USH1309H - Phosphazene polymer containing composites and method for making phosphazene polymer containing composites - Google Patents
Phosphazene polymer containing composites and method for making phosphazene polymer containing composites Download PDFInfo
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- USH1309H USH1309H US07/559,234 US55923490A USH1309H US H1309 H USH1309 H US H1309H US 55923490 A US55923490 A US 55923490A US H1309 H USH1309 H US H1309H
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- United States
- Prior art keywords
- composite material
- phosphazene
- reinforcing material
- composite
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- 239000002131 composite material Substances 0.000 title claims abstract description 67
- GKTNLYAAZKKMTQ-UHFFFAOYSA-N n-[bis(dimethylamino)phosphinimyl]-n-methylmethanamine Chemical compound CN(C)P(=N)(N(C)C)N(C)C GKTNLYAAZKKMTQ-UHFFFAOYSA-N 0.000 title description 39
- 229920000642 polymer Polymers 0.000 title description 21
- 238000000034 method Methods 0.000 title description 19
- 239000012779 reinforcing material Substances 0.000 claims abstract description 37
- -1 phosphazene compound Chemical class 0.000 claims abstract description 17
- 239000000126 substance Substances 0.000 claims abstract description 13
- 239000011248 coating agent Substances 0.000 claims abstract description 5
- 238000000576 coating method Methods 0.000 claims abstract description 5
- 239000011521 glass Substances 0.000 claims description 16
- 229920002627 poly(phosphazenes) Polymers 0.000 claims description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 11
- 239000000835 fiber Substances 0.000 claims description 10
- 229910002804 graphite Inorganic materials 0.000 claims description 9
- 239000010439 graphite Substances 0.000 claims description 9
- 239000000470 constituent Substances 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 125000003545 alkoxy group Chemical group 0.000 claims description 2
- 125000000217 alkyl group Chemical group 0.000 claims description 2
- 125000003118 aryl group Chemical group 0.000 claims description 2
- 125000004104 aryloxy group Chemical group 0.000 claims description 2
- 125000000467 secondary amino group Chemical group [H]N([*:1])[*:2] 0.000 claims description 2
- 125000003396 thiol group Chemical group [H]S* 0.000 claims description 2
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- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims 1
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- 230000000379 polymerizing effect Effects 0.000 abstract description 3
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 18
- 230000008569 process Effects 0.000 description 18
- 238000005470 impregnation Methods 0.000 description 17
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- 239000002904 solvent Substances 0.000 description 7
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
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- UBIJTWDKTYCPMQ-UHFFFAOYSA-N hexachlorophosphazene Chemical compound ClP1(Cl)=NP(Cl)(Cl)=NP(Cl)(Cl)=N1 UBIJTWDKTYCPMQ-UHFFFAOYSA-N 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
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- 238000006243 chemical reaction Methods 0.000 description 4
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- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 239000004312 hexamethylene tetramine Substances 0.000 description 3
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
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- DZKXDEWNLDOXQH-UHFFFAOYSA-N 1,3,5,2,4,6-triazatriphosphinine Chemical class N1=PN=PN=P1 DZKXDEWNLDOXQH-UHFFFAOYSA-N 0.000 description 2
- PEJQKHLWXHKKGS-UHFFFAOYSA-N 2,2,4,4,6,6,8,8-octachloro-1,3,5,7-tetraza-2$l^{5},4$l^{5},6$l^{5},8$l^{5}-tetraphosphacycloocta-1,3,5,7-tetraene Chemical compound ClP1(Cl)=NP(Cl)(Cl)=NP(Cl)(Cl)=NP(Cl)(Cl)=N1 PEJQKHLWXHKKGS-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000012300 argon atmosphere Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- IMHDGJOMLMDPJN-UHFFFAOYSA-N biphenyl-2,2'-diol Chemical compound OC1=CC=CC=C1C1=CC=CC=C1O IMHDGJOMLMDPJN-UHFFFAOYSA-N 0.000 description 2
- 125000001309 chloro group Chemical group Cl* 0.000 description 2
- 229910003460 diamond Inorganic materials 0.000 description 2
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- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 description 2
- 229920001903 high density polyethylene Polymers 0.000 description 2
- 239000004700 high-density polyethylene Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
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- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 2
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- 230000005855 radiation Effects 0.000 description 2
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- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 2
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- 239000010959 steel Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
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- MQCPOLNSJCWPGT-UHFFFAOYSA-N 2,2'-Bisphenol F Chemical compound OC1=CC=CC=C1CC1=CC=CC=C1O MQCPOLNSJCWPGT-UHFFFAOYSA-N 0.000 description 1
- DBFHCPVZZSVFJL-UHFFFAOYSA-N 3-[2-(3-hydroxyphenoxy)ethoxy]phenol Chemical compound OC1=CC=CC(OCCOC=2C=C(O)C=CC=2)=C1 DBFHCPVZZSVFJL-UHFFFAOYSA-N 0.000 description 1
- VPWNQTHUCYMVMZ-UHFFFAOYSA-N 4,4'-sulfonyldiphenol Chemical compound C1=CC(O)=CC=C1S(=O)(=O)C1=CC=C(O)C=C1 VPWNQTHUCYMVMZ-UHFFFAOYSA-N 0.000 description 1
- NZGQHKSLKRFZFL-UHFFFAOYSA-N 4-(4-hydroxyphenoxy)phenol Chemical compound C1=CC(O)=CC=C1OC1=CC=C(O)C=C1 NZGQHKSLKRFZFL-UHFFFAOYSA-N 0.000 description 1
- BRPSWMCDEYMRPE-UHFFFAOYSA-N 4-[1,1-bis(4-hydroxyphenyl)ethyl]phenol Chemical compound C=1C=C(O)C=CC=1C(C=1C=CC(O)=CC=1)(C)C1=CC=C(O)C=C1 BRPSWMCDEYMRPE-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 241001274658 Modulus modulus Species 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- 229920000265 Polyparaphenylene Polymers 0.000 description 1
- 101100386054 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) CYS3 gene Proteins 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 125000000746 allylic group Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
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- 230000005540 biological transmission Effects 0.000 description 1
- VCCBEIPGXKNHFW-UHFFFAOYSA-N biphenyl-4,4'-diol Chemical compound C1=CC(O)=CC=C1C1=CC=C(O)C=C1 VCCBEIPGXKNHFW-UHFFFAOYSA-N 0.000 description 1
- 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 1
- 238000001460 carbon-13 nuclear magnetic resonance spectrum Methods 0.000 description 1
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- 150000001875 compounds Chemical class 0.000 description 1
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- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- VILAVOFMIJHSJA-UHFFFAOYSA-N dicarbon monoxide Chemical compound [C]=C=O VILAVOFMIJHSJA-UHFFFAOYSA-N 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
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- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- SLGWESQGEUXWJQ-UHFFFAOYSA-N formaldehyde;phenol Chemical compound O=C.OC1=CC=CC=C1 SLGWESQGEUXWJQ-UHFFFAOYSA-N 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 101150074899 gpa-10 gene Proteins 0.000 description 1
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- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
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- 229920002866 paraformaldehyde Polymers 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 125000000951 phenoxy group Chemical group [H]C1=C([H])C([H])=C(O*)C([H])=C1[H] 0.000 description 1
- 238000001394 phosphorus-31 nuclear magnetic resonance spectrum Methods 0.000 description 1
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- 239000002244 precipitate Substances 0.000 description 1
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- 150000003141 primary amines Chemical group 0.000 description 1
- OVARTBFNCCXQKS-UHFFFAOYSA-N propan-2-one;hydrate Chemical compound O.CC(C)=O OVARTBFNCCXQKS-UHFFFAOYSA-N 0.000 description 1
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
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Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/009—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
- C04B41/4584—Coating or impregnating of particulate or fibrous ceramic material
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
- C04B41/46—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with organic materials
- C04B41/49—Compounds having one or more carbon-to-metal or carbon-to-silicon linkages ; Organo-clay compounds; Organo-silicates, i.e. ortho- or polysilicic acid esters ; Organo-phosphorus compounds; Organo-inorganic complexes
- C04B41/4994—Organo-phosphorus compounds
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F11/00—Chemical after-treatment of artificial filaments or the like during manufacture
- D01F11/10—Chemical after-treatment of artificial filaments or the like during manufacture of carbon
- D01F11/12—Chemical after-treatment of artificial filaments or the like during manufacture of carbon with inorganic substances ; Intercalation
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F11/00—Chemical after-treatment of artificial filaments or the like during manufacture
- D01F11/10—Chemical after-treatment of artificial filaments or the like during manufacture of carbon
- D01F11/14—Chemical after-treatment of artificial filaments or the like during manufacture of carbon with organic compounds, e.g. macromolecular compounds
Definitions
- the present invention relates generally to phosphazene polymer composites and a method for producing phosphazene polymer composites.
- Composite matrix materials comprised of reinforcing materials and organic binding resins, long have been used to provide alternatives to more typical man-made and natural materials.
- organic compounds as high density polyethylene, polypropylene, polycarbonate, polymethylmethacrylate and polystyrene are examples of resins that, when incorporated as binders into composites, provide materials for fabrication in a myriad of applications.
- the tendency of organic polymers to burn readily, soften at moderate temperatures, or swell in contact with organic solvents limits their use in extreme environmental conditions. As such, many organic polymer-containing composites generally lack the thermal, chemical, and biological stability and the radiation resistance needed for widespread application.
- Phosphazene polymer materials are stable from approximately 80° C. to 250° C. and, with proper modification, can be made stable up to approximately 500° C. In addition, these polymers are resistant to most organic materials and are stable over a wide pH range. These materials are also resistant to ultraviolet and gamma radiation and biological attack.
- the general chemical formula for phosphazene is as follows: ##STR1## where n is a number greater than 1.
- a feature of phosphazene-containing composites is their superior stiffness, thermal stability, and hardness which is lacking in more typical composite constituents.
- An advantage of using phosphazene composites is a wider range of applications for phosphazene composites, including uses in harsh environments.
- Another object of the present invention provides a method for producing phosphazene-containing composite materials through a pultrusion process.
- a composite produced by first coating a reinforcing material with an inorganic phosphazene compound and then polymerizing the phosphazene compound so as to confer superior thermal, physical and chemical resistance qualities to the composite.
- a phosphazene-containing composite is provided whereby phosphazene imparts superior thermal, physical and chemical resistance to a reinforcing material.
- FIG. 1 is a diagram of an exemplary process illustrating the present invention.
- FIG. 2 is the chemical formula for a fiber-coating matrix component of the invention comprising hexa-p-hydroxyphenoxycyclotriphosphazene molecules interconnected by phenol formaldehyde linkages.
- FIG. 1 there is shown a method for producing a composite material of the invention through a pultrusion process generally designated by the reference numeral 20.
- the pultrusion process 20 combines a reinforcing material 21 with a phosphazene polymer, such as the phosphazene polymer having the chemical formula shown in FIG. 2.
- the pultrusion process 20 gets its name from the fact that the reinforcing material 21 is literally pulled through the entire process 20. There are generally nine stages involved in the process 20, namely a spooling-off stage 22, a tensioning system 24, a polymer impregnation bath stage 26, a drying process 28, a shaping stage 30, a puller 31, a take-up spool 34, a sizing stage 36, and a polymerization stage 38.
- the pultrusion process 20 begins when the reinforcing material 21 is supplied in the spooling-off stage 22. The reinforcing material 21 is then directed into the impregnation bath 26 via the tensioning system 24.
- a prepolymeric substituted phosphazene molecule dissolved in a suitable solvent mixture is contained in the impregnation bath 26. Constituents of the solvent mixture depend on which substitution groups are attached to the phosphazene molecule; different substitution groups require different reactants and solvents.
- the coated reinforcing material 21 is pulled through the bath 26, then the coated reinforcing material is dried in the drying process 28 to remove the solvents. Next, the coated reinforcing material 21 is subjected to a shaping stage 30 to form it into a desired configuration in preparation for the sizing stage 36 and the final polymerization stage 38. Upon polymerizing with heat and pressure, the final composite 42 is produced.
- the reinforcing material 21 is supplied via the spooling-off stage 22.
- the spooling-off stage 22 is controlled by a small gear, unwinding motor (not shown).
- the unspooling speed is controlled by the position of a dancer arm 25 in the tensioning system 24 to maintain a smooth and even spool off.
- the tensioning system 24 serves to apply the tension to the reinforcing material 21 and to control the speed of the unwinding of the reinforcing material 21. Both of the functions are accomplished simultaneously with the use of a dancer-arm-regulated system.
- the weight of the dancer arm 25 controls the tension applied to the reinforcing material 21.
- the dancer arm 25 is also part of an electrical feedback system (not shown) which regulates the speed of spool off. For example, as the dancer arm 25 is raised, the speed of the small gear unwinder motor increases. When the dancer arm 25 is horizontal, the speed of the small gear unwinder motor matches the required speed of the reinforcing material 21 entering the next step of the pultrusion process 20, which is the impregnation bath stage 26.
- the major constituent contained in the impregnation bath stage 26 is a prepolymeric phosphazene compound which is produced separately from the pultrusion process 20. This prepolymer coats the reinforcing material 21 during the impregnation bath state 26 and is later polymerized.
- a base unsubstituted phosphazene polymer such as hexachlorocyclotri-phosphazene, which has two chlorine atoms attached to each phosphorous
- suitable difunctional monomers can be selected from alkyl groups, aryl groups, aryloxy groups, alkoxy groups, primary amine groups, secondary amine groups, and mercapto groups.
- An exemplary list of such difunctional monomers follows:
- Hexa-p-hydroxyphenoxycyclotriphosphazene has the following chemical formula: ##STR3##
- Cyclomatrix or rigid polymers of phosphazene are hard thermosetting resins having limited solubility that can be employed to produce rigid composite structures having thermal stability up to approximately 500° C.
- Composites incorporating cyclomatrix polymers exhibit superior resistance to acids and bases and to all solvents when cured.
- the linear or ductile phosphazene polymers can be used. These flexible thermoplastic elastomers produce composites that exhibit a useful temperature range of 80° C. to 250° C. while exhibiting selected solubilities to various solvents. These more ductile composites exhibit good resistance to bases and some acids and most solvents. Good resistance is displayed to ketones, alcohols, and aliphatic hydrocarbons.
- a combination of rigid and elastic properties can be achieved by incorporating cyclolinear phosphazene molecules as the flexible thermoplastic elastomers or thermoplastic resins required to provide semi-rigid composite structures having thermal integrity up to 350° C.
- the phosphazene-to-difunctional monomer mole ratio is 6-to-1, as it is sought that all six chlorine atoms be removed from each unsubstituted phosphazene molecule.
- Isolation and purification of the hydroquinone prepolymer are effected by dissolving the amber solid in 500 ml of hot 80 percent acetic acid. After the light amber solution is allowed to cool to room temperature, it is added to 20 liters of deionized water, resulting in the precipitation of the hydroquinone prepolymer as a white solid. The mixture is stirred for 30-45 minutes to allow for digestion of the precipitate. The white solid is collected by filtration and then redissolved and reprecipitated in the same fashion. The white solid collected by filtration is then washed with pH-neutral water until the rinsate is neutral.
- the washing can be performed either on the filter, yielding a white powder, or using a Soxhlet extractor, yielding an off-white, compressed mass.
- the solid is then dried by gentle warming; a period of three to four days can be necessary to drive off all of the entrapped water, and no color change is observed during this time.
- the resultant dry mass typically weighs 130 grams for a yield of about 70 percent, based on the amount of phosphonitrilic chloride starting material.
- the polymer impregnation bath stage 26 where the prepolymer, formulated in the above process, is applied to the reinforcing material 21.
- the purpose of the impregnation bath stage 26 is to coat the reinforcing material 21 with the prepolymeric substituted phosphazene compound in preparation for the subsequent polymerization stage 38, whereby the prepolymeric substituted phosphazene molecules are polymerized or linked together.
- the preparation of the impregnation liquor in the impregnation bath stage 26 is dependant upon the type of difunctional monomer chosen in the substitution reaction with the base, unsubstituted, phosphazene polymer hexachlorocyclotriphosphazene. If a diol, such as hydroquinone, is substituted at the phosphorous sites, then linking of adjacent phosphazene molecules will have to be facilitated by exposing the ring to a nucleophilic carbon, such as that found on formaldehyde. The formaldehyde, then, or some other carbonyl carbon source, would have to be supplied sometime before or during the polymerization process.
- a number of suitable compounds can serve as the needed cross linking agent.
- a hexamethylenetetramine, formalin and paraformaldehyde can serve as the needed cross linking agent.
- difunctional monomers include allyl alcohol, hexamethylenediamine and the glycols.
- the resulting prepolymer hexa-p-hydroxyphenoxycyclotriphosphazene formulated in the above process, is then dissolved in a suitable solvent, in approximately a 2 to 1 mole ratio with hexamethylenetetramine.
- the hexamethylenetetramine is presented in a water-acetone mixture.
- the pressure of this reaction is maintained at 1 atmosphere.
- the resulting solution comprises the impregnation bath used to treat the reinforcement component of the composite.
- the prepolymer can also be applied as a fine powder or a liquid melt. Regardless of the process used, a desired weight percent fiber to resin mixture is 60%, plus or minus 5%.
- a myriad of types of reinforcing material including glass, oxynitride glass fibers, or carbon, such as graphite, which are typically supplied in fiberous ribbon-like or tape-like configurations, can be pulled through the impregnation bath. Any fiber thickness can be used. AS-4-12K Magnamite, by Hercules, is one example of a suitable graphite fiber type. Good results have been achieved at tape thicknesses ranging from 0.15 millimeters (mm) to 0.20 mm. The weight percent of reinforcing material 21 to total composite weight will vary, from 50 percent to 80 percent depending on the use of the final composite structure 42.
- the amount of impregnation of the reinforcing material 21 by the polymer depends on how long the reinforcing material 21 is immersed in the impregnation bath 26. Exposure times can vary, from approximately 0.25 minutes to 3 minutes. Good composites are produced when graphite fibers comprise 60 weight percent, plus or minus 5 percent of the final composite. This weight ratio is achieved when the graphite is immersed in the impregnation bath 26 of the proper concentration for approximately 30 seconds at 1 atm at room temperature.
- the solvent for example, acetone
- the drying process stage 28 can be any workable system, including, for example, such as an oven, a heated stream of air or a stream of hot inert gas.
- a stream of hot nitrogen ranging in temperature from 42° C. to 52° C. has been employed.
- any suitable system for the shaping stage 30 can be employed, for example, such as, a system of flat bars, dies or rollers to flatten the fiber-matrix composite.
- the shaped reinforcing material 39 is pulled through the pultrusion process 20 by the puller 31 and take-up means 34.
- the puller 31 can include a high torque, 100 in/oz, low speed 1.9 RPM motor for pulling the reinforcing material 21 through the process 20.
- the puller 31 can be an "S" type of puller arrangement as shown in FIG. 1 in which a spool 33 is free wheeling and the take-up spool 34 is attached to a separate puller motor (not shown) to wind up the shaped reinforcing material 39.
- the puller 31 can consist of the spools 32 and 34 with spool 32 adapted to wind the shaped reinforcing material 39 directly on the spool 34.
- the shaped reinforcing material 39 is then removed from the take-up spool 34 and cut or otherwise configured into a sized reinforcing material 40 at the sizing stage 36 in preparation for the polymerization stage 38.
- the polymerization stage 38 subjects the shaped reinforcing material 39 to heat and pressure. Heat and pressure are necessary to drive the polymerization reaction. Typically, a temperature of approximately 150° C. to 220° C. is employed. Using graphite fibers and cyclomatrix phosphazene polymers, applying heat for 5 minutes at contact pressure and for an additional 25 minutes at 5,000 psi produces a good rigid composite matrix as the resulting composite 42. If more flexible composites are desired, a blend of cyclomatrix and linear phosphazene polymers can be used. Generally, pressures can range from 100 psi to 5,000 psi.
- the polymerization stage 38 is the final step in producing the composite product 42.
- Table 1 shows the densities and percent open porosity of samples of polyphosphazene bars
- Table 2 shows the breaking strength and elasticity properties of phosphazene materials.
- the numbers in the column labelled Sample represent the identification number of the specific samples tested.
- the GPa designation represents gigaPascals and psi represents pounds per square inch.
- Shear modulus indicates the ratio of the shearing stress divided by the corresponding shear.
- Young's modulus is defined as the force in dynes per square centimeter (dynes/cm 2 ) to permanently deform a material by stretching, twisting or bending it.
- the deformation defined in the Young's Moduli standard is represented generally by the formula FL/al where F is the whole force, a the area, L the entire length of the wire or substrate, and l the extension.
- Bulk modulus is the approximate value in dynes/cm 2 between the limit of elasticity and the breaking strength of a material.
- Phosphazene polymer formulated by the above prepolymer fabrication process, also displays superior surface characteristics compared to composites formulated with organic resins.
- Table 3 depicts polyphosphazene material as having superior Rockwell Hardness characteristics compared to composite material fabricated with organic resins.
- the various composites designated as "PET-glass”, “PPO-glass”, “PC-glass”, and “ABS-glass” represent polyethyleneterephalate-glass, polyphenyleneoxide-glass, polycarbonate-glass and acrylonitrilebutadienestyrene-glass composites, respectively.
- the Rockwell Hardness of a substance is a measure of its relative hardness, based on the indentation made by a 1/16", 1/8" or 1/4" standard steel ball or a conical diamond with an apex angle of 120 degrees. Results are reported by using numbers to denote the pressure applied in kilograms, and letters are used to denote the ball or diamond producing the indentation. Accordingly, phosphazene bars withstand in excess of 120 kilograms of pressure applied by the M indentation standard, which is a 1/4 inch diameter steel ball.
- Phosphazene bars also exhibit superior stiffness properties, as shown in Table 4, below.
- Table 4 A comparison of the Young's Moduli properties of phosphazene bars with typical composites shows the relatively superior stiffness qualities of the invention.
- the resulting composite 42 exhibits unexpectedly superior qualities of hardness and elasticity.
- Table 5 depicts the flexural strength of phosphazene materials in monolithic form, for example, without reinforcement material, as well as phosphazene composite materials using carbon fiber and woven glass mat. The width and thickness of the samples are shown, as is the breaking point , designated as Break Pt, where the bar broke at the indicated pressure (given in pounds). The flexural strength of the materials is given in MPa and psi. Table 6 compares the flexural strength of a phosphazene-containing composite with more typical composite materials.
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Abstract
A composite is produced by first coating a reinforcing material with an inorganic phosphazene compound and then polymerizing the phosphazene compound so as to confer superior thermal, physical and chemical resistance qualities to the composite.
Description
The U.S. Government has rights in this invention pursuant to Contract No. DE-AC07-76ID01570 between the U.S. Department of Energy and EG&G Idaho, Inc., the operator of the Idaho National Engineering Laboratory.
1. Field of the Invention
The present invention relates generally to phosphazene polymer composites and a method for producing phosphazene polymer composites.
2. Background Art
Advances in technology continue to place more demands on existing fabricating materials. Composite matrix materials, comprised of reinforcing materials and organic binding resins, long have been used to provide alternatives to more typical man-made and natural materials. Such organic compounds as high density polyethylene, polypropylene, polycarbonate, polymethylmethacrylate and polystyrene are examples of resins that, when incorporated as binders into composites, provide materials for fabrication in a myriad of applications. However, the tendency of organic polymers to burn readily, soften at moderate temperatures, or swell in contact with organic solvents limits their use in extreme environmental conditions. As such, many organic polymer-containing composites generally lack the thermal, chemical, and biological stability and the radiation resistance needed for widespread application.
A need exists in the art for a composite material to withstand harsh environments, such as those associated with the following exemplary applications:
chemical storage or processing tanks,
pump housings,
insulators,
piping,
motor housings,
circuit boards and circuit breakers,
electrical components,
aerospace applications,
auto (under the hood) components,
transmission components,
brake components,
fuel storage tanks,
heating ducts,
wall paneling, and
light fixtures.
A need also exists to replace harmful products, such as asbestos, with a more durable, yet just as effective material.
Phosphazene polymer materials are stable from approximately 80° C. to 250° C. and, with proper modification, can be made stable up to approximately 500° C. In addition, these polymers are resistant to most organic materials and are stable over a wide pH range. These materials are also resistant to ultraviolet and gamma radiation and biological attack. The general chemical formula for phosphazene is as follows: ##STR1## where n is a number greater than 1.
It is an object of the present invention to provide a composite material which overcomes many of the disadvantages of the prior art.
It is another object of the invention to provide a composite material comprised of phosphazene polymer. A feature of phosphazene-containing composites is their superior stiffness, thermal stability, and hardness which is lacking in more typical composite constituents. An advantage of using phosphazene composites is a wider range of applications for phosphazene composites, including uses in harsh environments.
Another object of the present invention provides a method for producing phosphazene-containing composite materials through a pultrusion process.
In brief, these and other objects are achieved by a composite produced by first coating a reinforcing material with an inorganic phosphazene compound and then polymerizing the phosphazene compound so as to confer superior thermal, physical and chemical resistance qualities to the composite.
A phosphazene-containing composite is provided whereby phosphazene imparts superior thermal, physical and chemical resistance to a reinforcing material.
The present invention together with the above and other objects and advantages may best be understood from the following detailed description of the embodiment of the invention illustrated in the drawings, wherein:
FIG. 1 is a diagram of an exemplary process illustrating the present invention; and
FIG. 2 is the chemical formula for a fiber-coating matrix component of the invention comprising hexa-p-hydroxyphenoxycyclotriphosphazene molecules interconnected by phenol formaldehyde linkages.
Referring to FIG. 1, there is shown a method for producing a composite material of the invention through a pultrusion process generally designated by the reference numeral 20. The pultrusion process 20 combines a reinforcing material 21 with a phosphazene polymer, such as the phosphazene polymer having the chemical formula shown in FIG. 2.
The pultrusion process 20 gets its name from the fact that the reinforcing material 21 is literally pulled through the entire process 20. There are generally nine stages involved in the process 20, namely a spooling-off stage 22, a tensioning system 24, a polymer impregnation bath stage 26, a drying process 28, a shaping stage 30, a puller 31, a take-up spool 34, a sizing stage 36, and a polymerization stage 38. The pultrusion process 20 begins when the reinforcing material 21 is supplied in the spooling-off stage 22. The reinforcing material 21 is then directed into the impregnation bath 26 via the tensioning system 24. A prepolymeric substituted phosphazene molecule dissolved in a suitable solvent mixture is contained in the impregnation bath 26. Constituents of the solvent mixture depend on which substitution groups are attached to the phosphazene molecule; different substitution groups require different reactants and solvents.
After the reinforcing material 21 is pulled through the bath 26, then the coated reinforcing material is dried in the drying process 28 to remove the solvents. Next, the coated reinforcing material 21 is subjected to a shaping stage 30 to form it into a desired configuration in preparation for the sizing stage 36 and the final polymerization stage 38. Upon polymerizing with heat and pressure, the final composite 42 is produced.
At the beginning of the pultrusion process 20, the reinforcing material 21 is supplied via the spooling-off stage 22. In the present embodiment, the spooling-off stage 22 is controlled by a small gear, unwinding motor (not shown). The unspooling speed is controlled by the position of a dancer arm 25 in the tensioning system 24 to maintain a smooth and even spool off.
The tensioning system 24 serves to apply the tension to the reinforcing material 21 and to control the speed of the unwinding of the reinforcing material 21. Both of the functions are accomplished simultaneously with the use of a dancer-arm-regulated system. The weight of the dancer arm 25 controls the tension applied to the reinforcing material 21. The dancer arm 25 is also part of an electrical feedback system (not shown) which regulates the speed of spool off. For example, as the dancer arm 25 is raised, the speed of the small gear unwinder motor increases. When the dancer arm 25 is horizontal, the speed of the small gear unwinder motor matches the required speed of the reinforcing material 21 entering the next step of the pultrusion process 20, which is the impregnation bath stage 26.
The major constituent contained in the impregnation bath stage 26 is a prepolymeric phosphazene compound which is produced separately from the pultrusion process 20. This prepolymer coats the reinforcing material 21 during the impregnation bath state 26 and is later polymerized.
Generation of the prepolymeric substituted phosphazene compound is begun by subjecting a base unsubstituted phosphazene polymer, such as hexachlorocyclotri-phosphazene, which has two chlorine atoms attached to each phosphorous, to a substitution reaction with a difunctional monomer. Generally, suitable difunctional monomers can be selected from alkyl groups, aryl groups, aryloxy groups, alkoxy groups, primary amine groups, secondary amine groups, and mercapto groups. An exemplary list of such difunctional monomers follows:
hydroquinone,
4,4'-sulfonyl diphenol,
1,1,1-Tris(4-hydroxyphenyl)ethane,
3,3-(ethylenedioxy)diphenol,
Allyl alcohol,
4,4'-Isopropylidenediphenol,
2,2'-Methylenediphenol,
4,4'-Biphenol,
2,2'-Biphenol,
Resorcinol and
4,4'-Dihydroxydiphenyl ether.
The reaction effects a linkage at each phosphorous to yield the prepolymeric substituted cyclotriphosphazene molecule having the following general formula: ##STR2## where R represents the moiety formed by a nucleophilic substitution reaction. Such phosphazene polymer substitution reactions are disclosed in U.S. Pat. No. 4,749,489, issued on Jun. 7, 1988, which is incorporated herein by reference. The behavior of reactants on the reactive sites of the trimer are well known in the art and are disclosed in H. R. Allcock, "Phosphorous-Nitrogen Compounds-Cyclic, Linear, and High Polymeric Systems," Academic Press, New York 1972, Chapter 16.
In the case of using p-hydroquinone as the difunctional monomer, reaction with hexachlorotriphosphazene will result in two phenoxy substitutions at each phosphorous to yield the prepolymeric substituted cyclotriphosphazene, hexa-p-hydroxyphenoxycyclotriphosphazene. Hexa-p-hydroxyphenoxycyclotriphosphazene has the following chemical formula: ##STR3##
As described in U.S. Pat. No. 4,749,489, three phosphazene molecule configurations are available, namely linear-, cyclolinear- and cyclomatrix-phosphazene polymers. Cyclomatrix or rigid polymers of phosphazene are hard thermosetting resins having limited solubility that can be employed to produce rigid composite structures having thermal stability up to approximately 500° C. Composites incorporating cyclomatrix polymers exhibit superior resistance to acids and bases and to all solvents when cured.
If more flexible composites are desired, the linear or ductile phosphazene polymers can be used. These flexible thermoplastic elastomers produce composites that exhibit a useful temperature range of 80° C. to 250° C. while exhibiting selected solubilities to various solvents. These more ductile composites exhibit good resistance to bases and some acids and most solvents. Good resistance is displayed to ketones, alcohols, and aliphatic hydrocarbons.
A combination of rigid and elastic properties can be achieved by incorporating cyclolinear phosphazene molecules as the flexible thermoplastic elastomers or thermoplastic resins required to provide semi-rigid composite structures having thermal integrity up to 350° C.
Ultimately, the phosphazene-to-difunctional monomer mole ratio is 6-to-1, as it is sought that all six chlorine atoms be removed from each unsubstituted phosphazene molecule.
The laboratory synthesis of the hydroquinone prepolymer was performed as follows:
All of the glassware is dried in an oven at 120° C. and cooled before use under an argon atmosphere. In a nitrogen-purged glove bag, a 3-liter, three-necked, round-bottom flask is charged with 224 grams of hydroquinone and 120 grams of phosphonitrilic chloride trimer. The necks are plugged with rubber septa before the flask is removed from the bag. With argon flowing through the apparatus, the flask is fitted with a reflux condenser topped with a gas inlet, a 300 ml pressure-equalizing addition funnel, and a glass-clad thermocouple.
First, 800 ml of anhydrous cyclohexane is transferred into the flask via the addition funnel, followed by 200 ml of anhydrous pyridine. Cold tap water is run through the reflux condenser; the gas inlet is connected to an argon bubbler to maintain atmospheric pressure within the apparatus. The contents of the flask are warmed to 50° C. to facilitate dissolution of the hydroquinone and phosphonitrilic chloride timer and thereby allowing the mixture to be stirred. The mixture is then heated to reflux, which occurs at 76° C. Upon the reaction mixture reaching reflux, a modern exotherm commences and continues for a few minutes. The mixture is kept refluxing overnight under an argon atmosphere and then allowed to cool. At this point, the contents of the flask are not sensitive to moisture and so can be handled in air: the hydroquinone prepolymer is hydrolytically stable, as contrasted to the phosphonitrilic chloride trimer.
Isolation and purification of the hydroquinone prepolymer are effected by dissolving the amber solid in 500 ml of hot 80 percent acetic acid. After the light amber solution is allowed to cool to room temperature, it is added to 20 liters of deionized water, resulting in the precipitation of the hydroquinone prepolymer as a white solid. The mixture is stirred for 30-45 minutes to allow for digestion of the precipitate. The white solid is collected by filtration and then redissolved and reprecipitated in the same fashion. The white solid collected by filtration is then washed with pH-neutral water until the rinsate is neutral. The washing can be performed either on the filter, yielding a white powder, or using a Soxhlet extractor, yielding an off-white, compressed mass. The solid is then dried by gentle warming; a period of three to four days can be necessary to drive off all of the entrapped water, and no color change is observed during this time. The resultant dry mass typically weighs 130 grams for a yield of about 70 percent, based on the amount of phosphonitrilic chloride starting material.
The identity of the product is confirmed by comparison of 1 H, 13 C, and 31 P NMR spectra with those of a known sample.
It is the polymer impregnation bath stage 26 where the prepolymer, formulated in the above process, is applied to the reinforcing material 21. The purpose of the impregnation bath stage 26 is to coat the reinforcing material 21 with the prepolymeric substituted phosphazene compound in preparation for the subsequent polymerization stage 38, whereby the prepolymeric substituted phosphazene molecules are polymerized or linked together.
The preparation of the impregnation liquor in the impregnation bath stage 26 is dependant upon the type of difunctional monomer chosen in the substitution reaction with the base, unsubstituted, phosphazene polymer hexachlorocyclotriphosphazene. If a diol, such as hydroquinone, is substituted at the phosphorous sites, then linking of adjacent phosphazene molecules will have to be facilitated by exposing the ring to a nucleophilic carbon, such as that found on formaldehyde. The formaldehyde, then, or some other carbonyl carbon source, would have to be supplied sometime before or during the polymerization process. A number of suitable compounds, such as a hexamethylenetetramine, formalin and paraformaldehyde, can serve as the needed cross linking agent. Alternatively, such reactions are not necessary if difunctional monomers are selected which have allylic carbons or other electrophilic centers. Such monomers include allyl alcohol, hexamethylenediamine and the glycols.
Accordingly, if p-hydroquinone is used as the difunctional monomer, the resulting prepolymer hexa-p-hydroxyphenoxycyclotriphosphazene, formulated in the above process, is then dissolved in a suitable solvent, in approximately a 2 to 1 mole ratio with hexamethylenetetramine. The hexamethylenetetramine is presented in a water-acetone mixture. The pressure of this reaction is maintained at 1 atmosphere. The resulting solution comprises the impregnation bath used to treat the reinforcement component of the composite. Aside from a solution, the prepolymer can also be applied as a fine powder or a liquid melt. Regardless of the process used, a desired weight percent fiber to resin mixture is 60%, plus or minus 5%.
A myriad of types of reinforcing material, including glass, oxynitride glass fibers, or carbon, such as graphite, which are typically supplied in fiberous ribbon-like or tape-like configurations, can be pulled through the impregnation bath. Any fiber thickness can be used. AS-4-12K Magnamite, by Hercules, is one example of a suitable graphite fiber type. Good results have been achieved at tape thicknesses ranging from 0.15 millimeters (mm) to 0.20 mm. The weight percent of reinforcing material 21 to total composite weight will vary, from 50 percent to 80 percent depending on the use of the final composite structure 42. The amount of impregnation of the reinforcing material 21 by the polymer depends on how long the reinforcing material 21 is immersed in the impregnation bath 26. Exposure times can vary, from approximately 0.25 minutes to 3 minutes. Good composites are produced when graphite fibers comprise 60 weight percent, plus or minus 5 percent of the final composite. This weight ratio is achieved when the graphite is immersed in the impregnation bath 26 of the proper concentration for approximately 30 seconds at 1 atm at room temperature.
In both a slurry and solution type of impregnation of the reinforcing material 21, the solvent, for example, acetone, must be removed by heating the newly formulated composite mixture at approximately 40° C.-60° C., at the drying process stage 28. The drying process stage 28 can be any workable system, including, for example, such as an oven, a heated stream of air or a stream of hot inert gas. A stream of hot nitrogen ranging in temperature from 42° C. to 52° C. has been employed.
Usually, it is desirable to shape the reinforcing material 21 into a shaped reinforcing material 39 that is easily handled. Any suitable system for the shaping stage 30 can be employed, for example, such as, a system of flat bars, dies or rollers to flatten the fiber-matrix composite.
The shaped reinforcing material 39 is pulled through the pultrusion process 20 by the puller 31 and take-up means 34. For example, the puller 31 can include a high torque, 100 in/oz, low speed 1.9 RPM motor for pulling the reinforcing material 21 through the process 20. The puller 31 can be an "S" type of puller arrangement as shown in FIG. 1 in which a spool 33 is free wheeling and the take-up spool 34 is attached to a separate puller motor (not shown) to wind up the shaped reinforcing material 39. Alternatively, the puller 31 can consist of the spools 32 and 34 with spool 32 adapted to wind the shaped reinforcing material 39 directly on the spool 34.
The shaped reinforcing material 39 is then removed from the take-up spool 34 and cut or otherwise configured into a sized reinforcing material 40 at the sizing stage 36 in preparation for the polymerization stage 38.
The polymerization stage 38 subjects the shaped reinforcing material 39 to heat and pressure. Heat and pressure are necessary to drive the polymerization reaction. Typically, a temperature of approximately 150° C. to 220° C. is employed. Using graphite fibers and cyclomatrix phosphazene polymers, applying heat for 5 minutes at contact pressure and for an additional 25 minutes at 5,000 psi produces a good rigid composite matrix as the resulting composite 42. If more flexible composites are desired, a blend of cyclomatrix and linear phosphazene polymers can be used. Generally, pressures can range from 100 psi to 5,000 psi.
The polymerization stage 38 is the final step in producing the composite product 42.
Many polyphosphazene samples formulated by the prepolymer fabrication process outlined above have been tested for their mechanical and flexural properties. Accordingly, Table 1, below, shows the densities and percent open porosity of samples of polyphosphazene bars, and Table 2, below, shows the breaking strength and elasticity properties of phosphazene materials. The numbers in the column labelled Sample represent the identification number of the specific samples tested. The GPa designation represents gigaPascals and psi represents pounds per square inch.
Various moduli properties are also listed in Table 2. Shear modulus indicates the ratio of the shearing stress divided by the corresponding shear. Young's modulus is defined as the force in dynes per square centimeter (dynes/cm2) to permanently deform a material by stretching, twisting or bending it. The deformation defined in the Young's Moduli standard is represented generally by the formula FL/al where F is the whole force, a the area, L the entire length of the wire or substrate, and l the extension. Bulk modulus is the approximate value in dynes/cm2 between the limit of elasticity and the breaking strength of a material.
TABLE 1 ______________________________________ DENSITIES AND PERCENT OPEN POROSITY OF POLYPHOSPHAZENE BARS Density Open Porosity Sample (g/cm.sup.3) (%) ______________________________________ 139-1 1.441 0.0653 132-1 1.440 0.0784 131-2 1.439 0.0845 137-2 1.440 0.0633 ______________________________________
TABLE 2 ______________________________________ MECHANICAL PROPERTIES OF POLYPHOSPHAZENE BARS Shear Young's Modulus Modulus Poisson's Bulk Modulus Sample GPa (psi) GPa (psi) Ratio GPa (psi) ______________________________________ 139-1 2.74 (400040) 7.44 (1086240) 0.356 8.63 (1,259,980) 132-1 2.74 (400040) 7.44 (1086240) 0.356 8.62 (1,258,520) 131-2 2.74 (400040) 7.44 (1086240) 0.357 8.70 (1,270,200) 137-2 2.72 (397120) 7.39 (1078940) 0.356 8.57 (1,251,220) 131-1 2.76 (402960) 7.50 (1095000) 0.358 8.81 (1,286,260) ______________________________________
Phosphazene polymer, formulated by the above prepolymer fabrication process, also displays superior surface characteristics compared to composites formulated with organic resins. Table 3 below depicts polyphosphazene material as having superior Rockwell Hardness characteristics compared to composite material fabricated with organic resins. The various composites, designated as "PET-glass", "PPO-glass", "PC-glass", and "ABS-glass" represent polyethyleneterephalate-glass, polyphenyleneoxide-glass, polycarbonate-glass and acrylonitrilebutadienestyrene-glass composites, respectively. The Rockwell Hardness of a substance is a measure of its relative hardness, based on the indentation made by a 1/16", 1/8" or 1/4" standard steel ball or a conical diamond with an apex angle of 120 degrees. Results are reported by using numbers to denote the pressure applied in kilograms, and letters are used to denote the ball or diamond producing the indentation. Accordingly, phosphazene bars withstand in excess of 120 kilograms of pressure applied by the M indentation standard, which is a 1/4 inch diameter steel ball.
Phosphazene bars also exhibit superior stiffness properties, as shown in Table 4, below. A comparison of the Young's Moduli properties of phosphazene bars with typical composites shows the relatively superior stiffness qualities of the invention.
TABLE 3 ______________________________________ ROCKWELL HARDNESS OF POLYPHOSPHAZENE AND VARIOUS COMPOSITES Indentation Pressure Sample (Kgs. M Scale) ______________________________________ Polyphosphazene 120-130 PET-glass 80-100 Polyamides-glass 90-100 PPO-glass 90-97 PC-glass 80-90 ABS-glass 70-80 ______________________________________
TABLE 4 ______________________________________ COMPARISON OF YOUNGS'S MODULI OF POLYPHOSPHAZENE WITH VARIOUS ENGINEERING PLASTICS Sample GPa 10.sup.6 psi ______________________________________ Polyphosphazene 7.4 1.07 Phenolic 5.5 0.78 Polystyrene 3.4 0.48 Polymethylmethacrylate 2.8 0.41 Polycarbonate 2.4 0.35 Polypropylene 1.4 0.20 High Density Polyethylene 0.8 0.10 ______________________________________
The resulting composite 42 exhibits unexpectedly superior qualities of hardness and elasticity. Table 5 depicts the flexural strength of phosphazene materials in monolithic form, for example, without reinforcement material, as well as phosphazene composite materials using carbon fiber and woven glass mat. The width and thickness of the samples are shown, as is the breaking point , designated as Break Pt, where the bar broke at the indicated pressure (given in pounds). The flexural strength of the materials is given in MPa and psi. Table 6 compares the flexural strength of a phosphazene-containing composite with more typical composite materials.
TABLE 5 ______________________________________ FLEXURAL STRENGTH OF MONOLITHIC PHOSPHAZENE AND PHOSPHAZENE- CONTAINING COMPOSITES Width Thickness Break Pt Strength Sample (mm) (mm) (lbs) MPa PSI ______________________________________ Polyphosphazene Monolithic Bars. -115-2 12.71 2.74 40.50 56.64 8214.57 -115-3 12.69 2.74 66.50 93.15 13509.38 -116-2 12.60 2.80 43.80 59.17 8581.51 -116-3 12.67 2.82 61.80 81.85 11871.08 -122-1 12.75 2.81 19.00 25.19 3652.64 -123-1 12.73 2.81 56.80 75.41 10936.63 -127-3 12.68 2.82 63.00 83.38 12092.04 -127-1 12.73 2.82 87.60 115.48 16747.65 1743-28I 12.66 2.80 16.60 22.32 3236.94 -291 12.64 2.80 61.00 82.15 11913.60 -29-2 12.65 2.83 52.00 68.49 9933.82 Polyphosphazene Carbon Fiber Composites. -114-2 12.70 2.80 692.00 927.48 134512.53 -114-3 12.53 2.81 665.00 896.97 130087.14 -117-2 12.68 2.82 723.00 956.84 138770.53 -117-3 12.68 2.78 624.00 849.76 123240.14 -118-1 12.74 2.79 598.00 804.71 116707.77 -123-2 12.72 2.74 673.00 940.47 136396.51 -123-3 12.82 2.78 329.00 443.14 64267.99 -124-1 12.75 2.79 361.00 485.41 70398.76 -124-3 12.78 2.78 385.50 520.86 75540.59 -124-4 12.81 2.74 476.00 660.50 95792.86 -125-1 12.76 2.81 717.00 949.67 137731.18 -131-2 12.77 2.80 289.00 385.22 55868.54 -129-2 12.75 2.56 619.00 988.60 143376.16 -129-3 12.77 2.55 465.00 747.31 108382.24 -131-3 12.76 2.74 357.50 498.02 72227.18 -132-1 12.73 2.68 488.00 712.26 103299.51 -134-2 12.77 2.62 410.50 624.94 90635.03 -135-1 12.63 2.62 384.00 591.08 85723.86 Polyphosphazene Glass Mat Composites. -89-2 12.74 2.81 210.00 278.58 40403.00 -90-1 12.75 2.79 280.00 376.49 54602.92 -100-3 12.77 2.78 166.50 225.14 32652.03 102-1 12.78 2.80 96.00 127.86 18543.89 102-2 12.76 2.82 112.00 147.29 21362.18 -102-3 12.75 2.79 261.00 350.95 50897.72 -132-2 12.77 2.80 147.00 195.94 28417.56 ______________________________________
TABLE 6 ______________________________________ FLEXURAL STRENGTH OF A PHOSPHAZENE COMPOSITE AND VARIOUS OTHER COMPOSITES Sample 10.sup.3 psi ______________________________________ Phosphazene-Carbon fiber 194.97 Polyphenylene sulfide-Carbon fiber 198.00 Epoxy-Scotchply 184.00 Amine epoxy-Graphite fiber 260.00 ______________________________________
While the invention has been described with reference to details of the illustrated embodiment, these details are not intended to limit the scope of the invention as defined in the appended claims.
Claims (7)
1. A composite material comprising:
a single constituent fibrous reinforcing material; and
a phosphazene compound; said phosphazene compound coating said single constituent fibrous reinforcing material to form the composite material whereby to impart predetermined thermal, physical and chemical resistance to the composite material.
2. A composite material as recited in claim 1 wherein the single constituent fibrous reinforcing material is selected from the group consisting of glass, carbon, and oxynitride fibers.
3. A composite material as recited in claim 1 wherein the phosphazene compound is selected from the group consisting of linear polyphosphazene, cyclolinear polyphosphazene, cyclomatrix polyphosphazene, and combinations thereof.
4. A composite material as recited in claim 1 wherein the phosphazene compound has the chemical formula: ##STR4## where R is a difunctional side group selected from the group consisting of alkyl groups, aryl groups, aryloxy groups, alkoxy groups, primary amine groups, secondary amine groups, mercapto groups, and combinations thereof; and n is an integer greater than 1.
5. A composite material as recited in claim 1 wherein the composite material contains between 50 and 80 percent by weight of single constituent reinforcing fibrous material to the total weight of the composite material.
6. A composite material as recited in claim 1 wherein the composite material contains between 55 percent and 65 percent by weight of single constituent fibrous reinforcing material to total weight of the composite material.
7. A composite material comprising:
a graphite fiber; and
hexa-p-hydroxyphenoxycyclotriphosphazene; said hexa-p-hydroxyphenoxycyclotriphosphazene coating said graphite fiber to form the composite material whereby to impart predetermined thermal, physical and chemical resistance to the resulting composite material, and said graphite fiber comprises 55 weight percent to 70 weight percent of the composite material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/559,234 USH1309H (en) | 1990-07-30 | 1990-07-30 | Phosphazene polymer containing composites and method for making phosphazene polymer containing composites |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/559,234 USH1309H (en) | 1990-07-30 | 1990-07-30 | Phosphazene polymer containing composites and method for making phosphazene polymer containing composites |
Publications (1)
Publication Number | Publication Date |
---|---|
USH1309H true USH1309H (en) | 1994-05-03 |
Family
ID=24232831
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/559,234 Abandoned USH1309H (en) | 1990-07-30 | 1990-07-30 | Phosphazene polymer containing composites and method for making phosphazene polymer containing composites |
Country Status (1)
Country | Link |
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US (1) | USH1309H (en) |
Cited By (9)
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GB2280951A (en) * | 1993-07-05 | 1995-02-15 | Aaf Ltd | Housing with pultruded frame |
WO1996026385A1 (en) * | 1995-02-24 | 1996-08-29 | Owens Corning | Infrared radiation blocking insulation product |
US5569736A (en) * | 1994-11-22 | 1996-10-29 | Battelle Memorial Institute | Inorganic-organic composite polymers and methods of making |
US5855962A (en) * | 1997-01-09 | 1999-01-05 | International Business Machines Corporation | Flowable spin-on insulator |
US20050142296A1 (en) * | 2003-12-30 | 2005-06-30 | 3M Innovative Properties Company | Substrates and compounds bonded thereto |
US20070060739A1 (en) * | 2003-06-05 | 2007-03-15 | Kotaro Kuwata | Process for producing phosphonitrilic acid ester |
US20070065490A1 (en) * | 2003-12-30 | 2007-03-22 | Schaberg Mark S | Substrates and compounds bonded thereto |
US9193834B2 (en) | 2010-10-04 | 2015-11-24 | King Saud University | Phosphazene-formaldehyde polymers and their polymer metal-complexes |
CN116695271A (en) * | 2023-07-05 | 2023-09-05 | 潮州市丹辉婚纱礼服有限公司 | High-elasticity spandex fiber fabric and preparation process thereof |
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US4446191A (en) | 1980-10-27 | 1984-05-01 | Hitachi Chemical Company, Ltd. | Laminates comprising prepregs metal clad |
US4749489A (en) | 1986-05-30 | 1988-06-07 | The United States Of America As Represented By The United States Department Of Energy | Polyphosphazene semipermeable membranes |
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Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2280951A (en) * | 1993-07-05 | 1995-02-15 | Aaf Ltd | Housing with pultruded frame |
GB2280951B (en) * | 1993-07-05 | 1997-12-10 | Aaf Ltd | Improvements in and relating to air handling units |
US5569736A (en) * | 1994-11-22 | 1996-10-29 | Battelle Memorial Institute | Inorganic-organic composite polymers and methods of making |
WO1996026385A1 (en) * | 1995-02-24 | 1996-08-29 | Owens Corning | Infrared radiation blocking insulation product |
US5633077A (en) * | 1995-02-24 | 1997-05-27 | Owens-Corning Fiberglas Technology, Inc. | Infrared radiation blocking insulation product |
US5855962A (en) * | 1997-01-09 | 1999-01-05 | International Business Machines Corporation | Flowable spin-on insulator |
US7514520B2 (en) * | 2003-06-05 | 2009-04-07 | Asahi Kasei Chemicals Corporation | Process for producing phosphonitrilic acid ester |
US20070060739A1 (en) * | 2003-06-05 | 2007-03-15 | Kotaro Kuwata | Process for producing phosphonitrilic acid ester |
US20070065490A1 (en) * | 2003-12-30 | 2007-03-22 | Schaberg Mark S | Substrates and compounds bonded thereto |
US20050142296A1 (en) * | 2003-12-30 | 2005-06-30 | 3M Innovative Properties Company | Substrates and compounds bonded thereto |
US7658994B2 (en) | 2003-12-30 | 2010-02-09 | 3M Innovative Properties Company | Substrates and compounds bonded thereto |
US9193834B2 (en) | 2010-10-04 | 2015-11-24 | King Saud University | Phosphazene-formaldehyde polymers and their polymer metal-complexes |
CN116695271A (en) * | 2023-07-05 | 2023-09-05 | 潮州市丹辉婚纱礼服有限公司 | High-elasticity spandex fiber fabric and preparation process thereof |
CN116695271B (en) * | 2023-07-05 | 2024-05-14 | 普宁市杰仕达制衣有限公司 | High-elasticity spandex fiber fabric and preparation process thereof |
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