 0.000 description 1
- 241001251094 Formica Species 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- IHBCFWWEZXPPLG-UHFFFAOYSA-N [Ca].[Zn] Chemical compound [Ca].[Zn] IHBCFWWEZXPPLG-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- QRUDEWIWKLJBPS-UHFFFAOYSA-N benzotriazole Chemical compound C1=CC=C2N[N][N]C2=C1 QRUDEWIWKLJBPS-UHFFFAOYSA-N 0.000 description 1
- 239000012964 benzotriazole Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229940125846 compound 25 Drugs 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000007033 dehydrochlorination reaction Methods 0.000 description 1
- MQKMBXOZOISLIV-UHFFFAOYSA-N dioctadecyl benzene-1,2-dicarboxylate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCCCCCCCCCCCC MQKMBXOZOISLIV-UHFFFAOYSA-N 0.000 description 1
- YGANSGVIUGARFR-UHFFFAOYSA-N dipotassium dioxosilane oxo(oxoalumanyloxy)alumane oxygen(2-) Chemical compound [O--].[K+].[K+].O=[Si]=O.O=[Al]O[Al]=O YGANSGVIUGARFR-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000007380 fibre production Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 230000010006 flight Effects 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 229910052627 muscovite Inorganic materials 0.000 description 1
- 235000013873 oxidized polyethylene wax Nutrition 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 235000019809 paraffin wax Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 235000019271 petrolatum Nutrition 0.000 description 1
- 229910052615 phyllosilicate Inorganic materials 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000193 polymethacrylate Polymers 0.000 description 1
- 229920002620 polyvinyl fluoride Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 230000002123 temporal effect Effects 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 239000004634 thermosetting polymer Substances 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/625—Screws characterised by the ratio of the threaded length of the screw to its outside diameter [L/D ratio]
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/41—Intermeshing counter-rotating screws
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
The invention relates to a profile made of a reinforced polyvinyl chloride polymer comprising at least 40 weight parts, preferably at least 60 weight parts, most preferably at least 80 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride (PVC), and PVC with a .KAPPA.-value of 50-68.
Description
2 PCT/EP2009/064401 PVC profiles with high contents of mineral filler and their uses Technical field The invention relates to PVC profiles with high contents of naturally occurring mineral filler and their applications.
Background Polyvinyl chloride polymer (PVC) is a synthetic material that can be applied in various industries for its versatile physical and chemical characteristics. There is a demand for reinforced PVC
because sagging or expansion/shrinking of a PVC profile are undesirable in various applications.
EP 0085778 states that generally the best reinforcement materials are fibre structures. Fibre structures that can be used are synthetic fibres (aramid or carbon fibres), mineral fibres (glass fibre) or natural fibres (flax, wood fibres). The use of synthetic fibres leads to a substantial increase in the cost of raw materials which make a PVC profile thus reinforced not economically attractive. Mineral fibres should be avoided also for health reasons related to inhaling glass fibre dust. A disadvantage of natural fibres, like for example flax or wood, is their variability in composition and, consequently, their fluctuating quality. They are sensitive to humidity and consequently they can rot and mould, even when incorporated into a PVC
profile. A further disadvantage of synthetic or natural fibres is that they significantly hamper the processing of PVC.
In US2007/0078191 PVC was reinforced by means of increased quantities of glass fibre. The use of large quantities of glass fibre is disadvantageous. Glass fibres are very abrasive, and do significant damage to metal machine parts. As a consequence, repair and replacements must be carried out frequently. Damaging the die needed for the production of PVC
profiles, will cause loss of dimensional stability and increased rejection percentages.
Glass fibre reinforced profiles, produced by means of a pultrusion technique, whereby thermosetting polymer and reinforcing fibres are made into a profile, have the disadvantage that the joining between the fibre and the polymer is often insufficient and coupling agents must be used. Moreover the material cannot be recycled. Furthermore the raw material cost and the cost for equipment is high.
Consequently there is a need for new PVC profiles. The purpose of this disclosure is to at least partially solve the problems mentioned above.
Summary The disclosure provides PVC profiles with high naturally occurring mineral filler content and a description of their use.
In a first aspect, there is provided a granulate or profile made of a reinforced polyvinyl chloride polymer comprising at least 40 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride (PVC), and PVC with a K-value of 50-68, wherein the reinforced polyvinyl chloride polymer has a flexural modulus of at least 5 GPa, and wherein the naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
In a second aspect, there is provided a granulate or profile made of a reinforced polyvinyl chloride polymer composition, the reinforced polyvinyl chloride polymer composition comprising more than 80 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition has a flexural modulus of at least 5 GPa, and wherein the naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
In a third aspect, there is provided a granulate or profile made of a reinforced polyvinyl chloride polymer composition, the reinforced polyvinyl chloride polymer composition comprising more than 60 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition exhibits a coefficient of linear thermal expansion that is lower than 25 x 10-6 / K, and wherein the naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
- 2a -In a fourth aspect, there is provided a method for obtaining a granulate or a profile described herein, comprising the steps of: a) preparation of a pre-reinforced polymer by mixing polyvinyl chloride polymer with a quantity A of a naturally occurring mineral filler at a temperature lower than the melting temperature of the polyvinyl chloride polymer, b) mixing the pre-reinforced polymer obtained under a) with a quantity B of a naturally occurring mineral filler at a temperature higher than 180 C to obtain a reinforced polyvinyl chloride polymer, c) optionally granulating the reinforced polyvinyl chloride polymer obtained in step b), d) pressing the reinforced polymer obtained in step b) or the granulate obtained in step c) through a die to obtain said granulate or profile; wherein said naturally occurring mineral filler is selected from the list consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof; and wherein the ratio of the quantity A of naturally occurring mineral filler to the quantity B of naturally occurring mineral filler is at least 0.1.
In a fifth aspect, there is provided a granulate in steps of the method above.
Possible usages of these PVC profiles will be described in a further aspect.
This disclosure therefore also provides use of a granulate or profile described herein as a reinforcement element, preferably in a window-frame or fencing. The disclosure also provides use of a granulate or profile described herein, wherein the profile is fastened with nails or screws.
In order to better show the characteristics of the invention, an illustration of some preferred embodiments, but not limiting in nature, will be described below.
Description As used herein, the singular forms "a", "an", and "the" include both singular and plural referents unless the context clearly dictates otherwise.
The terms "comprising", "comprises" and "comprised of" as used herein are synonymous with "including", "includes" or "containing", "contains", and are inclusive or open-ended and do not exclude additional, non-recited members, elements or method steps.
The terms "comprising", "comprises" and "comprised of" also include the term "consisting of".
Background Polyvinyl chloride polymer (PVC) is a synthetic material that can be applied in various industries for its versatile physical and chemical characteristics. There is a demand for reinforced PVC
because sagging or expansion/shrinking of a PVC profile are undesirable in various applications.
EP 0085778 states that generally the best reinforcement materials are fibre structures. Fibre structures that can be used are synthetic fibres (aramid or carbon fibres), mineral fibres (glass fibre) or natural fibres (flax, wood fibres). The use of synthetic fibres leads to a substantial increase in the cost of raw materials which make a PVC profile thus reinforced not economically attractive. Mineral fibres should be avoided also for health reasons related to inhaling glass fibre dust. A disadvantage of natural fibres, like for example flax or wood, is their variability in composition and, consequently, their fluctuating quality. They are sensitive to humidity and consequently they can rot and mould, even when incorporated into a PVC
profile. A further disadvantage of synthetic or natural fibres is that they significantly hamper the processing of PVC.
In US2007/0078191 PVC was reinforced by means of increased quantities of glass fibre. The use of large quantities of glass fibre is disadvantageous. Glass fibres are very abrasive, and do significant damage to metal machine parts. As a consequence, repair and replacements must be carried out frequently. Damaging the die needed for the production of PVC
profiles, will cause loss of dimensional stability and increased rejection percentages.
Glass fibre reinforced profiles, produced by means of a pultrusion technique, whereby thermosetting polymer and reinforcing fibres are made into a profile, have the disadvantage that the joining between the fibre and the polymer is often insufficient and coupling agents must be used. Moreover the material cannot be recycled. Furthermore the raw material cost and the cost for equipment is high.
Consequently there is a need for new PVC profiles. The purpose of this disclosure is to at least partially solve the problems mentioned above.
Summary The disclosure provides PVC profiles with high naturally occurring mineral filler content and a description of their use.
In a first aspect, there is provided a granulate or profile made of a reinforced polyvinyl chloride polymer comprising at least 40 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride (PVC), and PVC with a K-value of 50-68, wherein the reinforced polyvinyl chloride polymer has a flexural modulus of at least 5 GPa, and wherein the naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
In a second aspect, there is provided a granulate or profile made of a reinforced polyvinyl chloride polymer composition, the reinforced polyvinyl chloride polymer composition comprising more than 80 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition has a flexural modulus of at least 5 GPa, and wherein the naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
In a third aspect, there is provided a granulate or profile made of a reinforced polyvinyl chloride polymer composition, the reinforced polyvinyl chloride polymer composition comprising more than 60 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition exhibits a coefficient of linear thermal expansion that is lower than 25 x 10-6 / K, and wherein the naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
- 2a -In a fourth aspect, there is provided a method for obtaining a granulate or a profile described herein, comprising the steps of: a) preparation of a pre-reinforced polymer by mixing polyvinyl chloride polymer with a quantity A of a naturally occurring mineral filler at a temperature lower than the melting temperature of the polyvinyl chloride polymer, b) mixing the pre-reinforced polymer obtained under a) with a quantity B of a naturally occurring mineral filler at a temperature higher than 180 C to obtain a reinforced polyvinyl chloride polymer, c) optionally granulating the reinforced polyvinyl chloride polymer obtained in step b), d) pressing the reinforced polymer obtained in step b) or the granulate obtained in step c) through a die to obtain said granulate or profile; wherein said naturally occurring mineral filler is selected from the list consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof; and wherein the ratio of the quantity A of naturally occurring mineral filler to the quantity B of naturally occurring mineral filler is at least 0.1.
In a fifth aspect, there is provided a granulate in steps of the method above.
Possible usages of these PVC profiles will be described in a further aspect.
This disclosure therefore also provides use of a granulate or profile described herein as a reinforcement element, preferably in a window-frame or fencing. The disclosure also provides use of a granulate or profile described herein, wherein the profile is fastened with nails or screws.
In order to better show the characteristics of the invention, an illustration of some preferred embodiments, but not limiting in nature, will be described below.
Description As used herein, the singular forms "a", "an", and "the" include both singular and plural referents unless the context clearly dictates otherwise.
The terms "comprising", "comprises" and "comprised of" as used herein are synonymous with "including", "includes" or "containing", "contains", and are inclusive or open-ended and do not exclude additional, non-recited members, elements or method steps.
The terms "comprising", "comprises" and "comprised of" also include the term "consisting of".
- 3 -The recitation of numerical ranges by endpoints includes all numbers and fractions subsumed within the respective ranges, as well as the recited endpoints.
The term "about'' as used herein when referring to a measurable value such as a parameter, an amount, a temporal duration, and the like, is meant to encompass variations of +/-10% or less, preferably +/-5% or less, more preferably +/-1 % or less, and still more preferably +/-0.1 % or less of and from the specified value, insofar such variations are appropriate to perform in the disclosed invention. It is to be understood that the value to which the modifier "about" refers is itself also specifically, and preferably, disclosed.
Generally it is assumed that in order to obtain reinforced PVC, fibrous materials must be used as a reinforcement material. In the current invention the term "fibrous materials" means glass fibres, aramid fibres, carbon fibres and/or combinations thereof. The quantity of reinforcing material is increased, in order to increase the reinforcement level. However, mixing and handling problems arise with high quantities of reinforcing fibres; compositions are no longer sufficiently homogeneous which negatively affects the mechanical performance, and PVC
profiles show bulging fibre materials on the surface.
The inventors have been able to make reinforced PVC profiles, exclusively based on naturally occurring mineral filler. By the term "naturally occurring mineral filler" it is meant a filler which can be found in nature and except for a milling step can be used without the need for a manufacturing process. The denomination mineral indicates an element or chemical compound that is normally crystalline and that has been formed as a result of geological processes. Glass fibre production requires a manufacturing process, is not naturally occurring as it is produced from 5i02. Wood fibres are not mineral.
In the current invention, "naturally occurring mineral filler" particularly means wollastonite, vermiculite, talc, mica and/or combinations thereof. In a preferred embodiment of the invention, the naturally occurring mineral filler in a profile is selected from a group including wollastonite, vermiculite, talc, mica, and/or combinations thereof. In a preferred embodiment of the invention, the naturally occurring mineral filler in a profile is talc and/or mica. If a stiff profile is desired, mica will have the preference. If a profile is desired with a reduced coefficient of linear thermal expansion, talc is most advantageous.
The term "about'' as used herein when referring to a measurable value such as a parameter, an amount, a temporal duration, and the like, is meant to encompass variations of +/-10% or less, preferably +/-5% or less, more preferably +/-1 % or less, and still more preferably +/-0.1 % or less of and from the specified value, insofar such variations are appropriate to perform in the disclosed invention. It is to be understood that the value to which the modifier "about" refers is itself also specifically, and preferably, disclosed.
Generally it is assumed that in order to obtain reinforced PVC, fibrous materials must be used as a reinforcement material. In the current invention the term "fibrous materials" means glass fibres, aramid fibres, carbon fibres and/or combinations thereof. The quantity of reinforcing material is increased, in order to increase the reinforcement level. However, mixing and handling problems arise with high quantities of reinforcing fibres; compositions are no longer sufficiently homogeneous which negatively affects the mechanical performance, and PVC
profiles show bulging fibre materials on the surface.
The inventors have been able to make reinforced PVC profiles, exclusively based on naturally occurring mineral filler. By the term "naturally occurring mineral filler" it is meant a filler which can be found in nature and except for a milling step can be used without the need for a manufacturing process. The denomination mineral indicates an element or chemical compound that is normally crystalline and that has been formed as a result of geological processes. Glass fibre production requires a manufacturing process, is not naturally occurring as it is produced from 5i02. Wood fibres are not mineral.
In the current invention, "naturally occurring mineral filler" particularly means wollastonite, vermiculite, talc, mica and/or combinations thereof. In a preferred embodiment of the invention, the naturally occurring mineral filler in a profile is selected from a group including wollastonite, vermiculite, talc, mica, and/or combinations thereof. In a preferred embodiment of the invention, the naturally occurring mineral filler in a profile is talc and/or mica. If a stiff profile is desired, mica will have the preference. If a profile is desired with a reduced coefficient of linear thermal expansion, talc is most advantageous.
- 4 -In doing so, they were not hampered by mixing problems. The quality of highly filled PVC
profiles was good. In this current invention, the term "highly filled" means high contents of naturally occurring mineral filler. A PVC profile is highly filled from the moment in which at least 25 weight parts of naturally occurring mineral filler are used per 100 weight parts of polyvinyl chloride. This is also expressed with the term "phr", which means "parts per hundred resins".
In a preferred embodiment, profiles are made of a reinforced polyvinyl chloride polymer comprising at least 60 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride (PVC). More preferably PVC profiles contain at least 80 weight parts, most preferably at least 100 weight parts of filler mineral. The possibility of replacing reinforcing fibrous materials with reinforcing naturally occurring mineral filler has the advantage that the price of PVC profiles can be kept down, not only by saving on raw materials, but also by saving on repair and replacement costs and by reducing the percentage of rejected products. When large quantities of fibres are used, binding problems often arise and coupling agents must be applied. The invention has the advantage that no coupling agents have to be added. The reinforced PVC profiles show a smooth surface.
In a preferred embodiment, PVC with a K-value between 50 to 68 is used. The "K-value" of a polymer is a measure of the molecular weight and it is based on the inherent viscosity. A K-value between 50 and 68 corresponds to an average molecular weight of about g/mol. In a more preferred embodiment, the polyvinyl chloride polymer has a K-value between 60 and 68. In a most preferred embodiment according to the invention, the PVC
has a K-value between 64 and 68. A K-value of 65 is advantageous because of its good workability and mechanical characteristics. PVC can be obtained commercially in the form of powder. The PVC
can also be applied in the form of scrap. By the term "scrap" recyclable PVC-based materials are meant that are the result of starting up or shutting down extrusion lines, or PVC-based materials that are out-of-specification. In a preferred embodiment, a method comprises extruding a formulation comprising at least 10 weight% scrap.
Consequently, the invention provides PVC profiles, with the characteristic that at least 40 weight parts, preferably 60 weight parts of reinforcing filler are used per 100 weight parts of PVC, more preferably at least 80 weight parts, most preferably at least 100 weight parts, and the PVC
preferably has a K-value between 50 and 68, more preferably between 60 and 68, most
profiles was good. In this current invention, the term "highly filled" means high contents of naturally occurring mineral filler. A PVC profile is highly filled from the moment in which at least 25 weight parts of naturally occurring mineral filler are used per 100 weight parts of polyvinyl chloride. This is also expressed with the term "phr", which means "parts per hundred resins".
In a preferred embodiment, profiles are made of a reinforced polyvinyl chloride polymer comprising at least 60 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride (PVC). More preferably PVC profiles contain at least 80 weight parts, most preferably at least 100 weight parts of filler mineral. The possibility of replacing reinforcing fibrous materials with reinforcing naturally occurring mineral filler has the advantage that the price of PVC profiles can be kept down, not only by saving on raw materials, but also by saving on repair and replacement costs and by reducing the percentage of rejected products. When large quantities of fibres are used, binding problems often arise and coupling agents must be applied. The invention has the advantage that no coupling agents have to be added. The reinforced PVC profiles show a smooth surface.
In a preferred embodiment, PVC with a K-value between 50 to 68 is used. The "K-value" of a polymer is a measure of the molecular weight and it is based on the inherent viscosity. A K-value between 50 and 68 corresponds to an average molecular weight of about g/mol. In a more preferred embodiment, the polyvinyl chloride polymer has a K-value between 60 and 68. In a most preferred embodiment according to the invention, the PVC
has a K-value between 64 and 68. A K-value of 65 is advantageous because of its good workability and mechanical characteristics. PVC can be obtained commercially in the form of powder. The PVC
can also be applied in the form of scrap. By the term "scrap" recyclable PVC-based materials are meant that are the result of starting up or shutting down extrusion lines, or PVC-based materials that are out-of-specification. In a preferred embodiment, a method comprises extruding a formulation comprising at least 10 weight% scrap.
Consequently, the invention provides PVC profiles, with the characteristic that at least 40 weight parts, preferably 60 weight parts of reinforcing filler are used per 100 weight parts of PVC, more preferably at least 80 weight parts, most preferably at least 100 weight parts, and the PVC
preferably has a K-value between 50 and 68, more preferably between 60 and 68, most
- 5 -preferably between 64 and 68, typically 65. In a preferred embodiment of the invention profiles are made of reinforced polyvinyl chloride polymer with a K-value between 64 and 68.
In a preferred embodiment, the naturally occurring mineral filler is talc and/or mica. Talc is a hydrated magnesium silicate, which has the following chemical structure formula:
Mg3Si4010(OH)2. For its application, it is ground to a powder with an average particle size between 0.5 pm and 20 pm. It is commercially available. Mica should preferably be of the muscovite kind, this is a phyllosilicate mineral, with the following chemical structure formula:
KAl2(AlSi3)010(OH,F)2. To apply it, it is ground to a powder with an average grain size between 0.5 pm and 40 pm. It is commercially available. These minerals typically provide the PVC
profiles with an improved fire resistance, a decreased coefficient of linear thermal expansion (CLTE) and a higher stiffness. This is an interesting characteristic when used for building components. Therefore, the invention provides PVC profiles, wherein the naturally occurring mineral filler is talc and/or mica. In an embodiment, the naturally occurring mineral filler is talc and/or mica with an average grain size between 0.5 and 40 pm.
In a preferred embodiment, the naturally occurring mineral filler is talc and/or mica with an average grain size between 0.5 and 5 pm. In a more preferred embodiment, the naturally occurring mineral filler is talc and/or mica with an average grain size between 0.5 and 3 pm for talc and between 30 and 35 pm for mica. Preferably the grains have an elongated shape and are platelets. Average grain size of a naturally occurring mineral filler may be determined by measuring techniques known to a person skilled in the art. For example, the method as described in ISO 13320.
Due to the large quantities of naturally occurring mineral filler, PVC
profiles made according to the embodiments of the invention are less flexible and not easily breakable. A
profile according to a preferred embodiment has a flexural modulus of at least 5 GPa. A more preferred embodiment has a flexural modulus of at least 8 GPa. The most preferred embodiment has a flexural modulus of at least 10 GPa. By the term "flexural modulus" it is meant the flexural modulus of elasticity, also defined as the ratio of flexural stress over flexural strain. The flexural modulus of a material can be measured by techniques known to a person skilled in the art, for instance according to ISO 178.
The advantage of an improved flexural modulus is that PVC profiles can be used in applications where profiles must have large dimensions. Because of their increased stiffness they will sag
In a preferred embodiment, the naturally occurring mineral filler is talc and/or mica. Talc is a hydrated magnesium silicate, which has the following chemical structure formula:
Mg3Si4010(OH)2. For its application, it is ground to a powder with an average particle size between 0.5 pm and 20 pm. It is commercially available. Mica should preferably be of the muscovite kind, this is a phyllosilicate mineral, with the following chemical structure formula:
KAl2(AlSi3)010(OH,F)2. To apply it, it is ground to a powder with an average grain size between 0.5 pm and 40 pm. It is commercially available. These minerals typically provide the PVC
profiles with an improved fire resistance, a decreased coefficient of linear thermal expansion (CLTE) and a higher stiffness. This is an interesting characteristic when used for building components. Therefore, the invention provides PVC profiles, wherein the naturally occurring mineral filler is talc and/or mica. In an embodiment, the naturally occurring mineral filler is talc and/or mica with an average grain size between 0.5 and 40 pm.
In a preferred embodiment, the naturally occurring mineral filler is talc and/or mica with an average grain size between 0.5 and 5 pm. In a more preferred embodiment, the naturally occurring mineral filler is talc and/or mica with an average grain size between 0.5 and 3 pm for talc and between 30 and 35 pm for mica. Preferably the grains have an elongated shape and are platelets. Average grain size of a naturally occurring mineral filler may be determined by measuring techniques known to a person skilled in the art. For example, the method as described in ISO 13320.
Due to the large quantities of naturally occurring mineral filler, PVC
profiles made according to the embodiments of the invention are less flexible and not easily breakable. A
profile according to a preferred embodiment has a flexural modulus of at least 5 GPa. A more preferred embodiment has a flexural modulus of at least 8 GPa. The most preferred embodiment has a flexural modulus of at least 10 GPa. By the term "flexural modulus" it is meant the flexural modulus of elasticity, also defined as the ratio of flexural stress over flexural strain. The flexural modulus of a material can be measured by techniques known to a person skilled in the art, for instance according to ISO 178.
The advantage of an improved flexural modulus is that PVC profiles can be used in applications where profiles must have large dimensions. Because of their increased stiffness they will sag
- 6 -less easily. This is useful in applications where metal reinforcements are currently applied. For example, this is the case for profiles for (sliding) doors and windows.
Therefore, the invention provides PVC profiles with a flexural modulus of at least 5 GPa, more preferably at least 8 GPa, most preferably at least 10 GPa.
In a preferred embodiment, a profile has a coefficient of linear thermal expansion (CLTE) lower than 25 x 10-6 mm/mm/K. In a more preferred embodiment, a profile has a coefficient of linear thermal expansion lower than 20 x 10-6 mm/mm/K. In a most preferred embodiment, a profile has a coefficient of linear thermal expansion lower than 15 x 10-6 mm/mm/K.
The term "coefficient of linear thermal expansion" describes by how much a material will expand for each incremental change in temperature, as given by the formula:
d:f = ______ where:
di = the change in length of material in the direction being measured /0 = initial length of material in the direction being measured dT = the change in temperature over which dl is measured Coefficients of linear thermal expansion can be measured by techniques known to a person skilled in the art. Coefficients of linear thermal expansion may for instance be determined with a silica dilatometer according to ASTM D 696 or ISO 11359. This characteristic of reduced linear thermal expansion has the advantage of profiles being less subject to shrinking and expansion when exposed to different temperatures. This is advantageous in applications where high dimensional stability is required and where the profiles are exposed to weather conditions, for example windows, doors, gates, fences, siding or decking. They are suitable for replacing reinforcement elements made of steel (CLTE = 13 x 10-6 mm/mm/K) or aluminium (CLTE = 22 x 10-6 mm/mm/K) Consequently the invention provides PVC profiles, with a coefficient of linear thermal expansion preferably lower than 25 x 10-6 mm/mm/K, more preferably lower than 20 x 10-6 mm/mm/K, most preferably lower than 15 x 10-6 mm/mm/K.
In a preferred embodiment, a profile according to the invention is provided with hollow cavities.
Profiles thus provided with chambers are light and easily transportable.
In a preferred embodiment, a profile is made with raw material obtained by means of two mixing steps; each mixing step involves the mixing of PVC with a naturally occurring mineral filler and a
Therefore, the invention provides PVC profiles with a flexural modulus of at least 5 GPa, more preferably at least 8 GPa, most preferably at least 10 GPa.
In a preferred embodiment, a profile has a coefficient of linear thermal expansion (CLTE) lower than 25 x 10-6 mm/mm/K. In a more preferred embodiment, a profile has a coefficient of linear thermal expansion lower than 20 x 10-6 mm/mm/K. In a most preferred embodiment, a profile has a coefficient of linear thermal expansion lower than 15 x 10-6 mm/mm/K.
The term "coefficient of linear thermal expansion" describes by how much a material will expand for each incremental change in temperature, as given by the formula:
d:f = ______ where:
di = the change in length of material in the direction being measured /0 = initial length of material in the direction being measured dT = the change in temperature over which dl is measured Coefficients of linear thermal expansion can be measured by techniques known to a person skilled in the art. Coefficients of linear thermal expansion may for instance be determined with a silica dilatometer according to ASTM D 696 or ISO 11359. This characteristic of reduced linear thermal expansion has the advantage of profiles being less subject to shrinking and expansion when exposed to different temperatures. This is advantageous in applications where high dimensional stability is required and where the profiles are exposed to weather conditions, for example windows, doors, gates, fences, siding or decking. They are suitable for replacing reinforcement elements made of steel (CLTE = 13 x 10-6 mm/mm/K) or aluminium (CLTE = 22 x 10-6 mm/mm/K) Consequently the invention provides PVC profiles, with a coefficient of linear thermal expansion preferably lower than 25 x 10-6 mm/mm/K, more preferably lower than 20 x 10-6 mm/mm/K, most preferably lower than 15 x 10-6 mm/mm/K.
In a preferred embodiment, a profile according to the invention is provided with hollow cavities.
Profiles thus provided with chambers are light and easily transportable.
In a preferred embodiment, a profile is made with raw material obtained by means of two mixing steps; each mixing step involves the mixing of PVC with a naturally occurring mineral filler and a
- 7 -temperature treatment. The mixing steps that are taken into consideration are classical preparation steps, like compounding, granulating and extruding. More information about these preparations can be found in textbooks, like for example PVC Handbook, Eds.
Charles E.
Wilkes, James W. Summers, and Charles A. Daniels, published by Hanser Gardner, 2005. The advantage of this preparation is that the homogeneity of a formulation will be preserved, so that problems like segregation and loss of quality are reduced. Therefore, the invention provides profiles wherein the raw material for the profile is obtained by means of two mixing steps for mixing the PVC with the naturally occurring mineral filler. Preferably the naturally occurring mineral filler is talc and/or mica. More preferably the naturally occurring mineral filler is talc.
Most preferably the naturally occurring mineral filler is talc with an average grain size between 0.5 and 40 pm.
In a preferred embodiment, a preparation includes a first mixing step a) where a pre-reinforced polymer is formed by mixing a quantity A of naturally occurring mineral filler with PVC at a temperature lower than the PVC melting temperature. Contrary to other substances, polyvinylchloride does not have one well-determined melting temperature but rather a melting range going from 130 C to 240 C. A "temperature lower than the melting temperature" of a polyvinylchloride polymer, means a temperature lower than 130 C.
During a second mixing step b), the pre-reinforced polymer obtained in step a) is mixed with a quantity B of a naturally occurring mineral filler at a temperature higher than 180 C. The temperature higher than 180 C should preferably be 185 C, more preferably 190 C, even more preferably 195 C, most preferably 200 C. In a preferred embodiment according to the invention, a PVC profile is obtained by extruding in step b), at a temperature of preferably 185 C, more preferably of 190 C, even more preferably of 195 C and most preferably of 200 C.
The filler used in step a) can differ from the one applied in step b). The advantage of this preparation is that the quantity of filler in a formulation can be increased without compromising the workability. The resulting profiles are of good quality. For example, the profiles show a smooth and homogeneous surface, without parts of filler protruding on the surface. Therefore, the invention provides profiles having the characteristic that during their preparation, in the first mixing phase a quantity A of the naturally occurring mineral filler is mixed with PVC at a temperature lower than the PVC melting temperature; and that during the second mixing phase a quantity B of the naturally occurring mineral filler is mixed with the first mixture, at a temperature higher than 180 C.
Charles E.
Wilkes, James W. Summers, and Charles A. Daniels, published by Hanser Gardner, 2005. The advantage of this preparation is that the homogeneity of a formulation will be preserved, so that problems like segregation and loss of quality are reduced. Therefore, the invention provides profiles wherein the raw material for the profile is obtained by means of two mixing steps for mixing the PVC with the naturally occurring mineral filler. Preferably the naturally occurring mineral filler is talc and/or mica. More preferably the naturally occurring mineral filler is talc.
Most preferably the naturally occurring mineral filler is talc with an average grain size between 0.5 and 40 pm.
In a preferred embodiment, a preparation includes a first mixing step a) where a pre-reinforced polymer is formed by mixing a quantity A of naturally occurring mineral filler with PVC at a temperature lower than the PVC melting temperature. Contrary to other substances, polyvinylchloride does not have one well-determined melting temperature but rather a melting range going from 130 C to 240 C. A "temperature lower than the melting temperature" of a polyvinylchloride polymer, means a temperature lower than 130 C.
During a second mixing step b), the pre-reinforced polymer obtained in step a) is mixed with a quantity B of a naturally occurring mineral filler at a temperature higher than 180 C. The temperature higher than 180 C should preferably be 185 C, more preferably 190 C, even more preferably 195 C, most preferably 200 C. In a preferred embodiment according to the invention, a PVC profile is obtained by extruding in step b), at a temperature of preferably 185 C, more preferably of 190 C, even more preferably of 195 C and most preferably of 200 C.
The filler used in step a) can differ from the one applied in step b). The advantage of this preparation is that the quantity of filler in a formulation can be increased without compromising the workability. The resulting profiles are of good quality. For example, the profiles show a smooth and homogeneous surface, without parts of filler protruding on the surface. Therefore, the invention provides profiles having the characteristic that during their preparation, in the first mixing phase a quantity A of the naturally occurring mineral filler is mixed with PVC at a temperature lower than the PVC melting temperature; and that during the second mixing phase a quantity B of the naturally occurring mineral filler is mixed with the first mixture, at a temperature higher than 180 C.
- 8 -In a preferred embodiment, a method for obtaining a profile according to the invention comprises the steps of:
a) preparation of a pre-reinforced polymer by mixing polyvinyl chloride polymer with a quantity A
of a naturally occurring mineral filler at a temperature lower than the melting temperature of the polyvinyl chloride polymer, b) mixing the pre-reinforced polymer obtained under a) with a quantity B of a naturally occurring mineral filler at a temperature higher than 180 C to obtain a reinforced polyvinyl chloride polymer, c) optionally granulating the reinforced polyvinyl chloride polymer obtained in step b), d) pressing the reinforced polymer obtained in step b) or the granulate obtained in step c) through a die to obtain said profile.
In a preferred embodiment the quantity A of a naturally occurring mineral filler used in a method to obtain a profile according to the invention is between 0-2 phr, between 2-25 phr, or between 25-40 per hundred parts of polyvinyl chloride polymer (phr). In a production environment where the processing equipment is in close proximity of the mixer, a quantity A
between 25-40 phr is advantageous, since there is little transport and thus little risk for segregation. For situations with an average requirement for transportation, a quantity A between 2-25 phr is advantageous.
With excellent feeders, the quantity A can be decreased to between 0-2 phr. In a preferred embodiment, a highly filled compound is formed by using at least 25 weight parts of naturally occurring mineral filler, during the first step.
The ratio of a quantity A of a filler to a quantity B of a filler is at least 0.1, preferably at least 0.2, more preferably at least 0.25, most preferably at least 0.3. If this ratio is used when preparing the feed for the extruder, then this will show an almost optimal flow and compressibility. This is unexpected, since it is known that it is hard for highly filled compositions to flow through the feed throat into a cylinder of an extruder and that they do not flow fast enough to fill the first screw flights. This leads to inefficient mixing and a bad quality of the final product. It is also known that a highly filled composition has a very high compressibility.
Consequently, the screw of an extruder can compress the filler only to a limited extent, which is insufficient to prompt the required friction needed for the material to melt. Because of this, a powder or only a sintered product comes out of the extruder, instead of a proper melt. Therefore, the invention provides PVC profiles, with the characteristic that the ratio of A over B is at least 0.1, preferably at least 0.2, more preferably at least 0.25, most preferably 0.3. In a preferred embodiment, the ratio of A
a) preparation of a pre-reinforced polymer by mixing polyvinyl chloride polymer with a quantity A
of a naturally occurring mineral filler at a temperature lower than the melting temperature of the polyvinyl chloride polymer, b) mixing the pre-reinforced polymer obtained under a) with a quantity B of a naturally occurring mineral filler at a temperature higher than 180 C to obtain a reinforced polyvinyl chloride polymer, c) optionally granulating the reinforced polyvinyl chloride polymer obtained in step b), d) pressing the reinforced polymer obtained in step b) or the granulate obtained in step c) through a die to obtain said profile.
In a preferred embodiment the quantity A of a naturally occurring mineral filler used in a method to obtain a profile according to the invention is between 0-2 phr, between 2-25 phr, or between 25-40 per hundred parts of polyvinyl chloride polymer (phr). In a production environment where the processing equipment is in close proximity of the mixer, a quantity A
between 25-40 phr is advantageous, since there is little transport and thus little risk for segregation. For situations with an average requirement for transportation, a quantity A between 2-25 phr is advantageous.
With excellent feeders, the quantity A can be decreased to between 0-2 phr. In a preferred embodiment, a highly filled compound is formed by using at least 25 weight parts of naturally occurring mineral filler, during the first step.
The ratio of a quantity A of a filler to a quantity B of a filler is at least 0.1, preferably at least 0.2, more preferably at least 0.25, most preferably at least 0.3. If this ratio is used when preparing the feed for the extruder, then this will show an almost optimal flow and compressibility. This is unexpected, since it is known that it is hard for highly filled compositions to flow through the feed throat into a cylinder of an extruder and that they do not flow fast enough to fill the first screw flights. This leads to inefficient mixing and a bad quality of the final product. It is also known that a highly filled composition has a very high compressibility.
Consequently, the screw of an extruder can compress the filler only to a limited extent, which is insufficient to prompt the required friction needed for the material to melt. Because of this, a powder or only a sintered product comes out of the extruder, instead of a proper melt. Therefore, the invention provides PVC profiles, with the characteristic that the ratio of A over B is at least 0.1, preferably at least 0.2, more preferably at least 0.25, most preferably 0.3. In a preferred embodiment, the ratio of A
- 9 -over B in a method for the preparation of a profile according to the invention is at least 0.1, preferably at least 0.2, more preferably at least 0.25, most preferably at least 0.3.
In a preferred embodiment the total quantity of filler expressed in weight%, amounts up to 70 weight % of the reinforced polyvinyl chloride polymer. The deployability of larger quantities of filler offers more possibilities for giving direction to the characteristics of the product, for example the reduction of the coefficient of linear thermal expansion or the increase of the flexural modulus.
In a preferred embodiment, the total number of filler parts (A+B) with regards to the number of polyvinyl chloride polymer parts, is preferably between 0.4 and 2.5, more preferably between 0.6 and 1.5, most preferably between 0.8 and 1.2. In a preferred embodiment, the total quantity of naturally occurring mineral filler (A+B) with regards to the quantity of polyvinyl chloride polymer is preferably between 0.4 (about 30 weight% naturally occurring mineral filler / 70 weight% PVC) and 2.5 (about 70 weight% naturally occurring mineral filler! 30 weight% PVC), more preferably between 0.6 and 1.5, most preferably between 0.8 and 1.2. The advantage of this proportion is that there will be enough polymer in relation to the filler, to achieve complete melting and mixing in an extruder, the consequence of which will be a homogeneous mixture.
In a preferred embodiment the total quantity of naturally occurring mineral filler (A+B) to the quantity of polyvinyl chloride polymer in a method for the preparation of a profile according to the invention, is preferably between 0.4 and 2.5, more preferably between 0.6 and 1.5, most preferably between 0.8 and 1.2.
In a preferred embodiment, a PVC profile contains at least one additive, selected from a group comprising heat stabilizers, lubricants, processing aids, toughening agents, foaming agents, light stabilizers and colouring agents. In a preferred embodiment according to the invention, a formulation comprises a heat stabilizer, a lubricant and a processing aid and requires no further additives.
In a preferred embodiment, a heat stabilizer is selected from a group of stabilizers of the CaZn, Ca-organic, Sn, or Pb type. The CaZn types are calcium-zinc systems based on calcium and zinc salts of fatty acids in combination with costabilizers. The Ca-organic types are stabilizers based on the calcium salt of fatty acids in combination with costabilizers. Sn types are stabilizers based on organic stannous compounds. The Pb types are stabilizers based on
In a preferred embodiment the total quantity of filler expressed in weight%, amounts up to 70 weight % of the reinforced polyvinyl chloride polymer. The deployability of larger quantities of filler offers more possibilities for giving direction to the characteristics of the product, for example the reduction of the coefficient of linear thermal expansion or the increase of the flexural modulus.
In a preferred embodiment, the total number of filler parts (A+B) with regards to the number of polyvinyl chloride polymer parts, is preferably between 0.4 and 2.5, more preferably between 0.6 and 1.5, most preferably between 0.8 and 1.2. In a preferred embodiment, the total quantity of naturally occurring mineral filler (A+B) with regards to the quantity of polyvinyl chloride polymer is preferably between 0.4 (about 30 weight% naturally occurring mineral filler / 70 weight% PVC) and 2.5 (about 70 weight% naturally occurring mineral filler! 30 weight% PVC), more preferably between 0.6 and 1.5, most preferably between 0.8 and 1.2. The advantage of this proportion is that there will be enough polymer in relation to the filler, to achieve complete melting and mixing in an extruder, the consequence of which will be a homogeneous mixture.
In a preferred embodiment the total quantity of naturally occurring mineral filler (A+B) to the quantity of polyvinyl chloride polymer in a method for the preparation of a profile according to the invention, is preferably between 0.4 and 2.5, more preferably between 0.6 and 1.5, most preferably between 0.8 and 1.2.
In a preferred embodiment, a PVC profile contains at least one additive, selected from a group comprising heat stabilizers, lubricants, processing aids, toughening agents, foaming agents, light stabilizers and colouring agents. In a preferred embodiment according to the invention, a formulation comprises a heat stabilizer, a lubricant and a processing aid and requires no further additives.
In a preferred embodiment, a heat stabilizer is selected from a group of stabilizers of the CaZn, Ca-organic, Sn, or Pb type. The CaZn types are calcium-zinc systems based on calcium and zinc salts of fatty acids in combination with costabilizers. The Ca-organic types are stabilizers based on the calcium salt of fatty acids in combination with costabilizers. Sn types are stabilizers based on organic stannous compounds. The Pb types are stabilizers based on
- 10 -(in)organic lead salts. A heat stabilizer ensures the delay of the dehydrochlorination process of polyvinyl chloride and it prevents the polyvinyl chloride from burning during a thermal treatment, like an extrusion. For applications in Europe there is a preference for CaZn and Ca-organic stabilizers, whereas for applications in North America Sn stabilizers are preferred. The reasons for this are historic. North America has always preferred Sn stabilizers, whereas Europe has always preferred Pb stabilizers. Since Pb stabilizers will disappear (at the latest in 2015) the preference in Europe goes to CaZn and Ca-organic.
In another preferred embodiment, a heat stabilizer is of the blocked thiol type. By the term "blocked thiol" it is meant a thiol of formula B-S-R wherein B and R represent an organic portion. Blocked thiol and organic-based heat stabilizer are used interchangeably. An organic-based heat stabilizer comprises a zinc salt, and at least one sulphur compound selected from the group consisting of a free mercaptan, a zinc mercaptide, and a latent mercaptan. Preferably the organic-based heat stabilizer is an organic-based composition comprising at least one organic-based heat stabilizer component, and at least one stabilizer modifying component selected from the group consisting of liquid calcium soap and 1,3,5-tris (2-hydroxyethyl) cyanuric acid; wherein the organic-based heat stabilizer component comprises a zinc salt and at least one sulfur compound selected from the group consisting of a free mercaptan, a zinc mercaptide, and a latent mercaptan; and wherein the liquid calcium salt is a solution of a calcium salt which is liquid at 105 C and is free from other metal salts.
Use of a blocked thiol type stabilizer system is advantageous as it is essentially free of heavy metals and harmful bisphenol A co-stabilizer. It is an environmentally friendly type of stabilizer.
A further advantage is that this type of stabilizer boosts recyclability. PVC
stabilized with a blocked thiol type heat stabilizer is compatible with other stabilizing systems such as the CaZn, Ca-organic, Sn, or Pb type stabilizers. It can be safely combined with recycled PVC. It provides good colour stability in PVC profiles. In an embodiment of the invention, a profile comprises an organic based thermal stabilizer. In a further embodiment of the invention, a profile comprising up to 10 weight%, preferably up to 25 weight % recycled PVC, comprises a blocked thiol type stabilizer.
In a preferred embodiment, the total quantity of stabilizers in a formulation is between 1 and 4 weight%, more preferably between 2 and 4 weight%, most preferably between 3 and 4 weight%. In a more preferred embodiment of the invention, the total quantity of stabilizers in a formulation is maximum 1.5 weight% in case Sn type stabilizers are used, 5 weight% when Pb
In another preferred embodiment, a heat stabilizer is of the blocked thiol type. By the term "blocked thiol" it is meant a thiol of formula B-S-R wherein B and R represent an organic portion. Blocked thiol and organic-based heat stabilizer are used interchangeably. An organic-based heat stabilizer comprises a zinc salt, and at least one sulphur compound selected from the group consisting of a free mercaptan, a zinc mercaptide, and a latent mercaptan. Preferably the organic-based heat stabilizer is an organic-based composition comprising at least one organic-based heat stabilizer component, and at least one stabilizer modifying component selected from the group consisting of liquid calcium soap and 1,3,5-tris (2-hydroxyethyl) cyanuric acid; wherein the organic-based heat stabilizer component comprises a zinc salt and at least one sulfur compound selected from the group consisting of a free mercaptan, a zinc mercaptide, and a latent mercaptan; and wherein the liquid calcium salt is a solution of a calcium salt which is liquid at 105 C and is free from other metal salts.
Use of a blocked thiol type stabilizer system is advantageous as it is essentially free of heavy metals and harmful bisphenol A co-stabilizer. It is an environmentally friendly type of stabilizer.
A further advantage is that this type of stabilizer boosts recyclability. PVC
stabilized with a blocked thiol type heat stabilizer is compatible with other stabilizing systems such as the CaZn, Ca-organic, Sn, or Pb type stabilizers. It can be safely combined with recycled PVC. It provides good colour stability in PVC profiles. In an embodiment of the invention, a profile comprises an organic based thermal stabilizer. In a further embodiment of the invention, a profile comprising up to 10 weight%, preferably up to 25 weight % recycled PVC, comprises a blocked thiol type stabilizer.
In a preferred embodiment, the total quantity of stabilizers in a formulation is between 1 and 4 weight%, more preferably between 2 and 4 weight%, most preferably between 3 and 4 weight%. In a more preferred embodiment of the invention, the total quantity of stabilizers in a formulation is maximum 1.5 weight% in case Sn type stabilizers are used, 5 weight% when Pb
- 11 -type stabilizers are used, 2-4 weight% when using CaZn or Ca-organic type stabilizers, 4 weight% when a blocked thiol type is used.
In a preferred embodiment, a method for obtaining a profile according to the invention further comprises the step of adding a thermal stabilizer in a quantity of between 0 and 5 weight%;
preferably between 1 and 4 weight%; most preferably around 4 weight%, wherein said thermal stabilizer is preferably a blocked thiol type stabilizer.
An additive can also be a lubricant, for example to improve the flow of the polymer melt in the extruder. In a preferred embodiment, a lubricant is selected from a group comprising polyethylene waxes, oxidized polyethylene waxes, paraffin waxes, fatty acid ester waxes (for example distearyl phthalate), fatty acids salts (for example calcium stearate), fatty acids, fatty acids alcohols, amine waxes and/or their combinations. In a preferred embodiment, the total quantity of lubricants in a formulation is between 0 and 2 weight%, more preferably between 1 and 2 weight%, most preferably between 1.5 and 2 weight%.
In a preferred embodiment, a processing aid is selected from a group comprising methacrylate copolymers, acrylate copolymers, methacrylate terpolymers, acrylate terpolymers and/or a combination thereof. In a preferred embodiment, the total quantity of processing aid in a formulation is between 0 and 15 weight%, more preferably between 5 and 15 weight%, most preferably between 10 and 15 weight%. This use supports, for example, the processability of a polymer by promoting fusion, improving melting strength, changing the surface characteristics, ensuring an improved release of a melt from metal parts.
In a preferred embodiment a method for obtaining a profile according to the invention further comprises the step of adding a processing aid in a quantity of between 0 and 15 weight%;
preferably between 5 and 15 weight%.
In order to improve the impact resistance of a PVC profile, a toughening agent can be added. In a preferred embodiment, the total quantity of toughening agents in a formulation is between 0 and 5 weight%, more preferably between 1 and 5 weight%, most preferably between 2 and 5 weight %.
A light stabilizer can be added in order to slow down the PVC degradation due to exposure to light. In a preferred embodiment, a light stabilizer is selected from a group comprising a
In a preferred embodiment, a method for obtaining a profile according to the invention further comprises the step of adding a thermal stabilizer in a quantity of between 0 and 5 weight%;
preferably between 1 and 4 weight%; most preferably around 4 weight%, wherein said thermal stabilizer is preferably a blocked thiol type stabilizer.
An additive can also be a lubricant, for example to improve the flow of the polymer melt in the extruder. In a preferred embodiment, a lubricant is selected from a group comprising polyethylene waxes, oxidized polyethylene waxes, paraffin waxes, fatty acid ester waxes (for example distearyl phthalate), fatty acids salts (for example calcium stearate), fatty acids, fatty acids alcohols, amine waxes and/or their combinations. In a preferred embodiment, the total quantity of lubricants in a formulation is between 0 and 2 weight%, more preferably between 1 and 2 weight%, most preferably between 1.5 and 2 weight%.
In a preferred embodiment, a processing aid is selected from a group comprising methacrylate copolymers, acrylate copolymers, methacrylate terpolymers, acrylate terpolymers and/or a combination thereof. In a preferred embodiment, the total quantity of processing aid in a formulation is between 0 and 15 weight%, more preferably between 5 and 15 weight%, most preferably between 10 and 15 weight%. This use supports, for example, the processability of a polymer by promoting fusion, improving melting strength, changing the surface characteristics, ensuring an improved release of a melt from metal parts.
In a preferred embodiment a method for obtaining a profile according to the invention further comprises the step of adding a processing aid in a quantity of between 0 and 15 weight%;
preferably between 5 and 15 weight%.
In order to improve the impact resistance of a PVC profile, a toughening agent can be added. In a preferred embodiment, the total quantity of toughening agents in a formulation is between 0 and 5 weight%, more preferably between 1 and 5 weight%, most preferably between 2 and 5 weight %.
A light stabilizer can be added in order to slow down the PVC degradation due to exposure to light. In a preferred embodiment, a light stabilizer is selected from a group comprising a
- 12 -stabilizer of the titanium dioxide type, of the benzotriazole type, or of the hydroxybenzophenone type and/or combinations thereof. Titanium dioxide is used in a more preferred embodiment according to the invention. In the most preferred embodiment, the total quantity of light stabilizers in a formulation is preferably between 0 and 10 weight%, more preferably between 8 and 4 weight%, most preferably between 4 and 6 weight%.
A profile according to the invention can be fit with a covering layer or cap.
The material for the cap layer is selected from a group comprising poly((meth))acrylate), poly(butyl acrylate-styrene-acrylonitrile), polyvinylidene fluoride, polyvinyl fluoride, poly(styrene-acrylonitrile), a light proof polyvinyl chloride material and/or a combination thereof. In a preferred embodiment according to the invention, the total quantity of additive for the covering layer in a formulation is preferably between 0 and 6 weight%, more preferably between 0 and 4 weight%, most preferably between 0 and 2 weight%.
If the final application becomes a visible part, so if no cap is extruded over a PVC profile, then a PVC profile can be coloured with a colouring agent. In a preferred embodiment, a colouring agent will be selected from among a group comprising metal salt, metal oxide, mixed-metal oxide and/or combinations thereof. In a more preferred embodiment, a mixed-metal oxide is used. This shows the most favourable ageing behaviour. In a preferred embodiment, the total quantity of colouring agents in a formulation is between 0 and 5 weight%, more preferably between 1 and 4 weight%, most preferably between 2 and 3 weight%.
In a further aspect, the invention provides a reinforced polyvinylchloride polymer based on a formulation comprising:
- polyvinylchloride polymer in a quantity preferably between 30 and 70 weight%, more preferably between 35 and 70 weight%, most preferably between 40 and 70 weight% of the formulation;
- filler in a quantity preferably between 30 and 70 weight%, more preferably between 35 and 70 weight%, most preferably between 40 and 70 weight% of the formulation.
In an embodiment of the invention, a reinforced polyvinylchloride polymer is based on a formulation comprising:
- polyvinylchloride polymer in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation; and
A profile according to the invention can be fit with a covering layer or cap.
The material for the cap layer is selected from a group comprising poly((meth))acrylate), poly(butyl acrylate-styrene-acrylonitrile), polyvinylidene fluoride, polyvinyl fluoride, poly(styrene-acrylonitrile), a light proof polyvinyl chloride material and/or a combination thereof. In a preferred embodiment according to the invention, the total quantity of additive for the covering layer in a formulation is preferably between 0 and 6 weight%, more preferably between 0 and 4 weight%, most preferably between 0 and 2 weight%.
If the final application becomes a visible part, so if no cap is extruded over a PVC profile, then a PVC profile can be coloured with a colouring agent. In a preferred embodiment, a colouring agent will be selected from among a group comprising metal salt, metal oxide, mixed-metal oxide and/or combinations thereof. In a more preferred embodiment, a mixed-metal oxide is used. This shows the most favourable ageing behaviour. In a preferred embodiment, the total quantity of colouring agents in a formulation is between 0 and 5 weight%, more preferably between 1 and 4 weight%, most preferably between 2 and 3 weight%.
In a further aspect, the invention provides a reinforced polyvinylchloride polymer based on a formulation comprising:
- polyvinylchloride polymer in a quantity preferably between 30 and 70 weight%, more preferably between 35 and 70 weight%, most preferably between 40 and 70 weight% of the formulation;
- filler in a quantity preferably between 30 and 70 weight%, more preferably between 35 and 70 weight%, most preferably between 40 and 70 weight% of the formulation.
In an embodiment of the invention, a reinforced polyvinylchloride polymer is based on a formulation comprising:
- polyvinylchloride polymer in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation; and
-13-- a naturally occurring mineral filler in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation.
In an embodiment of the invention, a reinforced polyvinylchloride polymer is based on a formulation comprising:
- polyvinylchloride polymer in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation; and - a naturally occurring mineral filler in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation; whereby said filler is talc and/or mica, preferably talc.
A polyvinyl chloride polymer based on a formulation according to a preferred embodiment of the invention has increased filler contents. This highly filled polyvinylchloride polymers are more reinforced, have increased fire resistant characteristics, increased rigidity and increased stiffness.
In a further aspect, the invention provides a granulate or profile obtained according to a method as previously described. Another further aspect of the invention discusses the uses of the PVC
profiles.
According to an embodiment of the invention, profiles are preferably used as reinforcing elements. Reinforcing elements are applied as a reinforcement for PVC profiles having large dimensions, for example (sliding) windows, doors, gates, fences or other railings. Typically, steel and aluminium reinforcement elements are used for this. A reinforcement element according to an embodiment of the invention can be a profile, one or more strips or co-extrudate. In the first case, in order to produce a strengthened PVC profile, a traditional PVC
profile is made with a chamber and a reinforced polyvinyl chloride reinforcement element. The reinforcement element is slid into the chamber. It can be attached, for example, with screws and/or glue. The reinforcement element can be integrated in a PVC profile during the production of a PVC profile, preferably by means of a (co)extrusion. In doing so, a part of the profile will consist in a profile according to the invention, for example through a (co)extrusion. A
(co)extrudate can take the shape of one or more strips. The use of a reinforcement element according to the invention as a replacement of a metal reinforcement element has the advantage of providing an improved insulation value. A conductive material, like a metal, is after all replaced with a much less conductive material. This can be important in windows or other
In an embodiment of the invention, a reinforced polyvinylchloride polymer is based on a formulation comprising:
- polyvinylchloride polymer in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation; and - a naturally occurring mineral filler in a quantity of at least 30 weight%, preferably at least 35 weight%, more preferably at least 40 weight%, most preferably at least 45 weight% of the formulation; whereby said filler is talc and/or mica, preferably talc.
A polyvinyl chloride polymer based on a formulation according to a preferred embodiment of the invention has increased filler contents. This highly filled polyvinylchloride polymers are more reinforced, have increased fire resistant characteristics, increased rigidity and increased stiffness.
In a further aspect, the invention provides a granulate or profile obtained according to a method as previously described. Another further aspect of the invention discusses the uses of the PVC
profiles.
According to an embodiment of the invention, profiles are preferably used as reinforcing elements. Reinforcing elements are applied as a reinforcement for PVC profiles having large dimensions, for example (sliding) windows, doors, gates, fences or other railings. Typically, steel and aluminium reinforcement elements are used for this. A reinforcement element according to an embodiment of the invention can be a profile, one or more strips or co-extrudate. In the first case, in order to produce a strengthened PVC profile, a traditional PVC
profile is made with a chamber and a reinforced polyvinyl chloride reinforcement element. The reinforcement element is slid into the chamber. It can be attached, for example, with screws and/or glue. The reinforcement element can be integrated in a PVC profile during the production of a PVC profile, preferably by means of a (co)extrusion. In doing so, a part of the profile will consist in a profile according to the invention, for example through a (co)extrusion. A
(co)extrudate can take the shape of one or more strips. The use of a reinforcement element according to the invention as a replacement of a metal reinforcement element has the advantage of providing an improved insulation value. A conductive material, like a metal, is after all replaced with a much less conductive material. This can be important in windows or other
- 14 -building materials, in order to be able to comply with stricter insulation norms. The use of a PVC
reinforcement element also has the advantage that a lighter construction is obtained without a reduction of the strength. This allows an easier manipulation and installation. Therefore, the invention provides a use of a profile according to a preferred embodiment as a reinforcement element, preferably in window frames or fencing.
PVC profiles according to a preferred embodiment of the invention are applied for decking floors. It is a sturdy, light and well insulating material. PVC profiles according to a preferred embodiment of the invention are recyclable.
PVC profiles according to a preferred embodiment of the invention have a good workability.
They can be shaped with standard carpenter tools like a saw or a drill. They can be nailed or attached without cracking or splintering the profile. Screws can be driven into the profiles of the invention. A profile according to a preferred embodiment of the invention can serve as a basis for suspended structures and closures (fittings). Therefore the invention provides use of a profile according to a preferred embodiment wherein the reinforcement element is used as basis for a suspended structure or closure such as a fitting. In another preferred embodiment the invention provides the use of a profile of the invention, wherein said profile is fastened with nails or screws.
It is obvious that the description of this invention can be related to alternative embodiments within its scope. The invention is illustrated based on the following non-limiting examples.
PVC Profiles Examples 1-8 Profiles according to a preferred embodiment of the invention, can be based on compositions like those represented in Table 1, under Example 1-7. The term "phr", the way it is used in this invention, means "parts per hundred resins". Upon using this unit, 100 parts of polyvinyl chloride polymer are adopted, and the quantity of other ingredients is expressed in relation to this 100 parts of polyvinyl chloride polymer.
To produce a batch quantity of 100 kg, the following quantities were put in a hot-mixer, of the Periplast brand, having a volume of 150 litres: 100 parts of polyvinyl chloride polymer, 3.5 parts of CaZn stabilizer or 1.5 parts of Sn stabilizer or 4.0 parts of blocked thiol type stabilizer, 1.9 parts of lubricants, 8 or 10 parts of processing aid, 5 or 6 parts of toughening agent and 25 parts
reinforcement element also has the advantage that a lighter construction is obtained without a reduction of the strength. This allows an easier manipulation and installation. Therefore, the invention provides a use of a profile according to a preferred embodiment as a reinforcement element, preferably in window frames or fencing.
PVC profiles according to a preferred embodiment of the invention are applied for decking floors. It is a sturdy, light and well insulating material. PVC profiles according to a preferred embodiment of the invention are recyclable.
PVC profiles according to a preferred embodiment of the invention have a good workability.
They can be shaped with standard carpenter tools like a saw or a drill. They can be nailed or attached without cracking or splintering the profile. Screws can be driven into the profiles of the invention. A profile according to a preferred embodiment of the invention can serve as a basis for suspended structures and closures (fittings). Therefore the invention provides use of a profile according to a preferred embodiment wherein the reinforcement element is used as basis for a suspended structure or closure such as a fitting. In another preferred embodiment the invention provides the use of a profile of the invention, wherein said profile is fastened with nails or screws.
It is obvious that the description of this invention can be related to alternative embodiments within its scope. The invention is illustrated based on the following non-limiting examples.
PVC Profiles Examples 1-8 Profiles according to a preferred embodiment of the invention, can be based on compositions like those represented in Table 1, under Example 1-7. The term "phr", the way it is used in this invention, means "parts per hundred resins". Upon using this unit, 100 parts of polyvinyl chloride polymer are adopted, and the quantity of other ingredients is expressed in relation to this 100 parts of polyvinyl chloride polymer.
To produce a batch quantity of 100 kg, the following quantities were put in a hot-mixer, of the Periplast brand, having a volume of 150 litres: 100 parts of polyvinyl chloride polymer, 3.5 parts of CaZn stabilizer or 1.5 parts of Sn stabilizer or 4.0 parts of blocked thiol type stabilizer, 1.9 parts of lubricants, 8 or 10 parts of processing aid, 5 or 6 parts of toughening agent and 25 parts
- 15 -of talc. The ingredients were mixed by means of a stirrer with a blade tip speed of 38 m/s. The mantle temperature was 80 C. Upon reaching the temperature of 120 C, the mixture was discharged into a cold-mixer of the Periplast brand, with a volume of 800 litres. The mixture was stirred with a blade tip speed of 6 m/s. In order to cool the mixture, the wall temperature was set at 10 C with cooling fluid. The mixture was cooled down until a discharge temperature of 40 C
was reached.
Table 1: Compositions for producing PVC profiles according to the invention (Examples 1-7) and according to prior art (Example 8) Example 1 2 3 4 Formulation (phr) (phr) (phr) (phr) PVC K-value 65 100 100 100 100 CaZn stabilizer 3.5 3.5 3.5 3.5 Sn stabilizer Lubricant 1.9 1.9 1.9 1.9 Processing aid 8 8 8 8 Toughening agent 6 6 6 6 Talc (d50 = 1.9 pm) 25 + 85 (*) 25 + 75 (*) Mica (d50 = 33 pm) 25 + 75 (*) 25 +
75 (*) (*) 25 phr added in the hot-mixer, + x parts added on the extruder Example 5 6 7 8 Formulation (phr) (phr) (phr) (phr) PVC K-value 65 100 100 100 100 CaZn stabilizer Sn stabilizer 1.5 1.5 1 Blocked thiol type stabilizer 4.0 Lubricant 1.9 1.9 1.9 1.9 Processing aid 10 10 8 10 Toughening agent 5 5 6 5 Talc (d50 = 1.9 pm) 25 + 75 (*) 25 + 75 (*) Mica (d50 = 33 pm) 25 + 75 (*) Glass fibre 25 +
75 (*) (*) 25 phr added in the hot-mixer, + x parts added on the extruder Examples 9-11
was reached.
Table 1: Compositions for producing PVC profiles according to the invention (Examples 1-7) and according to prior art (Example 8) Example 1 2 3 4 Formulation (phr) (phr) (phr) (phr) PVC K-value 65 100 100 100 100 CaZn stabilizer 3.5 3.5 3.5 3.5 Sn stabilizer Lubricant 1.9 1.9 1.9 1.9 Processing aid 8 8 8 8 Toughening agent 6 6 6 6 Talc (d50 = 1.9 pm) 25 + 85 (*) 25 + 75 (*) Mica (d50 = 33 pm) 25 + 75 (*) 25 +
75 (*) (*) 25 phr added in the hot-mixer, + x parts added on the extruder Example 5 6 7 8 Formulation (phr) (phr) (phr) (phr) PVC K-value 65 100 100 100 100 CaZn stabilizer Sn stabilizer 1.5 1.5 1 Blocked thiol type stabilizer 4.0 Lubricant 1.9 1.9 1.9 1.9 Processing aid 10 10 8 10 Toughening agent 5 5 6 5 Talc (d50 = 1.9 pm) 25 + 75 (*) 25 + 75 (*) Mica (d50 = 33 pm) 25 + 75 (*) Glass fibre 25 +
75 (*) (*) 25 phr added in the hot-mixer, + x parts added on the extruder Examples 9-11
- 16 -The pre-reinforced polymer obtained in this way, was brought into a dosing unit of a counter-rotating parallel double-screw extruder of the Bandera brand and was processed into granules or was directly transformed into a profile with the assistance of a shaping die.
A typical method for granulation is reproduced in Table 2. In total 100 phr of naturally occurring mineral filler were used; 25 phr in the first method step (described above) and 75 phr in the second step. Product streams were led to a reciprocating single-screw extruder of the Buss PR-46 brand, with a throughput of 26 and 14 kg per hour respectively, from a first dosing unit filled with a compound comprising 25 phr of naturally occurring mineral filler and a second dosing unit filled with naturally occurring mineral filler. Each product stream was brought onto the screw of the extruder through a separate feed throat. The kneader and the extruder were operated with the settings represented in Table 2.
Table 2: Example of a typical granulation method Example 9 Type Reciprocating single-screw extruder Brand Buss PR-46 Dosing unit Dosing unit 1 (compound) 26 kg/h Dosing unit 2 (naturally occurring 14 kg/h mineral filler ) Naturally occurring mineral filler 25 phr quantity in compound Additionally dosed naturally occurring 75 phr mineral filler Dose method Each stream through a separate feed throat Kneader Screw diameter 46 mm Screw length 11D (*) Temperature kneader zone 1 190 C
Temperature kneader zone 2 190 C
Screw temperature 13000 Screw speed 216 rpm Extruder Screw diameter 70 mm
A typical method for granulation is reproduced in Table 2. In total 100 phr of naturally occurring mineral filler were used; 25 phr in the first method step (described above) and 75 phr in the second step. Product streams were led to a reciprocating single-screw extruder of the Buss PR-46 brand, with a throughput of 26 and 14 kg per hour respectively, from a first dosing unit filled with a compound comprising 25 phr of naturally occurring mineral filler and a second dosing unit filled with naturally occurring mineral filler. Each product stream was brought onto the screw of the extruder through a separate feed throat. The kneader and the extruder were operated with the settings represented in Table 2.
Table 2: Example of a typical granulation method Example 9 Type Reciprocating single-screw extruder Brand Buss PR-46 Dosing unit Dosing unit 1 (compound) 26 kg/h Dosing unit 2 (naturally occurring 14 kg/h mineral filler ) Naturally occurring mineral filler 25 phr quantity in compound Additionally dosed naturally occurring 75 phr mineral filler Dose method Each stream through a separate feed throat Kneader Screw diameter 46 mm Screw length 11D (*) Temperature kneader zone 1 190 C
Temperature kneader zone 2 190 C
Screw temperature 13000 Screw speed 216 rpm Extruder Screw diameter 70 mm
- 17 -Screw length 6D (*) Cylinder temperature 190 C
Screw temperature 130 C
Screw speed 33 rpm Temperature granulation die 200 C
Throughput 40 kg/h (*) 11D = 11x screw diameter, 60 = 6x screw diameter, rpm= rotations per minute A typical example of a profile extrusion from granules (example 10) and a direct profile extrusion (example 11) are presented in Table 3.
Table 3: A typical example of a profile extrusion from granulate and a direct profile extrusion.
Example 10 Example 11 Counter-rotating Counter-rotating parallel Type parallel double-screw double-screw extruder extruder Brand Bandera Bandera Dosing unit Dosing unit 1 98 kg/h (granulate) 58 kg/h (compound) Dosing unit 2 (filler) 30 kg/h Filler quantity in compound 25 phr Additionally dosed filler 75 phi Both flows through the Dose method same feed throat Extruder Screw diameter 66 mm 66 mm Screw length 200 (*) 200 (*) Cylinder temperature zone 1 185 C 185 C
Cylinder temperature zone 2 190 C 190 C
Cylinder temperature zone 3 190 C 190 C
Cylinder temperature zone 4 190 C 190 C
Cylinder temperature zone 5 195 C 195 C
Temperature adapter zone 1 185 C 185 C
Temperature adapter zone 2 190 C 190 C
Temperature die zone 1 200 C 200 C
Screw temperature 130 C
Screw speed 33 rpm Temperature granulation die 200 C
Throughput 40 kg/h (*) 11D = 11x screw diameter, 60 = 6x screw diameter, rpm= rotations per minute A typical example of a profile extrusion from granules (example 10) and a direct profile extrusion (example 11) are presented in Table 3.
Table 3: A typical example of a profile extrusion from granulate and a direct profile extrusion.
Example 10 Example 11 Counter-rotating Counter-rotating parallel Type parallel double-screw double-screw extruder extruder Brand Bandera Bandera Dosing unit Dosing unit 1 98 kg/h (granulate) 58 kg/h (compound) Dosing unit 2 (filler) 30 kg/h Filler quantity in compound 25 phr Additionally dosed filler 75 phi Both flows through the Dose method same feed throat Extruder Screw diameter 66 mm 66 mm Screw length 200 (*) 200 (*) Cylinder temperature zone 1 185 C 185 C
Cylinder temperature zone 2 190 C 190 C
Cylinder temperature zone 3 190 C 190 C
Cylinder temperature zone 4 190 C 190 C
Cylinder temperature zone 5 195 C 195 C
Temperature adapter zone 1 185 C 185 C
Temperature adapter zone 2 190 C 190 C
Temperature die zone 1 200 C 200 C
- 18 -Temperature die zone 2 200 C 200 C
Temperature die zone 3 200 C 200 C
Temperature die zone 4 200 C 200 C
Screw temperature 14000 14000 Screw speed 18 rpm 18 rpm Vacuum degassing Yes Yes Yield 98 kg/h 88 kg/h (*) 20D = 20x screw diameter, rpm = rotations per minute Example 12 As a further example, the inventors prepared a formulation as described by Example 12. To produce a batch quantity of 100 kg, the ingredients and quantities as illustrated by Table 4 were used. The quantities used are expressed in weight percentages of the formulation.
The polyvinylchloride resin with K-value of 65, titanium dioxide, tin-based stabiliser, lubricants and processing aids were loaded into a hot-mixer at room temperature. These ingredients were mixed by means of a stirrer with a blade tip speed of 38 m/s. Upon reaching 80 C in the mixture a first amount A of talc was added to the hot-mixer and mixing continued. Upon reaching a temperature of 120 C, the mixture was transferred to a cold-mixer.
The mixture was stirred with a blade tip speed of 6 m/s. In order to cool down the mixture, the mantle temperature of the cold-mixer was set at 15 C. The mixture was cooled until the mixture reached a temperature of 4000 The compound thus obtained was transported by means of a transportation conduit to a mixing station (hopper + feeder). In the mixing station a first hopper was loaded with the compound. A
second hopper of the mixing station was loaded with PVC window profile scrap.
The amount of scrap PVC as indicated in Table 3 was mixed with the compound in the mixing station. From the mixing station the mixture thus obtained was transported by means of a conduit to the main hopper of a granulation extruder. The extruder used was a counter-rotating parallel double-screw extruder of the Krauss-Maffei KM 090 type.
Table 4: Composition for producing PVC profiles (Example 12) Example 12 Formulation weight%
Temperature die zone 3 200 C 200 C
Temperature die zone 4 200 C 200 C
Screw temperature 14000 14000 Screw speed 18 rpm 18 rpm Vacuum degassing Yes Yes Yield 98 kg/h 88 kg/h (*) 20D = 20x screw diameter, rpm = rotations per minute Example 12 As a further example, the inventors prepared a formulation as described by Example 12. To produce a batch quantity of 100 kg, the ingredients and quantities as illustrated by Table 4 were used. The quantities used are expressed in weight percentages of the formulation.
The polyvinylchloride resin with K-value of 65, titanium dioxide, tin-based stabiliser, lubricants and processing aids were loaded into a hot-mixer at room temperature. These ingredients were mixed by means of a stirrer with a blade tip speed of 38 m/s. Upon reaching 80 C in the mixture a first amount A of talc was added to the hot-mixer and mixing continued. Upon reaching a temperature of 120 C, the mixture was transferred to a cold-mixer.
The mixture was stirred with a blade tip speed of 6 m/s. In order to cool down the mixture, the mantle temperature of the cold-mixer was set at 15 C. The mixture was cooled until the mixture reached a temperature of 4000 The compound thus obtained was transported by means of a transportation conduit to a mixing station (hopper + feeder). In the mixing station a first hopper was loaded with the compound. A
second hopper of the mixing station was loaded with PVC window profile scrap.
The amount of scrap PVC as indicated in Table 3 was mixed with the compound in the mixing station. From the mixing station the mixture thus obtained was transported by means of a conduit to the main hopper of a granulation extruder. The extruder used was a counter-rotating parallel double-screw extruder of the Krauss-Maffei KM 090 type.
Table 4: Composition for producing PVC profiles (Example 12) Example 12 Formulation weight%
- 19 -PVC, K-value 65 36.4 PVC window profile scrap 11.7 Talc (amount A) 3.6 Talc (amount B) 41.7 Additives 6.6 The main hopper comprised a hopper and feeder. The feeder was connected to an inlet on the extruder. The mixture was loaded in the hopper. Through the hopper and feeder the material flowed to the inlet of the extruder and onto the screws of the granulation extruder. A second amount B of talc, as indicated in Table 4, was fed to a second dosing installation which also comprised a hopper and feeder and connected to an inlet on the extruder. Both material flows met on the screws of the extruder. The conditions used for the granulation extruder were as listed in Table 5.
On the screws of the granulation extruder the compound was heated above the melting temperature of the PVC. The material melted and an intensive mixing took place. The granulation extruder was equipped with a die. The melt flow was guided through the die. Upon leaving the die thin strands were formed with a diameter of about 3 mm. The strings were cut with a rotating knife to obtain pieces with a length of about 1 to 3 mm. The granulate obtained was blown to a drying and cooling tower, cooled down and poured into big bags or a storage tank. This granulate was fit for further use.
Table 5: Operational conditions used in the granulation extruder for the preparation of granulate based on the compound as exemplified by Example 10.
Zone Temperature ( C) Cylinder zone 1 160 Cylinder zone 2 185 Cylinder zone 3 185 Cylinder zone 4 182 Cylinder zone 5 177 Cylinder zone 6 171 Adapter zone 1 174 Adapter zone 2 171 Adapter zone zone 3 171
On the screws of the granulation extruder the compound was heated above the melting temperature of the PVC. The material melted and an intensive mixing took place. The granulation extruder was equipped with a die. The melt flow was guided through the die. Upon leaving the die thin strands were formed with a diameter of about 3 mm. The strings were cut with a rotating knife to obtain pieces with a length of about 1 to 3 mm. The granulate obtained was blown to a drying and cooling tower, cooled down and poured into big bags or a storage tank. This granulate was fit for further use.
Table 5: Operational conditions used in the granulation extruder for the preparation of granulate based on the compound as exemplified by Example 10.
Zone Temperature ( C) Cylinder zone 1 160 Cylinder zone 2 185 Cylinder zone 3 185 Cylinder zone 4 182 Cylinder zone 5 177 Cylinder zone 6 171 Adapter zone 1 174 Adapter zone 2 171 Adapter zone zone 3 171
- 20 -Die 1 177 The granulate obtained was transported to a profile extruder. The extruder used is a counter-rotating conical double-screw extruder of the Krauss-Maffei KMD60 type. The granulate was loaded in the dosing station of the extruder. The dosing station was connected to an inlet of the extruder. From this dosing station the granulate flows onto the screws of the extruder. On the screws the granulate was heated up, melted and transported to a die. The conditions used in the extruder for the preparation of the profile were as listed in Table 6.
Table 6: Operational conditions used in the extruder for the preparation of a profile based on the compound as exemplified by Example 12.
Zone Temperature ( C) Cylinder zone 1 168 Cylinder zone 2 171 Cylinder zone 3 174 Cylinder zone 4 177 Adapter zone 1 182 Die 1 188 Die 2 188 Die 3 188 Die 4 188 The die that was used had the shape and size of the desired profile. The melt is pushed through the die and took the shape as dictated by the die. This melt was transported to a calibration unit and cooling installation, where the melt was brought to its exact dimensions and cooled.
The reinforcing profile obtained was cut to a desired length to obtain reinforcement elements.
The reinforcement elements were brought into a chamber of a window profile.
The reinforced window profiles thus obtained were assembled, according to techniques known in the art, to window frames.
Characteristics of PVC profiles Characteristics of PVC profiles based on a composition of Table 1 and according to a working method of Table 3 are represented in Table 7. The results obtained by using naturally occurring
Table 6: Operational conditions used in the extruder for the preparation of a profile based on the compound as exemplified by Example 12.
Zone Temperature ( C) Cylinder zone 1 168 Cylinder zone 2 171 Cylinder zone 3 174 Cylinder zone 4 177 Adapter zone 1 182 Die 1 188 Die 2 188 Die 3 188 Die 4 188 The die that was used had the shape and size of the desired profile. The melt is pushed through the die and took the shape as dictated by the die. This melt was transported to a calibration unit and cooling installation, where the melt was brought to its exact dimensions and cooled.
The reinforcing profile obtained was cut to a desired length to obtain reinforcement elements.
The reinforcement elements were brought into a chamber of a window profile.
The reinforced window profiles thus obtained were assembled, according to techniques known in the art, to window frames.
Characteristics of PVC profiles Characteristics of PVC profiles based on a composition of Table 1 and according to a working method of Table 3 are represented in Table 7. The results obtained by using naturally occurring
-21 -mineral filler (examples 1-7) can be compared with the results obtained with glass fibre (example 8). As a comparison, a PVC without reinforcing filler has a flexural modulus of 2.7 GPa and a CLTE of 52 x 10-6 mm/mmK.
Table 7: Characteristics of PVC profiles according to the invention (Examples 1-7 and 11) and according to the prior art (Example 8) Example (No.) 1 2 3 4 5 6 7 8 11 Flexural modulus (GPa) 13.9 15.7 10.8 15.7 10.8 15.7 10.8 15.0 12.5 CLTE (x 10-6 mm/mm/K) 8 19 10 19 10 19 10 47
Table 7: Characteristics of PVC profiles according to the invention (Examples 1-7 and 11) and according to the prior art (Example 8) Example (No.) 1 2 3 4 5 6 7 8 11 Flexural modulus (GPa) 13.9 15.7 10.8 15.7 10.8 15.7 10.8 15.0 12.5 CLTE (x 10-6 mm/mm/K) 8 19 10 19 10 19 10 47
Claims (36)
1. A granulate or profile made of a reinforced polyvinyl chloride polymer comprising at least 40 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride (PVC), and PVC with a K-value of 50-68, wherein said reinforced polyvinyl chloride polymer has a flexural modulus of at least 5 GPa, and wherein said naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
2. The granulate or profile according to claim 1, wherein said reinforced polyvinyl chloride polymer has a flexural modulus of at least 8 GPa.
3. The granulate or profile according to claims 1 or 2, wherein said reinforced polyvinyl chloride polymer has a flexural modulus of at least 10 GPa.
4. The granulate or profile according to any one of claims 1 to 3, wherein the reinforced polyvinyl chloride polymer composition is substantially free of natural and mineral fibers.
5. The granulate or profile according to any one of claims 1 to 4, wherein said reinforced polyvinyl chloride polymer composition comprises more than 60 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein said naturally occurring mineral filler is selected from wollastonite, vermiculite, talc, mica, and/or combinations thereof, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition has a flexural modulus of at least 8 GPa, and wherein the reinforced polyvinyl chloride polymer composition is substantially free of natural and mineral fibers.
6. The granulate or profile according to any one of claims 1 to 5, wherein said reinforced polyvinyl chloride polymer composition comprises more than 80 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride.
7. The granulate or profile according to any one of claims 1 to 6, wherein said reinforced polyvinyl chloride polymer composition comprises about 95 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride.
8. The granulate or profile according to any one of claims 1 to 7, wherein said reinforced polyvinyl chloride polymer composition comprises more than 100 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride.
9. The granulate or profile according to any one of claims 1 to 8, wherein the naturally occurring mineral filler is talc and/or mica.
10. The granulate or profile according to any one of claims 1 to 9, wherein the naturally occurring mineral filler comprises mica, and wherein the flexural modulus is at least 15 GPa.
11. The granulate or profile according to any one of claims 1 to 10, wherein the naturally occurring mineral filler comprises talc, and wherein the flexural modulus is at least 10.8 GPa.
12. The granulate or profile according to any one of claims 1 to 11, with a K-value between 64 and 68.
13. The granulate or profile according to any one of claims 4 to 12, said talc having an average grain size d50 between 0.5 and 5 µm.
14. The granulate or profile according to any one of claims 4 to 13, wherein the naturally occurring mineral filler has an average grain size between 0.5 and 50 µm;
said talc has an average grain size d50 between 0.5 and 5 µm and said mica has an average grain size d50 between 30 and 35 µm.
said talc has an average grain size d50 between 0.5 and 5 µm and said mica has an average grain size d50 between 30 and 35 µm.
15. The granulate or profile according to any one of claims 1 to 14, with a coefficient of linear thermal expansion (CLTE) lower than 25 x 10 -6 mm/mm/K.
16. The granulate or profile according to any one of claims 1 to 15, wherein said reinforced polyvinyl chloride polymer composition comprises at least 35 weight percent of said naturally occurring mineral filler.
17. The granulate or profile according to any one of claims 1 to 16, wherein said reinforced polyvinyl chloride polymer composition comprises at least 40 weight percent of said naturally occurring mineral filler.
18. The granulate or profile according to any one of claims 1 to 17, wherein said reinforced polyvinyl chloride polymer composition comprises at least 45 weight percent of said naturally occurring mineral filler.
19. The granulate or profile according to any one of claims 1 to 18, wherein said profile is provided with hollow cavities.
20. A granulate or profile made of a reinforced polyvinyl chloride polymer composition, said reinforced polyvinyl chloride polymer composition comprising more than 80 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition has a flexural modulus of at least 5 GPa, and wherein said naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
21. The granulate or profile according to claim 20, wherein said reinforced polyvinyl chloride polymer composition has a flexural modulus of at least 8 GPa.
22. The granulate or profile according to claims 20 or 21, wherein said reinforced polyvinyl chloride polymer composition has a flexural modulus of at least 10 GPa.
23. The granulate or profile according to any one of claims 20 to 22, wherein said reinforced polyvinyl chloride polymer composition exhibits a coefficient of linear thermal expansion that is lower than 20 x 10 -6 /°K.
24. The granulate or profile according to any one of claims 20 to 23, wherein said reinforced polyvinyl chloride polymer composition comprises more than 100 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride.
25. A granulate or profile made of a reinforced polyvinyl chloride polymer composition, said reinforced polyvinyl chloride polymer composition comprising more than 60 weight parts of naturally occurring mineral filler for every 100 weight parts of polyvinyl chloride, wherein the polyvinyl chloride has a K-value of 50 to 68, wherein the reinforced polyvinyl chloride polymer composition exhibits a coefficient of linear thermal expansion that is lower than 25 x 10 -6 /°K, and wherein said naturally occurring mineral filler is selected from the group consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof.
26. The granulate or profile according to claim 25, wherein the reinforced polyvinyl chloride polymer composition is substantially free of natural and mineral fibers.
27. A method for obtaining a granulate or a profile according to any one of claims 1 to 26, comprising the steps of:
a) preparation of a pre-reinforced polymer by mixing polyvinyl chloride polymer with a quantity A of a naturally occurring mineral filler at a temperature lower than the melting temperature of the polyvinyl chloride polymer, b) mixing the pre-reinforced polymer obtained under a) with a quantity B of a naturally occurring mineral filler at a temperature higher than 180°C to obtain a reinforced polyvinyl chloride polymer, c) optionally granulating the reinforced polyvinyl chloride polymer obtained in step b), d) pressing the reinforced polymer obtained in step b) or the granulate obtained in step c) through a die to obtain said granulate or profile;
wherein said naturally occurring mineral filler is selected from the list consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof; and wherein the ratio of the quantity A of naturally occurring mineral filler to the quantity B of naturally occurring mineral filler is at least 0.1.
a) preparation of a pre-reinforced polymer by mixing polyvinyl chloride polymer with a quantity A of a naturally occurring mineral filler at a temperature lower than the melting temperature of the polyvinyl chloride polymer, b) mixing the pre-reinforced polymer obtained under a) with a quantity B of a naturally occurring mineral filler at a temperature higher than 180°C to obtain a reinforced polyvinyl chloride polymer, c) optionally granulating the reinforced polyvinyl chloride polymer obtained in step b), d) pressing the reinforced polymer obtained in step b) or the granulate obtained in step c) through a die to obtain said granulate or profile;
wherein said naturally occurring mineral filler is selected from the list consisting of wollastonite, vermiculite, talc, mica, and/or combinations thereof; and wherein the ratio of the quantity A of naturally occurring mineral filler to the quantity B of naturally occurring mineral filler is at least 0.1.
28. The method according to claim 27, wherein said quantity A is between 2 and 25 or between 25 and 40 parts per hundred parts of the polyvinyl chloride polymer (phr).
29. The method according to any one of claims 27 to 28, wherein the total quantity of naturally occurring mineral filler (A+B) to the quantity of polyvinyl chloride polymer, is between 0.4 and 2.5.
30. The method according to any one of claims 27 to 29, further comprising the step of adding a processing aid in a quantity of between 0 and 15 weight%
31. The method according to any one of claims 27 to 30, further comprising the step of adding a thermal stabilizer in a quantity of between 0 and 5 weight%.
32. A granulate obtained in step c) of the method according to any one of claims 27 to 31.
33. Use of a granulate or profile according to any one of claims 1 to 26 as a reinforcement element.
34. The use of a granulate or profile according to claim 33, wherein said reinforcement element is used as basis for a suspended structure or closure.
35. The use of a granulate or profile according to claim 34, wherein said reinforcement element is used as basis for a fitting.
36. Use of a granulate or profile according to any one of claims 1 to 26, wherein said profile is fastened with nails or screws.
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US11020408P | 2008-10-31 | 2008-10-31 | |
BE2008/0593 | 2008-10-31 | ||
US61/110,204 | 2008-10-31 | ||
BE2008/0593A BE1018451A3 (en) | 2008-10-31 | 2008-10-31 | PVC PROFILES WITH HIGH CONTENT OF MINERAL FILLER AND THEIR USE. |
PCT/EP2009/064401 WO2010049532A1 (en) | 2008-10-31 | 2009-10-30 | Pvc profiles with high contents of mineral filler and their uses |
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