WO2008103128A1 - Diffusion retardation in fluoroplastics - Google Patents
Diffusion retardation in fluoroplastics Download PDFInfo
- Publication number
- WO2008103128A1 WO2008103128A1 PCT/SE2008/050208 SE2008050208W WO2008103128A1 WO 2008103128 A1 WO2008103128 A1 WO 2008103128A1 SE 2008050208 W SE2008050208 W SE 2008050208W WO 2008103128 A1 WO2008103128 A1 WO 2008103128A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- additive
- fluoroplastic
- reactive
- compound
- diffusion
- Prior art date
Links
- 229920002313 fluoropolymer Polymers 0.000 title claims abstract description 62
- 238000009792 diffusion process Methods 0.000 title claims abstract description 53
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 claims abstract description 148
- 239000000654 additive Substances 0.000 claims abstract description 86
- 230000000996 additive effect Effects 0.000 claims abstract description 79
- 239000004155 Chlorine dioxide Substances 0.000 claims abstract description 74
- 235000019398 chlorine dioxide Nutrition 0.000 claims abstract description 67
- 239000002033 PVDF binder Substances 0.000 claims abstract description 33
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims abstract description 32
- 238000000034 method Methods 0.000 claims abstract description 24
- 150000001875 compounds Chemical class 0.000 claims abstract description 19
- 230000015556 catabolic process Effects 0.000 claims abstract description 11
- 238000006731 degradation reaction Methods 0.000 claims abstract description 11
- 229920001780 ECTFE Polymers 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 18
- 229920000642 polymer Polymers 0.000 claims description 17
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 14
- 239000000460 chlorine Substances 0.000 claims description 14
- 229910052801 chlorine Inorganic materials 0.000 claims description 14
- 150000001412 amines Chemical class 0.000 claims description 13
- -1 alkali metal formate Chemical class 0.000 claims description 9
- 150000001805 chlorine compounds Chemical class 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- 229910052783 alkali metal Inorganic materials 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 claims description 3
- 229920005862 polyol Polymers 0.000 claims description 3
- 230000002344 fibroplastic effect Effects 0.000 claims 1
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical class CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 description 34
- 230000035515 penetration Effects 0.000 description 28
- 239000000463 material Substances 0.000 description 20
- 239000000523 sample Substances 0.000 description 17
- 230000000694 effects Effects 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- VSAWBBYYMBQKIK-UHFFFAOYSA-N 4-[[3,5-bis[(3,5-ditert-butyl-4-hydroxyphenyl)methyl]-2,4,6-trimethylphenyl]methyl]-2,6-ditert-butylphenol Chemical compound CC1=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C1CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 VSAWBBYYMBQKIK-UHFFFAOYSA-N 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 10
- 150000002989 phenols Chemical class 0.000 description 9
- 239000004033 plastic Substances 0.000 description 9
- 229920003023 plastic Polymers 0.000 description 9
- 238000010586 diagram Methods 0.000 description 8
- 235000012701 green S Nutrition 0.000 description 6
- WDPIZEKLJKBSOZ-UHFFFAOYSA-M green s Chemical compound [Na+].C1=CC(N(C)C)=CC=C1C(C=1C2=CC=C(C=C2C=C(C=1O)S([O-])(=O)=O)S([O-])(=O)=O)=C1C=CC(=[N+](C)C)C=C1 WDPIZEKLJKBSOZ-UHFFFAOYSA-M 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 239000004811 fluoropolymer Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000003963 antioxidant agent Substances 0.000 description 4
- 230000003078 antioxidant effect Effects 0.000 description 4
- 235000006708 antioxidants Nutrition 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- CEQFOVLGLXCDCX-WUKNDPDISA-N methyl red Chemical compound C1=CC(N(C)C)=CC=C1\N=N\C1=CC=CC=C1C(O)=O CEQFOVLGLXCDCX-WUKNDPDISA-N 0.000 description 4
- 230000000149 penetrating effect Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000003381 stabilizer Substances 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 229920005610 lignin Polymers 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical compound OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 229920006373 Solef Polymers 0.000 description 2
- 238000002835 absorbance Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 239000011152 fibreglass Substances 0.000 description 2
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical compound FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920002620 polyvinyl fluoride Polymers 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- 239000004801 Chlorinated PVC Substances 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- 238000004566 IR spectroscopy Methods 0.000 description 1
- 239000004283 Sodium sorbate Substances 0.000 description 1
- 229930003427 Vitamin E Natural products 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000008366 buffered solution Substances 0.000 description 1
- 238000011088 calibration curve Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920000457 chlorinated polyvinyl chloride Polymers 0.000 description 1
- 239000008199 coating composition Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000007687 exposure technique Methods 0.000 description 1
- 238000013213 extrapolation Methods 0.000 description 1
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000007793 ph indicator Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000013074 reference sample Substances 0.000 description 1
- 239000002990 reinforced plastic Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000003017 thermal stabilizer Substances 0.000 description 1
- 235000019165 vitamin E Nutrition 0.000 description 1
- 229940046009 vitamin E Drugs 0.000 description 1
- 239000011709 vitamin E Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- GZIFEOYASATJEH-VHFRWLAGSA-N δ-tocopherol Chemical compound OC1=CC(C)=C2O[C@@](CCC[C@H](C)CCC[C@H](C)CCCC(C)C)(C)CCC2=C1 GZIFEOYASATJEH-VHFRWLAGSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/005—Stabilisers against oxidation, heat, light, ozone
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/13—Phenols; Phenolates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/13—Phenols; Phenolates
- C08K5/134—Phenols containing ester groups
- C08K5/1345—Carboxylic esters of phenolcarboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
- C08K5/17—Amines; Quaternary ammonium compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/16—Nitrogen-containing compounds
- C08K5/34—Heterocyclic compounds having nitrogen in the ring
- C08K5/3467—Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
- C08K5/3477—Six-membered rings
- C08K5/3492—Triazines
- C08K5/34922—Melamine; Derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
- C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L27/12—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D127/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers
- C09D127/02—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
- C09D127/12—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L58/00—Protection of pipes or pipe fittings against corrosion or incrustation
- F16L58/02—Protection of pipes or pipe fittings against corrosion or incrustation by means of internal or external coatings
- F16L58/04—Coatings characterised by the materials used
- F16L58/10—Coatings characterised by the materials used by rubber or plastics
- F16L58/1009—Coatings characterised by the materials used by rubber or plastics the coating being placed inside the pipe
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L9/00—Rigid pipes
- F16L9/14—Compound tubes, i.e. made of materials not wholly covered by any one of the preceding groups
- F16L9/147—Compound tubes, i.e. made of materials not wholly covered by any one of the preceding groups comprising only layers of metal and plastics with or without reinforcement
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L11/00—Hoses, i.e. flexible pipes
- F16L11/04—Hoses, i.e. flexible pipes made of rubber or flexible plastics
- F16L2011/047—Hoses, i.e. flexible pipes made of rubber or flexible plastics with a diffusion barrier layer
Definitions
- the present invention is concerned with preventing diffusion through fluoropolymers, such as those used as liners to protect metal or FRP structures. It is further concerned with stabilizing fluoropolymers used in or at a chlorine dioxide reactor against deterioration.
- the fluoroplastics are normally not themselves attacked chemically but small molecules, such as acids and CIO2 , can diffuse through the material and attack the other, less corrosion resistant, material.
- a decrease of the diffusion rate or the amount of the permeating media would increase the service life of structures where diffusion is a problem, i.a. lined tanks or pipes.
- US 3,557.050 describes a vinyl fluoride polymer which is heat stabilized by a combination of an alkali metal formate and an organic antioxidant.
- US 3,775,496 describes a pigmented coating composition containing a liquid medium, pigment and a polyvinyl fluoride polymer.
- the composition is heat stabilized by incorporation of a mixture of an aliphatic polyol, organic antioxidant and glycidyl methacrylate polymer. It is especially underlined that lack of any one of the three components materially mitigates the effect to be otherwise achieved.
- One object of the invention is to overcome the problems discussed above by preventing or slowing down diffusion through a fluoroplastic, such as a liner on a substrate of steel or FRP.
- a further object is to avoid or decrease the degradation of fluoroplastics used in or in connection with a chlorine dioxide reactor.
- Another object is to achieve a fluoroplastic which is diffusion resistant or at least shows a decreased diffusion.
- Still another object is to achieve a fluoroplastic which is completely or at least partially resistant to degradation when used in or in connection with a chlorine dioxide reactor.
- a further object is to achieve a process for producing a fluoroplastic which is diffusion resistant or at least shows a decreased diffusion.
- a reactive additive i.e., an additive which will react with the permeating media without impairing the properties of the polymer.
- the diffusion resistant fluoropolymers of the invention do not contain for example inorganic non-metallic reducing agents, aliphatic polyols together with glycidyl methacrylate polymer or alkali metal formate in combination with the additive having reactive groups.
- Hindered phenols are presently used in thermal stabilizer systems for other plastics.
- fluoroplastics have generally such high strength and thermal resistance that the use of stabilizers has not been necessary. Also, in the present case it is not a question of stabilizing the fluoroplastic, but of hindering diffusion through the polymer.
- Hindered phenols are e.g. used in water conduits, normally made of polyolefins, such as polyethylene or polypropylene.
- the plastic is stabilized from oxidization by oxygen.
- the drinking water contains small amounts of chlorine dioxide or hypochlorite and it has been noticed that the plastic is gradually depleted of the stabilizer owing to its reaction with the chlorine compounds.
- Irganox 1010 slowed down the diffusion of chlorine dioxide and HCIO by reacting with these compounds.
- the reaction between the additive and the permeating media could be followed by FTIR.
- Additive loadings between 0.1 and 1 wt% were tested and it was found to be a linear relationship between amount of additive and penetration depth.
- the addition of 1 wt% Irganox 1010 to PVDF (polyvinylidene fluoride) gave about half of the penetration depth of CIO2 as compared to a sample without additive. For HCIO the effect was even larger.
- Irganox 1010 another hindered phenol Irganox 1330 has been tested.
- the invention concerns a process of slowing down diffusion of an element or a compound through a fluoroplastic comprising the addition of a reactive additive that reacts with the element or compound.
- the element or compound which should be prevented from diffusing through the fluoropolymer may be for instance chlorine or a chlorine compound such as chlorine dioxide or hypochloric acid.
- the reactive additive is preferably a hindered phenol or hindered amine.
- the necessary concentration may be as low as 0.1 wt%, preferably more than 0.5 wt% and especially at least 1 wt%. At most 10 wt% should be used, preferably at most 5 wt%. The best results are obtained at a loading of about 1 wt%.
- wt% is based on the weight of the plastic without the additive.
- vitamin E vitamin E
- lignin lignin
- phenols in general.
- Suitable reactive additives are hindered phenols and amines such as
- Fig 1 is a diagram showing penetration depth of chlorine dioxide in different plastics.
- Fig 2 is a diagram showing solubility of chlorine dioxide in different thermoplastics.
- Fig 3 is a diagram showing penetration depth of chlorine dioxide, with and without additive.
- Fig 4 is a diagram showing penetration profiles of chlorine dioxide.
- Fig 5 is a diagram showing concentration of penetrating agent for different concentrations of Irganox 1010.
- Fig 6 is a diagram showing Arrhenius plots of the temperature dependence.
- Fig 7 is a diagram showing the penetration depth at different concentrations of chlorine dioxide.
- Figure 1 shows the concentration of CIO2 as a function of penetration depth, measured after immersion of the plastic at 70 0 C for 24 hours.
- Figure 2 shows the solubility of CIO2 in different thermoplastics, at different temperatures. As can be seen, the solubility is quite large in PVDF compared to the all the others, except for PVC and CPVC.
- Irganox 1010 This is a hindered phenol commonly used as an antioxidant for polyolefins (PP and PE). It is easily available at a relatively low price.
- Another additive that could be of interest is lignin.
- the reaction between lignin and CIO 2 is well known from paper bleaching. It is important that the additive is stable at the processing temperature of the polymer, which is not the case for the combination of Irganox 1010 with the fully fluorinated polymers such as PFA. In this case an additive with a higher decomposition temperature should be used.
- Irganox E201 Vitamine E
- the aim of a laboratory study was to investigate if the addition of a reactive additive could slow down the diffusion of chlorine dioxide in PVDF.
- PVDF powder A commercial grade of PVDF powder (SOLEF 1010) was supplied by Solvay Solexis and Irganox 1010, Formula I, was supplied by Ciba Specialty Chemicals.
- the Irganox was mixed into the PVDF powder by first dissolving different amounts in dichloromethane (CH 2 Cb) and then adding it to the PVDF powder. The mixtures were stirred thoroughly and left to dry for 48h.
- Sheets with different concentrations of Irganox 1010 were then prepared by compression moulding of the powder.
- Irganox 1010 was also added to commercial grades of ECTFE (Halar 901 ) supplied by Solvay Solexis.
- Samples approximately 20x20 mm, were cut from the compression moulded plates. The samples were then immersed in the penetrating media and kept at 50 0 C. The exposure time was between 17 and 24 hours, unless otherwise specified. After exposure the samples were cut in two, and 150 ⁇ m thick films were cut from the cross-section with a microtome. The films were then immersed in the methyl red solution. After the reaction time, the samples were cleaned with ethanol and dried. The films were scanned and analysed with image analysis software, giving a colour profile of the penetration depth. 2. LGB method
- the samples When exposed in the industrial environment the samples are mounted on metal bars immersed in the penetrating medium. Thus, the samples are exposed to the medium from both sides and the maximum penetration depth is 1.5 mm into the 3 mm thick samples.
- the concentration of chlorine dioxide can be plotted as a function of penetration depth for the two samples, treated by immersion in 7 g/l CIO2 solution at 50 0 C for 17 hours.
- One sample contained no additive and the second sample contained 1 wt% Irganox 1010. The results are shown in Figure 3.
- the plots in Figure 3 show that the profile of the penetration depth is much sharper for the sample with additive than in the one without.
- CIO2 has penetrated 0.8 mm while in the sample with 1 wt% Irganox 1010 the penetration depth is only 0.3 mm.
- the penetration depth was also followed using the LGB method. This method does not only give a relative concentration of CIO2 in the sample but can be used to calculate the actual amount in the material.
- Irganox 1010 have shown that it is only the hindered phenol group that decreases and not the ester.
- Test pieces of PVDF were also exposed 50 days in the CIO2 stripper at Aspa bruk.
- the temperature was 58 0 C and the CIO2 concentration about 1.4 g/l.
- the CIO2 had permeated all the way through all samples except the ones with 0.5 and 1 wt% of additive. In the samples containing the additive no blisters, no other deterioration nor any negative effect on material properties were observed.
- Test pieces of PVDF with different concentrations of Irganox 1010 were also exposed for one year in the primary chlorine dioxide reactor at the Skarblacka mill.
- the temperature was 58 0 C and the CIO2 concentration around 2.6 g/l.
- Test pieces of PVDF with 1 wt% Irganox 1010 and 1330 and without additive were exposed in hot (75-85 0 C) wet chlorine gas at the chlorine plant in
- PVDF sample without additive showed an internal layer with cracks due to degraded material. This was not found in the samples with additive and just as for the other industrially exposed samples, no blisters nor any other negative effect on material properties were observed in these samples after the exposure.
- FIG. 6 is a diagram showing Arrhenius plots of the temperature dependence showing the negative logarithm of the diffusion coefficient D as a function of the reciprocal absolute temperature. The higher the value of neg Log D the slower the diffusion.
- PVDF with Irganox 1330 and Irganox 1010 are, within the experimental error, more or less as efficient throughout the whole temperature range.
- the hindered amine Chimasorb 944 is a bit less efficient and PVDF without additive shows the highest diffusion rate. It is interesting to note that the slope of the lines is about the same for all mixes, which means that the activation energy is the same. From this it can be concluded that it is the activation energy for the diffusion which is rate determining, i.e. slower than the reaction between the additives and CIO2.
- Figure 7 shows the effect of the concentration of the chlorine dioxide solution on the penetration depth in the PVDF containing 1 wt% Irganox 1010.
- the samples were immersed in the Cl ⁇ 2-solution at 5O 0 C for 24 hours.
- the concentrations used were 3 g/l (cone 1/1 ), 0.3 g/l (cone 1/10) and 0.03 g/l (cone 1/100), respectively.
- the reactive additive also stabilised the samples against degradation when exposed in a chlorine dioxide reactor. Addition of at least 0.5 wt% Irganox 1010 completely prevented the degradation of PVDF when exposed for one year.
- HCIO is a complex mixture of chlorine species and the composition depends on the pH value and the temperature.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
A process of slowing down diffusion of an element or a compound through a fluoroplastic comprising the addition of a reactive additive having reactive groups that react with the element or compound. A process of preventing degradation of the fluoroplastics PVDF and ECTFE used in, or in connection with a reactor where chlorine dioxide is produced comprising mixing the fluoroplastic with a reactive additive having reactive groups. A diffusion resistant fluoroplastic which comprises a reactive additive having reactive groups that react with an element and/or compound to which the fluoroplastic is diffusion resistant. The use of a reactive additive having reactive groups as an additive in a fluoroplastic to prevent or slow down the diffusion of an element or a compound through the fluoroplastic. The use of a reactive additive having reactive groups as an additive in the fluoroplastics PVDF and ECTFE used in, or in connection with a reactor for producing chlorine dioxide to prevent or slow down degradation of the fluoroplastic.
Description
Diffusion retardation in fluoroplastics
The present invention is concerned with preventing diffusion through fluoropolymers, such as those used as liners to protect metal or FRP structures. It is further concerned with stabilizing fluoropolymers used in or at a chlorine dioxide reactor against deterioration.
TECHNICAL FIELD
One of the most important differences in properties between plastics and metals, when used in corrosive environments, is the fact that polymers are permeable to small molecules. This permeability can lead to swelling of the polymer and also means that polymers cannot be used as absolute shields. Fluoroplastics are widely used as protective linings and in other shielding applications since they have unique chemical and temperature resistance in severe environments. However, experience from the field shows that the lifetime of a lined or coated structure quite often is determined by diffusion of aggressive species, such as hydrochloric acid (HCI) and chlorine dioxide (CIO2), through the fluoroplastic material followed by corrosion attack on the FRP (fibreglass reinforced plastic) or steel substrate.
Thus, the fluoroplastics are normally not themselves attacked chemically but small molecules, such as acids and CIO2 , can diffuse through the material and attack the other, less corrosion resistant, material. A decrease of the diffusion rate or the amount of the permeating media would increase the service life of structures where diffusion is a problem, i.a. lined tanks or pipes.
Another problem encountered with one of the fluoroplastics, PVDF, and sometimes also with ECTFE, and not generally recognized occurs when used in, or in connection with a chlorine dioxide reactor. In spite of the general high resistance of fluoroplastics to chlorine and chlorine compounds
the fluoroplastic is degraded and must be changed after a certain time. Thus, in this case the fluoroplastic itself is attacked.
In such a reactor many different elements and compounds are present. It is not known which species or combination of species cause the degradation of the fluoroplastic.
BACKGROUND ART
US 3,557.050 describes a vinyl fluoride polymer which is heat stabilized by a combination of an alkali metal formate and an organic antioxidant.
US 3,557,051 describes heat stabilization of a polymer comprising a homopolymer of vinyl fluoride and a copolymer of vinyl fluoride and up to 25 wt% of copolymerizable monomers by the use of a combination of an inorganic non-metallic reducing agent and an organic antioxidant.
US 3,775,496 describes a pigmented coating composition containing a liquid medium, pigment and a polyvinyl fluoride polymer. The composition is heat stabilized by incorporation of a mixture of an aliphatic polyol, organic antioxidant and glycidyl methacrylate polymer. It is especially underlined that lack of any one of the three components materially mitigates the effect to be otherwise achieved.
However, none of these documents discuss the problem with diffusion through a polymer, nor the problem of degradation in a chlorine dioxide reactor.
OBJECTS OF THE INVENTION
One object of the invention is to overcome the problems discussed above by preventing or slowing down diffusion through a fluoroplastic, such as a liner on a substrate of steel or FRP.
A further object is to avoid or decrease the degradation of fluoroplastics used in or in connection with a chlorine dioxide reactor.
Another object is to achieve a fluoroplastic which is diffusion resistant or at least shows a decreased diffusion.
Still another object is to achieve a fluoroplastic which is completely or at least partially resistant to degradation when used in or in connection with a chlorine dioxide reactor.
A further object is to achieve a process for producing a fluoroplastic which is diffusion resistant or at least shows a decreased diffusion.
SHORT DESCRIPTION OF THE INVENTION
One idea for slowing down the diffusion that has come up is the addition of a reactive additive, i.e., an additive which will react with the permeating media without impairing the properties of the polymer.
The objects of the invention are achieved by the addition to the fluoroplastic of an additive having reactive groups which will react with the permeating media without impairing the properties of the fluoropolymer.
It is not necessary to add any further stabilizer, in addition to the additive having reactive groups. Thus, the diffusion resistant fluoropolymers of the invention do not contain for example inorganic non-metallic reducing agents,
aliphatic polyols together with glycidyl methacrylate polymer or alkali metal formate in combination with the additive having reactive groups.
Hindered phenols are presently used in thermal stabilizer systems for other plastics. However, fluoroplastics have generally such high strength and thermal resistance that the use of stabilizers has not been necessary. Also, in the present case it is not a question of stabilizing the fluoroplastic, but of hindering diffusion through the polymer.
Hindered phenols are e.g. used in water conduits, normally made of polyolefins, such as polyethylene or polypropylene. The plastic is stabilized from oxidization by oxygen. However, the drinking water contains small amounts of chlorine dioxide or hypochlorite and it has been noticed that the plastic is gradually depleted of the stabilizer owing to its reaction with the chlorine compounds.
Due to this Irganox 1010, one of the most commonly used hindered phenols, was chosen for a trial investigation. PVDF was chosen as the main polymer matrix since this material is often used in liner applications and since the diffusion rate can easily be determined in this material. Some experiments were also performed on ECTFE containing 1 wt% Irganox 1010.
It was found that the addition of Irganox 1010 slowed down the diffusion of chlorine dioxide and HCIO by reacting with these compounds. The reaction between the additive and the permeating media could be followed by FTIR. Additive loadings between 0.1 and 1 wt% were tested and it was found to be a linear relationship between amount of additive and penetration depth. The addition of 1 wt% Irganox 1010 to PVDF (polyvinylidene fluoride) gave about half of the penetration depth of CIO2 as compared to a sample without additive. For HCIO the effect was even larger.
In addition to Irganox 1010, another hindered phenol Irganox 1330 has been tested. It was found to give the same good effect on the diffusion rate as Irganox 1010. To check the use of other reactive groups, apart from phenols, Chimasorb 944, which is a hindered amine, was also tested. It also showed the same effect as the hindered phenols.
DETAILED DESCRIPTION OF THE INVENTION
The invention concerns a process of slowing down diffusion of an element or a compound through a fluoroplastic comprising the addition of a reactive additive that reacts with the element or compound. The element or compound which should be prevented from diffusing through the fluoropolymer may be for instance chlorine or a chlorine compound such as chlorine dioxide or hypochloric acid.
The reactive additive is preferably a hindered phenol or hindered amine. The necessary concentration may be as low as 0.1 wt%, preferably more than 0.5 wt% and especially at least 1 wt%. At most 10 wt% should be used, preferably at most 5 wt%. The best results are obtained at a loading of about 1 wt%.
In this application wt% is based on the weight of the plastic without the additive.
Other possible reactive additives are vitamin E, lignin, and phenols in general.
It was also discovered that not only does the reactive additive slow down diffusion of aggressive species, but it also increases the resistance of PVDF when used in such an aggressive surrounding as in or in connection with a chlorine dioxide reactor.
Suitable reactive additives are hindered phenols and amines such as
The invention is further clarified by the following description with reference to the enclosed drawings.
BRIEF DESCRIPTION OF DRAWINGS
Fig 1 is a diagram showing penetration depth of chlorine dioxide in different plastics. Fig 2 is a diagram showing solubility of chlorine dioxide in different thermoplastics.
Fig 3 is a diagram showing penetration depth of chlorine dioxide, with and without additive.
Fig 4 is a diagram showing penetration profiles of chlorine dioxide. Fig 5 is a diagram showing concentration of penetrating agent for different concentrations of Irganox 1010.
Fig 6 is a diagram showing Arrhenius plots of the temperature dependence.
Fig 7 is a diagram showing the penetration depth at different concentrations of chlorine dioxide.
EXAMPLES
After 5 years in service an FRP pipe with a lining of FEP (fluoroplastic), which has been used for transporting CI2 containing brine, could no longer be used since the lining had loosened completely and obstructed the flow. The reason for the loosening was that CI2 had diffused through the FEP and destroyed the interface between the FRP and the lining.
Another example of failure due to diffusion through a fluoroplastic liner concerns a PVDF lined FRP pipe for transport of hot chlorine dioxide bleached pulp. This pipe burst open dumping 600 tonnes of hot pulp on the factory floor. The failure was due to stress corrosion cracking occurring as a result of bad clamping generating stresses in the pipe and CIO2 diffusing through the PVDF attacking the fibre glass in the FRP.
With the help of new techniques developed by the inventor, data on diffusion, permeation and solubility could be generated for different fluoroplastics. It was found that the diffusion is very fast through many of the fluoroplastics,
especially PVDF which is one of the most used lining materials. Figure 1 shows the concentration of CIO2 as a function of penetration depth, measured after immersion of the plastic at 70 0C for 24 hours.
Of importance is, however, not only how fast but also how much that is permeating. This will depend on the solubility. Figure 2 shows the solubility of CIO2 in different thermoplastics, at different temperatures. As can be seen, the solubility is quite large in PVDF compared to the all the others, except for PVC and CPVC.
It is well known that a chemical reaction will slow down the permeation through a plastic material. Since fluoroplastics are so chemically inert in themselves the penetrant will pass through without being held back by chemical reactions. In other plastics it might be that the penetrant is diffusing very slowly due to it reacting with the polymer or some additive. The material will thus act as a shield for a while but it might become totally degraded and useless with time. One way of getting the reduced diffusion rate without impairing the properties of the polymer is by adding a reactive additive, i.e., an additive which can react with the permeating media without changing the properties of the polymer.
One additive that could be suitable as a reactive additive for preventing CIO2 diffusion is Irganox 1010. This is a hindered phenol commonly used as an antioxidant for polyolefins (PP and PE). It is easily available at a relatively low price. Another additive that could be of interest is lignin. The reaction between lignin and CIO2 is well known from paper bleaching. It is important that the additive is stable at the processing temperature of the polymer, which is not the case for the combination of Irganox 1010 with the fully fluorinated polymers such as PFA. In this case an additive with a higher decomposition temperature should be used. An example of such an additive is Irganox E201 (Vitamine E).
The aim of a laboratory study was to investigate if the addition of a reactive additive could slow down the diffusion of chlorine dioxide in PVDF.
A commercial grade of PVDF powder (SOLEF 1010) was supplied by Solvay Solexis and Irganox 1010, Formula I, was supplied by Ciba Specialty Chemicals. The Irganox was mixed into the PVDF powder by first dissolving different amounts in dichloromethane (CH2Cb) and then adding it to the PVDF powder. The mixtures were stirred thoroughly and left to dry for 48h.
Formula I
Sheets with different concentrations of Irganox 1010 were then prepared by compression moulding of the powder.
In addition to the above mentioned samples, four batches of plaques (100 x 100 x 3 mm) were injection moulded from granulated PVDF (SOLEF 1010). Batch 1 had an addition of 1 wt% of Irganox 1010, batch 2 1 wt% Irganox 1330, which is also a hindered phenol, and batch 3 1 wt% Chimasorb 944, which is a hindered amine. All additives were supplied by Ciba Specialty Chemicals. Batch 4 did not contain any additive. All four batches were extruded before the injection moulding to ensure good mixing. Irganox 1330 and Chimasorb 944 have Formulas Il and III.
Formula Il
Formula
The results from recalculating 1 wt% into the concentration of reactive groups, i.e. the hindered phenol for Irganox 1010 and 1330 and the hindered amine for Chimasorb 944, are shown in Table 1.
In addition to the experiments performed on PVDF, 1 wt% Irganox 1010 was also added to commercial grades of ECTFE (Halar 901 ) supplied by Solvay Solexis.
Methods of penetration depth measurements
1. Indicator technique
This technique is based on the colour change of a pH-indicator solution. A solution of methyl red in ethanol and acetone was used. Methyl red changes colour from yellow to red when the pH drops below 4.5. It has been found that this technique works very well for determining the penetration depth and diffusion rate of both strong acids and chlorine dioxide.
Samples, approximately 20x20 mm, were cut from the compression moulded plates. The samples were then immersed in the penetrating media and kept at 50 0C. The exposure time was between 17 and 24 hours, unless otherwise specified. After exposure the samples were cut in two, and 150 μm thick films were cut from the cross-section with a microtome. The films were then immersed in the methyl red solution. After the reaction time, the samples were cleaned with ethanol and dried. The films were scanned and analysed with image analysis software, giving a colour profile of the penetration depth.
2. LGB method
The LGB-method uses the fact that a buffered solution of Lissamine Green B (LGB) loses its clear blue colour in a reaction with CIO2. By measuring the absorbance of a Clθ2-containing sample relative to a reference sample and using a calibration curve, the CIO2 concentration in the initial sample can be calculated.
Slices cut from the sample were put in LGB-solution and then left for 48 hours to ensure that all CIO2 had diffused out of the samples and reacted with the LGB. After that, the absorbance at 616 nm was measured and the concentration of CIO2 in the sample slices could be calculated. With these data a concentration profile is obtained by plotting the CIO2 concentration of the slices versus their cumulative thickness.
3. Exposure technique
When exposed in the industrial environment the samples are mounted on metal bars immersed in the penetrating medium. Thus, the samples are exposed to the medium from both sides and the maximum penetration depth is 1.5 mm into the 3 mm thick samples.
Results
Penetration depth of CIO2
Samples of PVDF were first immersed in 7 g/l CIO2 for 17 hours and then microtome slices were cut from the cross-sections and treated with methyl red solution, as described in the experimental part. From the pictures taken it is clear that the penetration depth is reduced substantially by the addition of Irganox 1010 to the sample. It also seems as if the boundary between the
Clθ2-affected part and the unaffected core is sharper in the sample with the additive.
By using the colour analysis program, the concentration of chlorine dioxide can be plotted as a function of penetration depth for the two samples, treated by immersion in 7 g/l CIO2 solution at 50 0C for 17 hours. One sample contained no additive and the second sample contained 1 wt% Irganox 1010. The results are shown in Figure 3.
The plots in Figure 3 show that the profile of the penetration depth is much sharper for the sample with additive than in the one without. In the sample without additive CIO2 has penetrated 0.8 mm while in the sample with 1 wt% Irganox 1010 the penetration depth is only 0.3 mm. To verify that these results are really valid for the CIO2 penetration and are not due to some artefact the penetration depth was also followed using the LGB method. This method does not only give a relative concentration of CIO2 in the sample but can be used to calculate the actual amount in the material.
The results from the indicator technique shown in Figure 3 and the LGB method give about the same penetration depth of CIO2.
It was found that the addition of both Irganox 1330 and Chimasorb 944 gave about the same effect on the diffusion rate as Irganox 1010 as can be seen in Figure 4. Observe that the data in Figure 4 are for a 24 hour exposure at 500C while the previously presented data shown in Figure 3 were from a 17 hour exposure.
When plotting the penetration depth as a function of the concentration of Irganox 1010 it was found to be linear. An extrapolation indicated that an addition of a bit more than 2 wt% Irganox 1010 would result in no penetration at all of CIO2.
Consumption of additive
During the reaction between Irganox 1010 and chlorine dioxide the hindered phenol is destroyed. Normally the detection limit for IR-spectroscopy is quite high and it is difficult to detect low concentrations of additives. However, due to the fact that the hindered phenol group has an IR-absorption in a region where it does not overlap with the PVDF polymer, it was found that it was possible to detect the additive with FTIR. Experiments on ECTFE with 1 wt%
Irganox 1010 have shown that it is only the hindered phenol group that decreases and not the ester.
Exposure in CIO2 stripper at Aspa bruk
Test pieces of PVDF were also exposed 50 days in the CIO2 stripper at Aspa bruk. The temperature was 58 0C and the CIO2 concentration about 1.4 g/l. When examining the pieces with indicator solution it was found that the CIO2 had permeated all the way through all samples except the ones with 0.5 and 1 wt% of additive. In the samples containing the additive no blisters, no other deterioration nor any negative effect on material properties were observed.
Exposure in the primary CIO2 reactor at the Skarblacka mill
Test pieces of PVDF with different concentrations of Irganox 1010 were also exposed for one year in the primary chlorine dioxide reactor at the Skarblacka mill. The temperature was 58 0C and the CIO2 concentration around 2.6 g/l.
It was found that the sample without any stabiliser was so brittle that it had fallen apart during the exposure. The addition of Irganox 1010 made the material less susceptible to this attack. Table 2 lists the amount of degraded material in the samples for different concentrations of additive. Above 0.5
wt% no degradation could be found at all. Chlorine dioxide had penetrated all the way through all the samples. For the samples with 0.5 and 1 wt% additive, no blisters, no other deterioration nor any negative effect on material properties were observed after being exposed for one year. It seems that a higher stability was obtained by the additive.
Table 2. Amount of degraded material in the samples with different concentration of additive after exposure for one year in the primary CIO2 reactor at the Skarblacka mill.
Exposure in the pulp/CIO2 inlet line at the Skarblacka mill
Exposure of test pieces of PVDF with 1 wt% Irganox 1010 and 1330 and Chimasorb 944 and without additive was made in a test station in the by-pass line for pulp/CIO2 inlet line to the D0 stage bleach tower at the Skarblacka mill. The temperature is 68-75°C and the chlorine dioxide charge is 20 kg CIO2 (as active chlorine) per ton pulp and the pulp consistency is 5%. The samples were exposed for 6 months.
The chlorine dioxide had penetrated all the way through the sample without additive and had only just penetrated into the middle of the one with Chimasorb 944. In the samples with 1 wt% Irganox 1010 or 1330 the diffusion of chlorine dioxide had been slowed down so much that both showed a penetration depth of only 1 mm. This confirms that the addition of
the additive is slowing down the diffusion through the fluoroplastic also in an industrial environment and that it does not influence the material in a negative way even after as long exposure times as 6 months. It also shows that the hindered phenols are more active than the hindered amine.
Exposure in hot wet CI2-gas at the chlorine plant in Skoghall
Test pieces of PVDF with 1 wt% Irganox 1010 and 1330 and without additive were exposed in hot (75-85 0C) wet chlorine gas at the chlorine plant in
Skoghall for 6 months. It was found that the chlorine had permeated all the way through all the samples but it was also seen that the Irganox had been consumed in the samples with the additive. This indicates that the diffusion rate had been decreased for these samples due to the chemical reaction between the chlorine and the hindered phenol. It was also found that the
PVDF sample without additive showed an internal layer with cracks due to degraded material. This was not found in the samples with additive and just as for the other industrially exposed samples, no blisters nor any other negative effect on material properties were observed in these samples after the exposure.
Penetration depth of HCIO
To test if the very promising results of slowing down the diffusion of chlorine dioxide by the addition of Irganox 1010 to PVDF also are applicable to other chlorine species the samples were exposed to a HCIO solution at pH 5.5. Figure 5 shows the profiles from the reaction with the indicator solution after the sample exposure.
As can be seen in the figure the penetration depth is greatly affected by the additive.
Figure 6 is a diagram showing Arrhenius plots of the temperature dependence showing the negative logarithm of the diffusion coefficient D as a function of the reciprocal absolute temperature. The higher the value of neg Log D the slower the diffusion. As can be seen in the figure PVDF with Irganox 1330 and Irganox 1010 are, within the experimental error, more or less as efficient throughout the whole temperature range. The hindered amine Chimasorb 944 is a bit less efficient and PVDF without additive shows the highest diffusion rate. It is interesting to note that the slope of the lines is about the same for all mixes, which means that the activation energy is the same. From this it can be concluded that it is the activation energy for the diffusion which is rate determining, i.e. slower than the reaction between the additives and CIO2.
Lastly, Figure 7 shows the effect of the concentration of the chlorine dioxide solution on the penetration depth in the PVDF containing 1 wt% Irganox 1010. The samples were immersed in the Clθ2-solution at 5O0C for 24 hours. The concentrations used were 3 g/l (cone 1/1 ), 0.3 g/l (cone 1/10) and 0.03 g/l (cone 1/100), respectively.
Discussion
It is obvious from the results that an addition of as low as 0.1 wt% Irganox 1010 can slow down the penetration rate of chlorine dioxide and HCIO solution. FTIR data show that there is a consumption of the hindered phenol.
It was also found that another hindered phenol, Irganox 1330, gave the same effect as Irganox 1010. This confirms that it is the phenol group that is the active site. Also the hindered amine Chimasorb 944 slows down the diffusion by reacting with the CIO2 and HCIO.
The exposures in the stripper at Aspa bruk and in the pulp/CIO2 inlet line at the Skarblacka mill show that the addition of reactive additives such as Irganox 1010 does slow down the penetration of CIO2 also in an industrial environment and for longer ageing times. No blisters or negative effects on material properties were observed.
The exposure in hot wet C^-gas at the chlorine plant in Skoghall shows that the hindered phenols also react with CI2 and by this slows down the penetration rate through the material. It was also found that it prevents the material from forming an internal brittle layer.
The reactive additive also stabilised the samples against degradation when exposed in a chlorine dioxide reactor. Addition of at least 0.5 wt% Irganox 1010 completely prevented the degradation of PVDF when exposed for one year.
It seems that the effect of the additive is even higher against HCIO than CIO2. For HCIO it is, however, not clear exactly what the penetrating species is. HCIO is a complex mixture of chlorine species and the composition depends on the pH value and the temperature.
Conclusions
It is possible to slow down the diffusion of chlorine, chlorine dioxide and HCIO in fluoroplastics such as PVDF by adding a reactive additive having reactive groups, such as a hindered phenol.
Further, a stabilization of fluoriplastics such as PVDF and ECTFE in a chlorine dioxide reactor may be obtained by such an additive.
The above discussion and experiments performed mainly on PVDF using some special reactive additives are valid for fluoroplastics in general and in general for any reactive additive with groups which can react with the penetrant.
Claims
1. A process of slowing down diffusion of an element or a compound through a fluoroplastic comprising the addition of a reactive additive having reactive groups that react with the element or compound.
2. A process according to claim 1 wherein the element or compound is chlorine or a chlorine compound such as chlorine dioxide or hypochloric acid.
3. A process of preventing degradation of the fluoroplastics PVDF and ECTFE used in, or in connection with a reactor where chlorine dioxide is produced comprising mixing the fluoroplastic with a reactive additive having reactive groups.
4. A process according to any of claims 1-3, wherein the reactive additive is a hindered phenol or hindered amine.
5. A process according to claim 4, wherein the reactive additive has one of the formulas:
6. A process according to any of claims 1-5, wherein the fluoroplastic is to be used as liner on a tank or pipe of steel or FRP.
7. A process according to any of claims 1-6, wherein at least 0.1 wt% additive is used.
8. A process according to claim 7, wherein at least 0.5 wt%, preferably at least 1 wt%, additive is used, especially between about 1 and 2 wt%.
9. A process according to any of claims 1-8, wherein such an amount of reactive additive is used as to give the fluoroplastic a concentration of reactive groups of at least 6 mmol/g, preferably at least 30 and especially at least 60 mmol/g.
10. A diffusion resistant fluoroplastic which comprises a reactive additive having reactive groups that react with an element and/or compound to which the fluoroplastic is diffusion resistant.
11. A diffusion resistant fluoroplastic according to claim 10, wherein the element or compound is chlorine and/or a chlorine compound such as chlorine dioxide or hypochloric acid.
12.A diffusion resistant fluoroplastic according to claim 10 or 11 , wherein the reactive additive is a hindered phenol or hindered amine.
13.A diffusion resistant fluoroplastic according to claim 12, wherein the reactive additive has one of the formulas:
14. A diffusion resistant fibroplastic according to any of claims 10-13, comprising at least 0.1 wt% additive.
15.A diffusion resistant fluoroplastic according to claim 14, comprising at least 0.5 wt% additive, preferably at least 1 wt% additive, especially comprising between about 1 and 2 wt% additive.
16.A diffusion resistant fluoroplastic according to any of claims 10-15, comprising such an amount of additive as to give the fluoroplastic a concentration of reactive groups of at least 6 mmol/g, preferably at least 30 and especially at least 60 mmol/g.
17.A diffusion resistant fluoroplastic according to any of claims 1-16 which is essentially free from alkali metal formate, inorganic non- metallic reducing agent, aliphatic polyol, and glycidyl methacrylate polymer.
18. The use of a reactive compound having reactive groups as an additive in a fluoroplastic to prevent or slow down the diffusion through the fluoroplastic of an element and/or a compound that reacts with the the reactive groups.
19. The use according to claim 18, wherein the element or compound is chlorine and/or a chlorine compound such as chlorine dioxide or hypochloric acid.
20. The use of a reactive compound having reactive groups as an additive in the fluoroplastics PVDF and ECTFE utilized in, or in connection with a reactor for producing chlorine dioxide to prevent or slow down degradation of the fluoroplastic.
21. The use according to any of claims 18-20, wherein the reactive compound having reactive groups is a hindered phenol or amine.
22. The use according to any of claims 18-21 , wherein the flouroplastic is used as liner on a tank or pipe of steel or FRP.
23. The use according to any of claims 18-22 wherein at least 0.1 wt% additive, preferably at least 0.5 wt% additive and most preferably at least 1 wt% additive is used in the fluoroplastic.
24. The use according to any of claims 18-23, wherein such an amount of hindered phenol or amine is used as additive as to give the fluoroplastic a concentration of reactive groups of at least 6 mmol/g, preferably at least 30 and especially at least 60 mmol/g.
25. The use according to any of claims 18-24, wherein the hindered phenol or amine has one of the formulas:
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/526,698 US20100093945A1 (en) | 2007-02-23 | 2008-02-25 | Diffusion retardation in fluoroplastics |
EP08712836A EP2125979A4 (en) | 2007-02-23 | 2008-02-25 | Diffusion retardation in fluoroplastics |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE0700448A SE531642C2 (en) | 2007-02-23 | 2007-02-23 | Diffusion delay in fluorine plastics |
SE0700448-4 | 2007-02-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2008103128A1 true WO2008103128A1 (en) | 2008-08-28 |
Family
ID=39710317
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SE2008/050208 WO2008103128A1 (en) | 2007-02-23 | 2008-02-25 | Diffusion retardation in fluoroplastics |
Country Status (4)
Country | Link |
---|---|
US (1) | US20100093945A1 (en) |
EP (1) | EP2125979A4 (en) |
SE (1) | SE531642C2 (en) |
WO (1) | WO2008103128A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2199330A1 (en) * | 2008-12-22 | 2010-06-23 | Borealis AG | Polyolefin composition for water pipes with good resistance to chlorine dioxide and low migration |
EP2199327A1 (en) * | 2008-12-22 | 2010-06-23 | Borealis AG | Polyolefin composition for water pipes with increased resistance to chlorine dioxide |
EP2690115A1 (en) | 2012-07-24 | 2014-01-29 | Borealis AG | Slow partial cross-linking polyolefin composition for improving disinfectant resistance of an article |
CN103649197A (en) * | 2011-07-25 | 2014-03-19 | 北欧化工股份公司 | Polyolefin composition for pipes and fittings with increased resistance to chlorine dioxide |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3557050A (en) | 1967-03-08 | 1971-01-19 | Daikin Ind Ltd | Stabilized vinyl fluoride polymers |
US3557051A (en) | 1967-04-03 | 1971-01-19 | Daikin Ind Ltd | Stabilized vinyl fluoride polymers |
US3755496A (en) * | 1971-07-01 | 1973-08-28 | Daikin Ind Ltd | Coating compositions |
US3775496A (en) | 1972-08-09 | 1973-11-27 | Sun Research Development | Preparation of 2,6-dimethylnaphthalene and 2,7-dimethylnaphthalene |
US4478965A (en) * | 1982-05-20 | 1984-10-23 | E. I. Du Pont De Nemours And Company | Melt processable perfluorocarbon resin with degradation retarder |
WO1990008805A1 (en) * | 1989-01-25 | 1990-08-09 | Raychem Corporation | Fluoropolymer compositions |
US5328948A (en) * | 1992-09-23 | 1994-07-12 | Ausimont, U.S.A., Inc. | Stabilization of halopolymers with ionomers |
WO2003106736A2 (en) * | 2001-01-02 | 2003-12-24 | Halox Technologies, Inc. | Electrolytic process and apparatus |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4539354A (en) * | 1981-07-06 | 1985-09-03 | Allied Corporation | Stabilized ethylene/chlorotrifluoroethylene copolymer composition |
GB9902758D0 (en) * | 1999-02-08 | 1999-03-31 | H B Fuller Coatings Ltd | Heat transfer element |
US20060264540A1 (en) * | 2005-05-19 | 2006-11-23 | Gelbin Michael E | Stabilizer blend for improved chlorine resistance |
-
2007
- 2007-02-23 SE SE0700448A patent/SE531642C2/en not_active IP Right Cessation
-
2008
- 2008-02-25 EP EP08712836A patent/EP2125979A4/en not_active Withdrawn
- 2008-02-25 US US12/526,698 patent/US20100093945A1/en not_active Abandoned
- 2008-02-25 WO PCT/SE2008/050208 patent/WO2008103128A1/en active Application Filing
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3557050A (en) | 1967-03-08 | 1971-01-19 | Daikin Ind Ltd | Stabilized vinyl fluoride polymers |
US3557051A (en) | 1967-04-03 | 1971-01-19 | Daikin Ind Ltd | Stabilized vinyl fluoride polymers |
US3755496A (en) * | 1971-07-01 | 1973-08-28 | Daikin Ind Ltd | Coating compositions |
US3775496A (en) | 1972-08-09 | 1973-11-27 | Sun Research Development | Preparation of 2,6-dimethylnaphthalene and 2,7-dimethylnaphthalene |
US4478965A (en) * | 1982-05-20 | 1984-10-23 | E. I. Du Pont De Nemours And Company | Melt processable perfluorocarbon resin with degradation retarder |
WO1990008805A1 (en) * | 1989-01-25 | 1990-08-09 | Raychem Corporation | Fluoropolymer compositions |
US5328948A (en) * | 1992-09-23 | 1994-07-12 | Ausimont, U.S.A., Inc. | Stabilization of halopolymers with ionomers |
WO2003106736A2 (en) * | 2001-01-02 | 2003-12-24 | Halox Technologies, Inc. | Electrolytic process and apparatus |
Non-Patent Citations (1)
Title |
---|
See also references of EP2125979A4 |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2009331890B2 (en) * | 2008-12-22 | 2012-11-29 | Borealis Ag | Polyolefin composition for water pipes with increased resistance to chlorine dioxide |
EP2199330A1 (en) * | 2008-12-22 | 2010-06-23 | Borealis AG | Polyolefin composition for water pipes with good resistance to chlorine dioxide and low migration |
WO2010072374A1 (en) * | 2008-12-22 | 2010-07-01 | Borealis Ag | Polyolefin composition for water pipes with increased resistance to chlorine dioxide |
WO2010072373A1 (en) | 2008-12-22 | 2010-07-01 | Borealis Ag | Polyolefin composition for water pipes with good resistance to chlorine dioxide and low migration |
CN102257053A (en) * | 2008-12-22 | 2011-11-23 | 博里利斯股份公司 | Polyolefin composition for water pipes with increased resistance to chlorine dioxide |
CN102257054A (en) * | 2008-12-22 | 2011-11-23 | 博里利斯股份公司 | Polyolefin composition for water pipes with good resistance to chlorine dioxide and low migration |
EP2199327A1 (en) * | 2008-12-22 | 2010-06-23 | Borealis AG | Polyolefin composition for water pipes with increased resistance to chlorine dioxide |
AU2009331889B2 (en) * | 2008-12-22 | 2013-05-02 | Borealis Ag | Polyolefin composition for water pipes with good resistance to chlorine dioxide and low migration |
US8969445B2 (en) | 2008-12-22 | 2015-03-03 | Borealis Ag | Polyolefin composition for water pipes with good resistance to chlorine dioxide and low migration |
KR101307161B1 (en) * | 2008-12-22 | 2013-09-11 | 보레알리스 아게 | Polyolefin Composition for Water Pipes with Increased Resistance to Chlorine Dioxide |
US8443846B2 (en) | 2008-12-22 | 2013-05-21 | Borealis Ag | Polyolefin composition for water pipes with increased resistance to chlorine dioxide |
CN103649197A (en) * | 2011-07-25 | 2014-03-19 | 北欧化工股份公司 | Polyolefin composition for pipes and fittings with increased resistance to chlorine dioxide |
WO2014015923A1 (en) | 2012-07-24 | 2014-01-30 | Borealis Ag | Slow partial cross-linking polyolefin composition for improving disinfectant resistance of an article |
EP2690115A1 (en) | 2012-07-24 | 2014-01-29 | Borealis AG | Slow partial cross-linking polyolefin composition for improving disinfectant resistance of an article |
Also Published As
Publication number | Publication date |
---|---|
SE0700448L (en) | 2008-08-24 |
SE531642C2 (en) | 2009-06-16 |
EP2125979A4 (en) | 2011-03-16 |
US20100093945A1 (en) | 2010-04-15 |
EP2125979A1 (en) | 2009-12-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US9200136B2 (en) | Chlorine dioxide resistant polyethylene pipes, their preparation and use | |
EP0672214B1 (en) | Stabilized porous pipe | |
EP2729232B1 (en) | CO2 capture in an polypropylene absorption column comprising an antioxidant | |
EP2125979A1 (en) | Diffusion retardation in fluoroplastics | |
EP2820084B1 (en) | Composition of polyvinylidene fluoride | |
JP6253594B2 (en) | Polyvinyl chloride (PVC) composition for the manufacture of pipes, ducts, containers, plates, molded parts or welding rods, pipes, ducts or containers containing such PVC compositions, or such PVC compositions, pipes, ducts or Container use | |
MX2013001372A (en) | Melt-fabricable tetrafluoroethylene/perfluoro (alky vinyl ether) copolymer composition having improved heat aging property. | |
US8648147B2 (en) | Melt-fabricable perfluoropolymers having improved heat aging property | |
US20040054050A1 (en) | Compositions based on polyvinylidene fluoride | |
JP5174920B2 (en) | Composition of at least one vinylidene chloride copolymer | |
KR100627122B1 (en) | Chlorinated vinyl chloride-based resin and molded articles | |
KR20220080153A (en) | Process for the preparation of fluoropolymers and fluoroelastomers in the presence of non-fluorinated sulfonate type hydrocarbon containing surfactants thereof | |
CN108929477A (en) | Resistance to discoloration high strength polyethylene tubing of one kind and preparation method thereof | |
JP6868931B2 (en) | Hard products, components, pipes, and fittings in nuclear equipment | |
JP4555494B2 (en) | Vinyl chloride resin composition | |
Bredacs | Aging Mechanism and Material Ranking of PE Pipe Grades in Aqueous Chlorine Dioxide and Hypochlorite Solutions | |
US20240066827A1 (en) | Composite thermoplastic material for composite tubular structures | |
KR102113330B1 (en) | Fluororesin composite for tube with good extrusion properties | |
US20230391924A1 (en) | Fluorine-containing copolymer, injection molded article, wire coating material and wire | |
EP4299610A1 (en) | Copolymer, molded body, extruded body, and transfer molded body | |
US20130123429A1 (en) | Melt-Fabricable Tetrafluoroethylene/perfluoro(alkyl vinyl ether) Copolymer Having Improved Heat Aging Property | |
Hamma et al. | Assessment of Polyethylene Geomembrane Properties after Accelerated Thermal Ageing. | |
EP4299603A1 (en) | Copolymer, molded body, injection molded body, and coated electrical wire | |
EP4299609A1 (en) | Copolymer, molded body, extruded body, and transfer molded body | |
EP4219569A1 (en) | Acetoacetyl group-containing poly(vinyl alcohol)-based resin and method for producing acetoacetyl group-containing poly(vinyl alcohol)-based resin |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 08712836 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2008712836 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 12526698 Country of ref document: US |