CN1035771C - Polyamide resin composition and molded articles obtained therefrom - Google Patents
Polyamide resin composition and molded articles obtained therefrom Download PDFInfo
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- CN1035771C CN1035771C CN 93112789 CN93112789A CN1035771C CN 1035771 C CN1035771 C CN 1035771C CN 93112789 CN93112789 CN 93112789 CN 93112789 A CN93112789 A CN 93112789A CN 1035771 C CN1035771 C CN 1035771C
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Abstract
The present invention provides a polyamide resin compound which contains a polyamide ingredient (A) and at least one 5 to 70 wt% of inorganic filler (B), wherein the polyamide ingredient (A) as a semi-aramid polyamide accounts for 30 to 95 wt % of polyamide resin and is formed by 70 to 95 wt% of hexahedral methylene adipamide unit (a) obtained fromadipic acid and hexamethylenediamine and 5 to 30 wt % of hexahedral methylene iso-phthalic amide unit (b) obtained from iso-phthalic acid and hexamethylenediamine, and the viscidity etar r of a sulfuric acid solution is from 1.5 to 2.8; the inorganic filler is selected from glass fibers, carbon fibers, mica, talcum, kaolin, grammite, calcium carbonate and potassium titanate. The present invention also provides a moulding article which contains the resin compound and high surface gloss.
Description
The moulded parts that the present invention relates to a kind of Amilan polyamide resin composition and make by it, have fabulous surface luster.More particularly, the moulded parts that the present invention relates to a kind of Amilan polyamide resin composition and make by it, this moulded parts has the inside and outside decoration of automobile, office appliance, sports goods and the required fabulous surface luster of entertainment article, required high strength, high rigidity and high-dimensional stability in the practical application, also has some other fabulous characteristic in addition, as heat-resistant aging, photostabilization, anti-fadedness and light transmission.
At present, people utilize the fabulous mechanical property of polyamide resin, the advantage by the high reinforced effects that obtains with inorganic fillings (as glass fibre) enhanced method and aspect such as fabulous colourability and workability, more and more widely will be as its external and internal compositions member.
High surface luster, intensity, rigidity and dimensional stability are the performances that structural member needs jointly.Wherein, surface luster is not only comprised the die design of gate location, size and dimension and the remarkably influenced of condition of moulding, and is subjected to the flowability of resin in mould and the remarkably influenced of condition of cure.Especially, the composition that contains inorganic filler (as glass fibre) is often owing to the surface that inorganic filler partly is projected into moulded parts is damaged surface luster.These have the appearance poor than the moulded parts of low gloss, and its commercial value is descended, and the slidably property of itself and other materials is degenerated.
In order to satisfy the requirement of high strength, rigidity and dimensional stability, inorganic filler is added to as glass fibre normally everybody is familiar with in the resin.But, known when the quantity that increases inorganic filler when improving intensity, rigidity and dimensional stability, the surface luster of moulded parts can variation.Therefore, in order to obtain the moulded parts of fabulous gloss and high strength, rigidity and dimensional stability, way so far all is that the quantity with inorganic filler is reduced to such degree, so that weighting agent can not give prominence on the surface, and the design of the decline of the intensity, rigidity and the dimensional stability that are caused by the minimizing of weighting agent quantity by article shape compensates as the increase wall thickness or with methods such as rib reinforcements.
On the other hand, also developed and do not damaged the resin material that its surface luster increases inorganic filler quantity simultaneously again as far as possible.For example, open 63-118367,2-265965 of Japanese Patent Kokoku 61-60861 and Japanese Patent, 3-269056,4-77554 and 4-149234 have applied for these resin materials.
Wherein, in the open 2-265965 of Japanese Patent disclosed, because suction, only contain the remarkably influenced of the temperature and humidity of the intensity of polyamide resin of aliphatic polyamide (as nylon 6, nylon 66 and nylon 66/6 multipolymer) combination and the environment that rigidity is subjected to their actual uses, so these polyamide resins are restricted in its application.
In addition, in order this patent Kokoku 61-60861 and Japanese Patent open 63-118367,3-269056 and 4-149234 disclosed like that because suction makes the decline of intensity and inflexible decline and dimensional stability contain the monomer component of aromatic ring such as the polyamide resin of terephthalic acid and m-phthalic acid improves to a certain extent by use.But, according to these technology, be difficult to obtain the moulded parts of satisfied high-surface gloss, because the flowability difference of this resin combination that contains inorganic filler or the curing speed height in mould.In order to obtain the moulded parts of high-surface gloss with these resins, method is the temperature of mould of raising as far as possible.But produce a new problem so again, extended molding cycle.And when using bigger mould, the entire die that raises equably temperature inside has become difficulty.In addition, under the situation of the mould of the somewhat complex design that rib structure is arranged, form localized hyperthermia district and local cold zone, therefore the moulded parts that generates has been seen high-surface gloss part and low surface gloss part on the whole.Therefore, in order to obtain all having the moulded parts of high-surface gloss, need and in very wide die temperature scope, to produce the resin combination of high gloss, but do not have a kind of material of routine can satisfy this requirement on whole surface.
That is to say, not having a kind of resin combination to satisfy simultaneously all has high surface luster and pair needed high strength of structured material parts, rigidity and dimensional stability is arranged in actual applications in very wide condition of moulding, therefore an object of the present invention is to provide a kind of resin combination that can satisfy all these requirements, and the moulded parts that fabulous surface luster is arranged that makes by it.
In order to achieve the above object, the present inventor has carried out research widely, thereby find, contain very specific component and have the resin combination of very specific ratio of components in very wide die temperature scope, can produce very high-surface gloss, this resin combination suction back intensity and rigidity have decline slightly, and when molding fabulous dimensional stability are arranged.Therefore, the present invention is achieved.
That is to say, a first aspect of the present invention is a kind of Amilan polyamide resin composition that is applicable to molding, it contains (A) a kind of polyamide component and (B) at least a inorganic filler polyamide component of 5-70% (weight) 30-95% (weight) that is polyamide resin, it is a kind of partially aromatic polyamide, by the hexa-methylene adipamide units that obtains by hexanodioic acid and hexamethylene-diamine of (a) 70-95% (weight) and (b) the hexa-methylene isophthaloyl amine unit that obtains by m-phthalic acid and hexamethylene-diamine of 5-30% (weight) form, its sulphuric acid soln viscosities il r is 1.5-2.8, and inorganic filler is selected from glass fibre, carbon fiber, mica, talcum, kaolin, wollastonite, lime carbonate and potassium titanate.
A second aspect of the present invention is above-mentioned Amilan polyamide resin composition, and wherein, the not end carboxyl of described polymeric amide is than being at least 65%, and contains the mixture of copper compound and iodine compound and/or manganic compound, and its ratio satisfies following formula (1)-(3):
(1) 0.5ppm≤copper≤150ppm
(2) 20≤iodine/copper≤30 (grammeatom ratio)
(3) 0.5ppm≤manganese≤60ppm.
A third aspect of the present invention is above-mentioned Amilan polyamide resin composition, also contains 5-80 part reunion phenylate resin, by 100 parts of above-mentioned polyamide resins of weight.
A fourth aspect of the present invention is the moulded parts that is made by above-mentioned Amilan polyamide resin composition, fabulous surface luster is arranged.
Fig. 1 represents to be used to measure the test exemplar of weld seam intensity partly, and this exemplar is used for following examples and Comparative Examples.Reference number among Fig. 1 is represented as follows:
1. weld seam part
2. notes road
3. runner
4. test exemplar
The polyamide that the present invention uses contain the hexa-methylene adipamide units (hereinafter referred to as " N66 ") that obtained by adipic acid and hexamethylene diamine and the hexa-methylene that obtained by M-phthalic acid and hexamethylene diamine between benzenedicarboxamide unit (hereinafter referred to as " N6I "). The constituent ratio of each component is 70-95% (weight) N66 and 5-30% (weight) N6I, preferably 72-93% (weight) N66 and 7-28% (weight) N6I. If the quantity of N6I is less than 5% (weight), owing to absorb water, intensity and rigidity all descend in actual applications, and mechanograph shrinks large to the problems such as warpage and distortion of generation. Particularly, moulding article is larger, because the slightly variant caused warpage of mechanograph contraction is also larger. If the quantity of N6I is greater than 30% (weight), inorganic filler often is projected into the surface of moulding article, thereby can not obtain satisfied lustrous surface, for example, and when using water that its temperature is controlled to mould below 100 ℃ and carries out molding. And unless adopt sufficiently long cool time for the resin in the mould, moulding article just can not the demoulding from mould, so generation rate is lower.
Therefore, really it is shocking, by very N6I component and the N66 combined polymerization of limited quantity, might obtain having the Amilan polyamide resin composition of following two specific characters, namely (1) mechanograph shrinks and can reduce the moulding article that also can obtain having high-surface gloss with (2) with the mould of water management temperature. This fact was expected by routine techniques never that it was found first by the present invention.
The molecular weight of the polyamide that the present invention is used is 1.5-2.8, preferred 1.6-2.7, and more preferably 1.7-2.6 presses the viscosities il r (per 1 gram polymer is in 100 milliliter of 95.5% sulfuric acid, 25 ℃ of lower mensuration) in sulfuric acid solution. Also can be by in the mould that resin combination was packed within the so short time, thus near the resin die surface can fully cover inorganic filler and the method for not solidifying improves the lustrous surface of molded resin. So, preferably use the polymer that high fluidity is arranged, namely use the alap polyamide of molecular weight. Because the result of the broad research that the molecular weight ranges that can not cause various character and lustrous surface variation is carried out has found that, when using η r as the polyamide of 1.5-2.8, can obtain high intensity, rigidity and lustrous surface. Therefore, molecular weight is fixed in the above-mentioned scope. If η r is less than 1.5, resin combination becomes fragile, and tear drop appears in the nozzle top at barrel when molding, so molding becomes impossible. If η r is greater than 2.8, it is too high that the melt viscosity of resin becomes, and inorganic filler partly is projected into the surface (relevant with the design of used mould) of moulding article when molding, so lustrous surface descends.
The used polyamide of the present invention is obtained by the salt polycondensation reaction of adipic acid and M-phthalic acid and hexamethylene diamine. Reaction method comprises known melt polymerization, solid phase, polymerisation in bulk, polymerisation in solution or its combination. In addition, polyamide also can be obtained by polymerisation in solution or the interfacial polymerization of Adipoyl Chloride and a phenyl-diformyl ammonia and hexamethylene diamine. From the viewpoint of economy, wherein the combination of melt polymerization or melt polymerization and solid phase is preferred.
The used inorganic filler of the present invention is at least a inorganic filler that is selected from glass fibre, carbon fiber, mica, talcum, kaolin, wollastonite, calcium carbonate and potassium titanate. Glass fibre preferably wherein, the combination of glass fibre and mica, the combination of glass fibre and kaolin or roasting kaolin, the combination of glass fibre, talcum and kaolin or roasting kaolin, kaolin or roasting kaolin, talcum, the combination of talcum and kaolin or roasting kaolin, mica, wollastonite, the combination of carbon fiber and glass fibre and carbon fiber. Can use those glass fibres that are generally used for thermoplastic resin, on thickness and length to them without special restriction. Any single thread that prescinds, rove and debris all can use. The poly-agent of available known silane idol is coated in the inorganic filler surface. The quantity of the inorganic filler that adds is 5-70% (weight), preferred 10-65% (weight). If its quantity is less than 5% (weight), the humidification of inorganic filler can not show fully, therefore can not obtain satisfied intensity and rigidity. If its quantity is greater than 70% (weight), the mobile variation of resin, so it becomes and is difficult to make resin to fill up thin-walled portion, and all be difficult to obtain the moulding article of excellent surface gloss with any mould.
Because according to different purposes, composition sometimes is used under the high-temperature atmosphere or exposes in the sun, so require composition of the present invention that fabulous heat-resistant aging and light resistance are arranged. Consider this some, the present inventor has carried out further research, found that, the method of being combined with copper, iodine and the manganese compound of specific quantity by the polyamide that the specified end group ratio is arranged, can obtain comparing with the polyamide of routine, not only improved heat-resistant aging and light resistance, and the temporal evolution less resin combination that fades. That is to say that the conventional polyamide that contains copper, iodine and manganese compound is in the improvement that has aspect attached heat aging and the light resistance to a certain degree, but some problems are also arranged: polyamide owing to absorb water fades or owing to heat or light damage. Particularly, in the use of the structural material of the resin painted with shades of colour, fading in the surface is a fatal shortcoming, therefore the minimum material that fades need to be arranged.
Have fabulous heat-resistant aging and light resistance and the temporal evolution less resin combination that fades will be described hereinafter, it is second aspect of the present invention.
The terminal carboxyl group ratio of polyamide of the present invention must be at least 65%, preferably is at least 70%, and this ratio is end carboxy concentration and end carboxy concentration (COOH) and terminal amino group concentration (NH2) ratio of sum: { (COOH)/((COOH)+(NH2)) * 100 (%). If this ratio is less than 65%, molded resin fades into pistac. In order to control the end carboxy concentration of polyamide, the following method is arranged. Namely before the beginning polymerization, again monocarboxylic acid or dicarboxylic acids are added to etc. in the saline solution of mole adipic acid and M-phthalic acid and hexamethylene diamine, or begin the polymerization of the molar salt aqueous solution such as being, in polymerization process, from reaction system, remove the hexamethylene diamine component. In addition, end carboxy concentration also can directly react in extruding machine or kneader by the compound of polyamide and monocarboxylic acid or dicarboxylic acids and control. When controlling end carboxy concentration with monocarboxylic acid or dicarboxylic acids, can mention and use CH3(CH
2)
nCOOH (n=0-30) and HOOC (CH2)
nThe aliphatic carboxylic acid of COOH (n=0-30) expression, aromatic carboxylic acid such as benzoic acid, toluic acid, M-phthalic acid and terephthalic acid (TPA), naphthalene-ring containing carboxylic acid such as naphthalene dicarboxylic acids and the carboxylic acid that contains cyclohexane ring.
As the example of copper compound, can mention cupric chloride, cupric bromide, cupric iodide, cupric phosphate, cuprammonium complex, copper stearate, montanic acid copper, hexanodioic acid copper, m-phthalic acid copper, terephthalic acid copper, cupric benzoate, cupric pyrophosphate, venus crystals and cuprammonium.Preferably cupric bromide, cupric iodide and venus crystals.The quantity of the copper compound that adds is that by polyamide, the quantity of copper is 0.5-150ppm, preferred 0.7-140ppm.If this quantity less than 0.5ppm, just can not obtain enough heat-resistant agings and photostabilization.If this quantity is greater than 150ppm, resin since suction cause after fade clearly.
Iodine compound for example comprises potassiumiodide, magnesium iodide and ammonium iodide and also can use simple iodine.Potassiumiodide is preferred.The quantity of the iodine compound that adds is that iodine element is 20-30 with the grammeatom of copper than ((I)/(Cu)), preferred 22-28.If this ratio less than 20, can not obtain enough heat-resistant agings and photostabilization, resin is owing to fading clearly that suction causes in addition.If this ratio greater than 30, can be easy to occur the corrosion of metal such as polymerization reactor, extruding machine and mould machine and the corrosion of metal that inserts moulded parts.
Manganic compound for example comprises manganous lactate and manganese pyrophosphate.The adding quantity of manganic compound is that by polymeric amide, the quantity of manganese element is 0.5-60ppm, preferred 0.7-55ppm.If this quantity less than 0.5ppm, can not obtain enough photostabilization.If this quantity greater than 60ppm, though there is not special problem, does not need to add the manganic compound than desired number greater amt, because can obtain enough photostabilization by the combination of copper compound and iodine compound.
The method that copper compound, iodine compound and manganic compound are added in the polymeric amide is unrestricted, their available known methods add, for example each compound is dissolved in the salt brine solution of di-carboxylic acid and diamines and carries out the polyamide polymerization, perhaps in the polymerizing polyamide process, add each compound, perhaps in single multiple screw extruder or Bitruder or kneader, each compound is mediated in the fused polyamide resin.
The resin combination that the present invention contains polymeric amide and inorganic filler is aspect the surface luster of the moulded parts that is made by it and all the polyamide resin material than routine is much superior intensity in actual applications, rigidity and dimensional stability aspect.But the present inventor has done further research, attempts to improve intensity, rigidity and dimensional stability in the practical application, found that, can obtain further obviously improving under the situation of the surface luster of not damaging moulded parts the resin combination of these character.
A third aspect of the present invention will explain hereinafter.
The polyphenylene oxide resin that the present invention uses is the polymkeric substance that contains the structural unit that following formula represents
(R wherein
1, R
2, R
3And R
4Represent hydrogen, halogen atom, alkyl or aryl separately, n represents the polymerization degree).The example of polymkeric substance is poly-(2,6-dimethyl-1,4-phenylene ether), poly-(2,6-diethyl-1, the 4-phenylene ether), poly-(2,6-dipropyl-1, the 4-phenylene ether), poly-(2-methyl-6-ethyl-1, the 4-phenylene ether), poly-(2-ethyl-6-propyl group-1,4-phenylene ether), poly-(2,6-diallyl-1, the 4-phenylene ether), poly-(2-methyl-6-allyl group-1, the 4-phenylene ether), poly-(2,6-two chloro-1,4-phenylene ether), poly-(2,6-two bromo-1, the 4-phenylene ether), poly-(2-chloro-6-bromo-1,4-phenylene ether), poly-(2,6-two fluoro-1, the 4-phenylene ether), poly-(2,3,6-trimethylammonium-1,4-phenylene ether) and poly-(2,3,5,6-tetrabromo-1,4-phenylene ether) and their multipolymer.
It is heavy that the quantity of the polyphenylene oxide resin that adds is counted 5-80 part by the weight of 100 parts of polyamide resins, and preferred 10-75 part is heavy.If this quantity is less than 5 parts of weights, the effect of improving intensity, rigidity and dimensional stability in actual applications is less.If this quantity is greater than 80 parts of weights, flowability descends, so the surface luster of moulded parts also descends.In addition, to the chemical-resistant decline of oil product and other chemical, therefore application is restricted.
Add when polyphenylene oxide resin mixes with polymeric amide if will be grafted to the styrene polymer of the modification for preparing on the polystyrene or be grafted to the modified polyphenylene ether resin for preparing on the polyphenylene oxide, can improve the intensity of the weld seam part that often goes wrong for moulded parts with toxilic acid with toxilic acid.
The styrene polymer of modification be free radical form that agent exists or non-existent situation under by α, β-undersaturated carboxylic acid or derivatives thereof is grafted to mainly the polymkeric substance that obtains on the polymkeric substance of being made up of aromatic vinyl compound.Here used aromatic vinyl compound for example comprises vinylbenzene, Vinyl toluene, vinyl naphthalene, monochlorostyrene, dichlorostyrene, trichlorobenzene ethene, phenyl-monobromide ethene, Dowspray 9 and tribromo-benzene ethene.One or both or two or more aromatic vinyl compound are aggregated.Vinylbenzene is particularly preferred.
The polyphenylene oxide resin of modification be free radical form that agent exists or non-existent condition under by α, β-undersaturated carboxylic acid or derivatives thereof is grafted to the polymkeric substance that obtains on the polyphenylene oxide.
Free radical forms agent and comprises that peroxide radical forms agent, as benzoyl peroxide, peroxidation di-isopropyl, di-t-butyl peroxide, 1, two (tert-butyl peroxides) 3,3 of 1-, 5-trimethyl-cyclohexane and 2,5-dimethyl-two (tert-butyl peroxide)-hexane.
As α, the example of β-undersaturated carboxylic acid and derivative thereof can be mentioned toxilic acid, maleic anhydride, succsinic acid, succinyl oxide, himic acid, the himic acid acid anhydride, methylene-succinic acid, itaconic anhydride, citraconic anhydride, aconitic anhydride, monomethyl maleate, ethyl maleate, the metal-salt of ethyl maleate, monomethyl ester, vinyl benzoic acid, the vinyl fumaric acid, the metal-salt of monomethyl ester, glycidyl methacrylate, glycidyl acrylate, allyl glycidyl ether, vinyl glycidyl ether, glycidyl itoconate, vinylformic acid, methacrylic acid and maleimide.Particularly preferably be anhydride group.α, the grafting quantity of β-undersaturated carboxylic acid or derivatives thereof is preferably in 0.01-50% (mole) scope.If grafting quantity can produce undesirable result greater than 50% (mole), as yellow, molecular weight and molecular weight and resin gel.If this quantity, just can not be observed the effect of the intensity of improving the weld seam part less than 0.01% (mole).
When the polyphenylene oxide resin of the styrene polymer of styrene polymer that adds modification or modification and modification, its quantity is preferably 1-50% (weight) by polyphenylene oxide resin, and the quantity of the polyphenylene oxide resin of modification is preferably 1-100% (weight).
Find that further the resin combination that the present invention contains polyamide resin, polyphenylene oxide resin and inorganic filler improves the effect of moulded parts transparency surprisingly in addition except the effect of improving above-mentioned character.That is to say, by containing the polyamide of polyphenylene oxide resin (as poly-decyl amide (Ny6) with routine, polyhexamethylene adipamide (Ny66), the multipolymer (Ny66/6) of poly-decyl amide and polyhexamethylene adipamide, the moulded parts that the composition of the multipolymer (Ny6T/6I) of multipolymer of polyhexamethylene adipamide and polyhexamethylene terephthalamide (Ny66/6T) and polyhexamethylene terephthalamide and polyhexamethylene isophthaloyl amine makes does not have light transmission, and very high light transmission is arranged by the moulded parts that resin combination of the present invention makes, even when adding the high density inorganic filler, also can keep sufficiently high light transmission.These facts expected never in the technology of the composition that contains polymeric amide and polyphenylene oxide resin of routine that it was first by the present invention's explanation.So composition of the present invention is specially adapted to moulded parts such as the jar and the bottle of the liquid levels that is mounted in it from visual observation.
Use for these, need the resin combination of high light transmittance, however the moulded parts of high-surface gloss also needs because when inorganic filler was given prominence to moulded parts surperficial, light transmission can further decline.According to the technology of routine, when light transmission during, use no crystallization or low crystalline resin as important index, but the chemical-resistant variation of these resins.On the other hand,, use the crystalline resin, but light transmission variation in this case has only the thin-walled moulded parts could obtain sufficiently high light transmission, so sacrifices the intensity and the rigidity of moulded parts again when chemical-resistant during as important indicator.
The present invention has solved above-mentioned these problems at one stroke; The moulded parts of this resin combination has fabulous surface luster, intensity, rigidity, chemical-resistant and light transmission.
Below a fourth aspect of the present invention will be described.
Moulded parts of the present invention has fabulous surface luster to mean that such moulded parts is owing to the surperficial caused blushing that inorganic filler is projected into goods visually is not observed, and, when measuring moulded parts surperficial with glossmeter (JIS K-7105), gloss number is 90% of 50 glossiness or the higher zone whole surf zone that accounts for moulded parts at least.
Moulded parts with high-surface gloss of the present invention is used to need the goods of fabulous outward appearance and with other materials the goods of slide unit is arranged, and the goods that need sliding capability.
Such examples of applications is that furniture is (as the leg and the seat of chair, the leg of desk, and the parts of cabinet and chest), office accommodations (as the shell of notebook-PC), the internal and external ornament thing of automobile is (as the peephole stay, wheel rim, wheel hub cover, wiper, electric fan, the seat locking piece, gear, lamp housing, spoiler, the decorations cover, the rly. group, slide switch, limit switch, the switchgroup handle, fuel reserve tank and fuel oil drum), electrical appliance is (as belt pulley, gear and blast heater shell), also have attachments of a bicycle in addition (as wheel rim, spoke, seat, seat supports, handle, support and splash pan), valve casing, nail, screw, bolt, nut, jar and bottle.
Resin combination of the present invention also can contain antioxidant, UV light absorber, thermo-stabilizer, the rotten inhibitor of light, tinting material (as dyestuff and pigment), softening agent, lubricant, release agent, nucleating agent and fire retardant, and they normally are added in the polyamide resin.In addition, other polyamide resins or other thermoplastic resins also can with the blending of this composition.
Below some non-limiting examples illustrate in greater detail the present invention.
The evaluation of sample is carried out in order to following method in kind of embodiment and Comparative Examples.
(1) relative viscosity (η r): the concentration that polymkeric substance is risen with 1.0 Grams Per Minutes is dissolved in 95.5 ± 0.03% the sulfuric acid, measures relative viscosities with the Ostwald viscometer tube down at 25 ℃.
(2) terminal carboxyl(group) ratio: polymkeric substance is dissolved in 90% phenol solution, and, obtains amino group concentration (25 ℃) ((NH with l/40N salt acidometric titration
2)).Polymkeric substance is dissolved in the phenylcarbinol, and, obtains carboxyl concentration (phenolphthalin is as indicator) (160 ℃) ((COOH)) with the titration of l/10N KOH ethylene glycol solution.Terminal carboxyl(group) is than using following formula by amino group concentration ((NH
2)) and carboxyl concentration ((COOH)) calculating.
(3) tensile property: ASTM D638
(4) flexural property ASTM D790
(5) surface luster: the plate of one 130 millimeters * 130 millimeters * 3 mm thick made from Toshiba Machine Co.Ltd. of injection moulding machine IS150E molding, when inorganic filler is 33% (weight) or still less the time, gate size is 2 millimeters * 3 millimeters; When inorganic filler during greater than 33% (weight) gate size be 6 millimeters * 3 millimeters.Condition of moulding is: 80 ℃ of 290 ℃ of barrel temperatures, die temperature and 120 ℃, 10/20 second injection moulding/cooling period, injection pressure 34.3MPa and injecting rate 50%.The surface luster of the moulded parts that generates is pressed JIS K7105 method Horiba Co., and the Portable glossmeter IG320 that Ltd. makes measures.
(6) dimensional performance: use the moulded parts that in surface luster is estimated, obtains, obtain the rosin size on flow direction, and obtain size changing rate to die size with following formula.
Size changing rate={ ((die size)-(moulded parts size))/(die size) } * 100 (%)
(7) water adsorption equilibrium condition: moulded parts is placed in 23 ℃, the atmosphere of relative temperature 50%, until water adsorption ratio reaches balance.
(8) water adsorption ratio: test the weight of exemplar and the weight of suction back test exemplar after measuring firm molding, water adsorption ratio calculates with following formula.
(9) heat-resistant aging: molding exemplar (3 mm thick) is placed the stove that is controlled at 180 ℃, obtain tensile strength and reach the preceding required time of 50% retention rate.
(10) photostabilization: the exemplar (3 mm thick) of molding is put into weatherometer at sunshine (had 18 minutes at 63 ℃ during 2 hours, use neon lamp as light source), shone 3000 hours.Observe the surface of exposure exemplar, check the appearance and the surperficial fading extent of crackle, compare with molding exemplar before the exposure.
(11) intensity of weld seam part: press ASTM D638 method, the test exemplar of measuring the intensity of weld seam part with shown in Figure 1 being used to obtains tensile strength.
(12) transmission: the box pattern that makes a thickness and be 3 millimeters is moulded goods, and water is full of wherein.With the naked eye judge whether to see from the outside surface of water breakthrough.
Following polymkeric substance and raw material are used for embodiment and Comparative Examples.
(1) polymkeric substance
(1) polyhexamethylene adipamide (Ny66): LEONA 1300 and LEONA1200, made by Asahi kasei Kogyo K.K..
(2) multipolymer (Ny66/6I) of polyhexamethylene adipamide and polyhexamethylene isophthaloyl amine: it is by preparation embodiment 1 preparation.
(3) multipolymer of polyhexamethylene adipamide and poly-decyl amide (Ny66/6), the multipolymer (Ny66/6T) of polyhexamethylene adipamide/polyhexamethylene terephthalamide, the polyhexamethylene adipamide, the multipolymer (Ny66/6T/6I) of polyhexamethylene terephthalamide and polyhexamethylene isophthaloyl amine, poly-inferior m-xylene base adipamide (NyMXD6): these polymkeric substance are by preparing the following feedstock production of embodiment 1: the salt of equimolar hexanodioic acid and hexamethylene-diamine, ε-Ji Neixianan, the salt of equimolar m-phthalic acid and hexamethylene-diamine, the salt of equimolar terephthalic acid and hexamethylene-diamine and etc. the salt of mole m-xylylene amine and hexanodioic acid.
(4) multipolymer (Ny6I/6T) of polyhexamethylene isophthaloyl amine and polyhexamethylene terephthalamide, polyhexamethylene isophthaloyl amine (Ny6I): these polymkeric substance are used following feedstock production: the salt of the salt of equimolar m-phthalic acid and hexamethylene-diamine and equimolar terephthalic acid and hexamethylene-diamine by preparation embodiment 2.
(5) poly-decyl amide (Ny6): by the product of Asahi Kasei Kogyo K.K. manufacturing.
(6) polyphenylene oxide (PPE): by the product of Asahi Kasei Logyo K.K. manufacturing.
(7) polystyrene of maleic anhydride graft (Compatibilizer C 1): it is by preparation embodiment 3 preparations.
(8) polyphenylene oxide of maleic anhydride graft (Compatibilizer C 2): it is by preparation embodiment 4 preparations.
(2) inorganic filler:
(1) glass fibre (GF): by Asahi Fiber Glass Co., the 03JA416 that Ltd. makes.
(2) talcum: by the CRS6002 of Tatsumori K.K. manufacturing.
(3) roasting kaolin: by the SATINTONF W of Engelhard Co. manufacturing.
(4) mica: by the M-400T of Lepco Co. manufacturing.
(5) carbon fiber (CF): by the Hi-Carbolon A-9000 of Shin Asahi Kasei Carbon Fiber K.K. manufacturing.
Preparation embodiment 1
The salt of the salt of 2.00 kilograms of equimolar hexanodioic acids and hexamethylene-diamine, 0.50 kilogram of equimolar m-phthalic acid and hexamethylene-diamine and 2.5 kilograms of pure water are packed in 5 liters of autoclaves, and fully stir.Use N
2Fully after the atmosphere in the displacement autoclave, under agitation, in about 1 hour, temperature is raised to 220 ℃ from room temperature.Owing to press in the autogenous pressure that water vapor produces in the autoclave makes and reach 1.77MPa (gauge pressure).Continue to heat from reactive system, to remove simultaneously and anhydrate, be no more than 1.77MPa (gauge pressure) so that press in making.Behind the reheat 2 hours, when internal temperature reaches 260 ℃, stop heating, and close the baiting valve of autoclave, greatly in 8 hours with the material cool to room temperature.After this, open autoclave, take out about 2 kilograms of polymkeric substance, and grind.The broken polymkeric substance that generates is put into 10 liters of vaporizers, and in 200 ℃ of following nitrogen gas stream, carry out 10 hours solid state polymerizations.Because the result of solid state polymerization, sulfuric acid relative viscosity η r (1 gram polymkeric substance/100 milliliter 95.5% sulfuric acid is measured down at 25 ℃) brings up to 2.30 from 1.38.
Preparation embodiment 2
The salt of the salt of 1.75 kilograms of equimolar m-phthalic acids and hexamethylene-diamine, 0.75 kilogram of equimolar terephthalic acid and hexamethylene-diamine and 2.5 kilograms of pure water are packed in 5 liters of autoclaves, and fully stir.After fully replacing atmosphere in the autoclave with nitrogen, under agitation in about 2 hours, temperature is raised to 250 ℃ from room temperature.Reach 24.5MPa (gauge pressure) owing to press in the autogenous pressure that the interior water vapor of autoclave produces makes, continue to heat from reactive system, to remove simultaneously and anhydrate, be no more than 24.5MPa (gauge pressure) so that press in making.Behind the reheat 2 hours, when internal temperature reaches 300 ℃, in about 1 hour, interior pressure is dropped to normal pressure gradually.Under internal temperature is 300 ℃ and normal pressure, reaction was carried out 1 hour again.After this, cut off well heater, and in about 8 hours with the reaction product cool to room temperature.After the cooling, open autoclave, take out about 2 kilograms of polymkeric substance, and grind.The broken polymkeric substance that generates under 100 ℃ in nitrogen gas stream dry 24 hours.
Preparation embodiment 3
104 gram polystyrene (by Wako Jun-yaku Co.Ltd, manufacturing) and 98 are restrained maleic anhydrides be dissolved in 400 milliliters of neighbour-dichlorobenzene, solution is heated in 120 ℃ of following dry nitrogen air-flows and stir.Then, (" NYPERBO " is by Nippon Oil ﹠amp with dioctyl terephthalate with 20 grams; Fats Co., Ltd. makes) be diluted to the solution that 50% benzoyl peroxide is dissolved in 40 milliliters of neighbour-dichlorobenzene and slowly add wherein, allow be reflected in 120 ℃ of following exsiccant nitrogen gas stream and carried out 6 hours.After reacting completely, again 500 milliliters of neighbours-dichlorobenzene is added diluted reaction mixture.Then, reaction mixture is added in two ketone makes polymer precipitation.With acetone thorough washing polymkeric substance, and, obtain desired product 80 ℃ of following vacuum-dryings.With the grafting quantity of the titrating method measurement of sodium methylate maleic anhydride, finding has 1.7% (mole) maleic anhydride graft to polystyrene.
Preparation embodiment 4
36.4 gram polyphenylene oxide and 29.4 gram maleic anhydrides are dissolved in 200 milliliters of p-Xylol, solution is heated in 1 20 ℃ of following dry nitrogen air-flows and stir.Then, with 5.8 gram dioctyl terephthalate (" NYPER BO ", Nippon Oil ﹠amp; Fats Co.Ltd. makes) be diluted to the solution that 50% benzoyl peroxide is dissolved in 50 milliliters of p-Xylol and slowly be added in the solution, allow be reflected in 120 ℃ of following dry nitrogen air-flows and carried out 5 hours.After reacting completely, again 200 milliliters of p-Xylol are added with diluted reaction mixture.Then, will react to mix to be added to and make polymer precipitation in the acetone.With acetone thorough washing polymkeric substance, and, obtain required product 80 ℃ of following vacuum-dryings.With the grafting quantity of the titrating method measurement of sodium methylate maleic anhydride, find that the maleic anhydride of 1.2% (mole) is grafted on the polyphenylene oxide.
Preparation embodiment 5
With following method polymkeric substance and inorganic filler are mediated.
(made by Werner Co., barrel temperature ZSK25) is fixed on 280 ℃, and polymkeric substance is incorporated into the extruding machine from hopper, and the screw rod speed of rotation is 100 rev/mins with Bitruder.Middle part at the tube material adds inorganic filler.When using two or more inorganic fillings, they also separately add from the middle part of barrel, and the inorganic filler except that GF can adhere to 1 part heavy y-aminopropyltriethoxywerene werene by per 100 parts of heavy inorganic fillers in advance.Fully wash polymkeric substance and inorganic filler intake with nitrogen, and the part of any vacuumizes (0.87MPa) by exhaust before the discharge opening of extruding machine.Discharge quantity be the 8.0-10 kilogram/hour, resin temperature is 290-215 ℃.
The bead and each hundred parts of resin 0.13 part of montanic acid sodium blending and the molding that generate.
Embodiment 1-1.3.
Preparation contains the molding exemplar of the composition shown in table 1 and 2, and measures the outward appearance of molding exemplar, tensile property, flexural property and dimensional stability (table 1 and 2).The outward appearance of all compositions is subjected to that the influence of die temperature is all very little all a fabulous surface luster, because the decline of intensity that suction causes and Young's modulus is very little, the dimensional change of moulded parts is very little when molding.
Comparative Examples 1-4 and 17
Prepare as shown in table 3 containing the Ny66 polymkeric substance and use inorganic filler enhanced composition, and above-mentioned identical method evaluation.Under these conditions even when improving the temperature of mould, can not obtain the moulded parts of high-surface gloss by these materials.In addition, because the intensity that suction causes and the decline of Young's modulus are big, dimensional change is also very big.
Comparative Examples 5-7 and 10
Preparation is also estimated the GF enhanced composition that contains Ny6, Ny66/6 multipolymer and Ny66/Ny6 alloyed polymer that is used as the material that good processing is arranged usually.Can obtain the moulded parts of high-surface gloss by these materials, but because the intensity and the Young's modulus low (table 3 and 4) of suction moulded parts.
Comparative Examples 8,9,11,12, l4 and 16.
Preparation and evaluation contain the GF enhanced composition of the known polymeric amide of aromatic ring component.Can obtain that by these materials suction is had high strength and high elastic coefficient, moulded parts that dimensional change is little, but their surface luster is poor, and gloss obviously depends on die temperature.Surface luster is not too even when the tool moulded parts is put in order in observation, the part blushing occurs owing to inorganic filler is projected into the surface, and is relevant with the kind of mould therefor.These problems its commercial value is descended and with the sliding variation of other materials.
Comparative Examples 13.
Preparation contains the Ny66/6I polymkeric substance of 50% (weight) Ny6I component, and makes GF enhanced composition with above-mentioned identical method.As shown in table 4, when the Ny6I components contents surpasses scope of the present invention, the rapid variation of surface luster.
Comparative Examples 15
It is 3.20 GF enhanced composition that preparation contains Ny66/6I, η r.As shown in table 4, when molecular weight is too high, mobile variation, under above-mentioned condition of moulding, said composition can not be full of mould.
Comparative Examples 18
It is 1.40 50%GF enhanced composition that same preparation contains Ny66/6I (80/20% (weight)) polymkeric substance, relative viscosity η r.But when molding, material appears leaking in mould machine barrel nozzle top, so it fully can not the charging molding.
Comparative Examples 19
It is 2.20 75%GF enhanced composition that same preparation contains Ny66/6I (80/20% (weight)) polymkeric substance, relative viscosity η r.But the flowability of this resin combination is poor, and said composition can not be full of mould like this.Therefore, can not make moulded parts.
Embodiment 14-22
In preparation embodiment 1, before the beginning polymerization, add the aqueous solution of each cupric iodide, potassiumiodide and manganous lactate, its concentration is as shown in table 5, begins polymerization then.Control the carboxyl ratio in the equimolar salt brine solution by further hexanodioic acid being added to.With preparation method identical among the embodiment 5 33%GF is attached in the polymkeric substance of generation.
The composition that generates is by molding, and tensile property, flexural property, outward appearance, dimensional change, photostabilization and the heat-resistant aging of measurement moulded parts.The result lists table 5 in.
Comparative Examples 20-26
With above-mentioned identical method preparation and evaluation composition.The result lists table 6 in.
Embodiment 23-30
With the preparation Ny66/6I, PPE polymkeric substance and the mixture C1 that make of embodiment 1 or C2 in the pre-blending of the ratio shown in the table 7, and under the identical extruding condition of preparation embodiment 5 by its preparation GF enhanced composition.
Estimate tensile property, flexural property, outward appearance, dimensional change, weld strength and the light transmission of moulded parts.The result lists table 7 in.
Comparative Examples 27-29
With above-mentioned identical method preparation and evaluation composition.The result lists table 7 in.
Just as explained above, the invention provides a kind of resin combination, it has the required high-surface gloss of structural member under very wide condition of moulding, fabulous intensity is arranged in actual applications, rigidity and dimensional stability.Except above-mentioned characteristic, this resin combination also has other characteristics, as photostabilization, heat-resistant aging and light transmission.The present invention also provides and contains above-mentioned composition, and the moulded parts of fabulous surface luster is arranged.
Table 1
| Project | Unit | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 | Embodiment 6 | Embodiment 7 | Embodiment 8 | |
| Type of polymer (ratio of components) | (WT％) | NY66/6I (80/20) | NY66/6I (90/10) | NY66/6I (75/25) | NY66/6I (80/20) | NY66/6I (80/20) | NY66/6I (80/20) | NY66/6I (80/20) | NY66/6I (80/20) | |
| ηr | 2.20 | 2.40 | 2.25 | 1.70 | 2.33 | 2.50 | 2.60 | 2.35 | ||
| The kind of inorganic filler and quantity | GF50％ | GF50％ | GF50％ | GF50％ | GF42％ | GF33％ | GF15％ | GF30% mica 30% | ||
| Outward appearance | 80 ℃ of molding temperatures | Gloss | 80 | 78 | 85 | 88 | 90 | 85 | 90 | 75 |
| 120 ℃ of molding temperatures | Gloss | 85 | 80 | 88 | 91 | 92 | 89 | 93 | 80 | |
| Just behind the molding | Tensile strength | 9.8×10 4Pa | 2,570 | 2,470 | 2,580 | 2,400 | 2,300 | 1,950 | 1,250 | 2,100 |
| Flexural strength | 9.8×10 4Pa | 3,740 | 3,700 | 3,750 | 3,700 | 3,300 | 2,860 | 1,800 | 3,000 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 150,000 | 145,000 | 152,000 | 150,000 | 130,000 | 104,000 | 55,000 | 181,000 | |
| After the suction balance | Tensile strength | 9.8×10 4Pa | 2,270 | 2,150 | 2,280 | 2,300 | 2,150 | 1,760 | 1,100 | 1,950 |
| Flexural strength | 9.8×10 4Pa | 3,430 | 3,120 | 3,430 | 3,500 | 3,150 | 2,400 | 1,550 | 2,900 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 160,000 | 135,000 | 159,800 | 162,000 | 128,000 | 95,000 | 4,700 | 180,000 | |
| Water-intake rate | ％ | 0.91 | 0.98 | 0.88 | 0.90 | 1.10 | 1.25 | 1.60 | 0.75 | |
| Dimensional change | ％ | 0.52 | 0.54 | 0.48 | 0.53 | 0.59 | 0.64 | 0.90 | 0.35 | |
Table 2
| Project | Unit | Embodiment 9 | Embodiment 10 | Embodiment 11 | Embodiment 12 | Embodiment 13 | |
| Type of polymer (ratio of components) | (WT％) | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | |
| nr | 2.30 | 2.33 | 2.40 | 2.33 | 2.30 | ||
| The kind of inorganic filler and quantity | Talcum 17% roasting kaolin 21% | GF 10% roasting kaolin 21% | GF20% talcum 11% roasting Jian kaolin 13% | GF15％ CF10％ | CF15％ | ||
| Outward appearance | 80 ℃ of molding temperatures | Gloss | 86 | 87 | 80 | 80 | 86 |
| 120 ℃ of molding temperatures | Gloss | 90 | 91 | 83 | 88 | 90 | |
| Just behind the molding | Tensile strength | 9.8×10 4Pa | 1,050 | 1,300 | 1,480 | 2,000 | 1,800 |
| Flexural strength | 9.8×10 4Pa | 1,700 | 2,000 | 2,100 | 3,000 | 2,700 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 70,000 | 68,000 | 98,000 | 110,000 | 100,000 | |
| After the suction balance | Tensile strength | 9.8×10 4Pa | 900 | 1,200 | 1,300 | 1,800 | 1,650 |
| Flexural strength | 9.8×10 4Pa | 1,500 | 1,850 | 1,900 | 2,850 | 2,550 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 58,000 | 60,000 | 90,000 | 100,000 | 93,000 | |
| Water-intake rate | ％ | 1.12 | 1.10 | 1.08 | 1.28 | 1.50 | |
| Dimensional change | ％ | 0.45 | 0.50 | 0.46 | 0.90 | 0.75 | |
Table 3
| Project | Unit | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 | |
| Type of polymer (ratio of components) | (WT％) | Ny66 | Ny66 | Ny66 | Ny66 | Ny6 | |
| nr | 2.30 | 2.62 | 2.64 | 2.64 | 2.33 | ||
| The kind of inorganic filler and quantity | GF50％ | GF42％ | GF33％ | GF15％ | GF50％ | ||
| Outward appearance | 80 ℃ of molding temperatures | Gloss | 7 | 10 | 11 | 18 | 75 |
| 120 ℃ of molding temperatures | Gloss | 12 | 15 | 18 | 22 | 80 | |
| Just behind the molding | Tensile strength | 9.8×10 4Pa | 2,380 | 2,200 | 1,900 | 1,150 | 2,300 |
| Flexural strength | 9.8×10 4Pa | 3,520 | 3,200 | 2,700 | 1,750 | 3,400 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 148,000 | 125,000 | 91,000 | 52,000 | 140,000 | |
| After the suction balance | Tensile strength | 9.8×10 4Pa | 1,700 | 1,650 | 1,350 | 850 | 1,490 |
| Flexural strength | 9.8×10 4Pa | 2,560 | 2,400 | 2,100 | 1,100 | 2,180 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 110,800 | 85,000 | 63,000 | 25,000 | 89,700 | |
| Water-intake rate | ％ | 1.38 | 1.42 | 1.70 | 2.10 | 1.63 | |
| Dimensional change | ％ | 0.80 | 0.85 | 0.90 | 1.20 | 0.70 | |
Table 3 (continuing)
| Comparative Examples 6 | Comparative Examples 7 | Comparative Examples 8 | Comparative Examples 9 |
| Ny66/6 (90/10) | Ny66/Ny6 | Ny66/6T | Ny6I/6T |
| 2.34 | 2.63 | 2.33 | 2.24 |
| GF50％ | GF50％ | GF50％ | GF50％ |
| 63 | 56 | 20 | 15 |
| 75 | 62 | 32 | 20 |
| 2,440 | 2,400 | 2,400 | 2,450 |
| 3,650 | 3,620 | 3,620 | 3,700 |
| 147,500 | 145,000 | 140,500 | 149,000 |
| 1,630 | 1,550 | 2,250 | 2,400 |
| 2,470 | 2,400 | 3,480 | 3,750 |
| 100,300 | 89,000 | 145,500 | 150,000 |
| 1.56 | 1.59 | 0.65 | 0.30 |
| 0.69 | 0.69 | 0.60 | 0.25 |
Table 4
| Project | Unit | Comparative Examples 10 | Comparative Examples 11 | Comparative Examples 12 | Comparative Examples 13 | Comparative Examples 14 | |
| Type of polymer (ratio of components) | (WT％) | Ny66/Ny6 (70/30)Blend | Ny66/6T/6I (50/30/20) | Ny6I/Ny66 (93/7)blend | Ny66/6I (50/50) | Ny6I | |
| ηr | 2.60 | 2.20 | 2.20 | 2.30 | 2.10 | ||
| The kind of inorganic filler and quantity | GF42％ | GF50％ | GF42％ | GF50％ | GF50％ | ||
| Outward appearance | 80 ℃ of molding temperatures | Gloss | 60 | 12 | 24 | 18 | 20 |
| 120 ℃ of molding temperatures | Gloss | 75 | 44 | 48 | 42 | 40 | |
| Just behind the molding | Tensile strength | 9.8×10 4Pa | 2,100 | 2,340 | 2,300 | 2,350 | 2,500 |
| Disturb Qu Qiangdu | 9.8×10 4Pa | 3,100 | 3,420 | 3,250 | 3,500 | 3,800 | |
| Disturb modulus in elasticity in bending | 9.8×10 4Pa | 117,000 | 144,000 | 135,000 | 145,000 | 151,000 | |
| After the suction balance | Tensile strength | 9.8×10 4Pa | 1,400 | 1,960 | 2,200 | 1,900 | 2,450 |
| Disturb Qu Qiangdu | 9.8×10 4Pa | 1,800 | 3,000 | 3,200 | 2,900 | 3,700 | |
| Disturb modulus in elasticity in bending | 9.8×10 4Pa | 60,000 | 143,500 | 137,000 | 144,000 | 150,000 | |
| Water-intake rate | ％ | 1.58 | 1.45 | 0.40 | 1.46 | 0.29 | |
| Dimensional change | ％ | 0.72 | 0.26 | 0.35 | 0.25 | 0.26 | |
Table 4 (continuing)
| Comparative Examples 15 | Comparative Examples 16 | Comparative Examples 17 |
| Ny66/6I (80/20) | NMXD6/Ny66 (90/10)blend | Ny66 |
| 3.20 | 2.40 | 2.55 |
| GF50％ | GF50％ | 11% roasting of CG20% talcum is to mountain range soil 13% |
| Can not be full of | 10 | 13 |
| Can not be full of | 85 | 18 |
| 2,650 | 2,750 | 1,410 |
| 3,850 | 3,990 | 2,100 |
| 155,000 | 176,000 | 91,000 |
| 2,430 | 2,490 | 1,060 |
| 3,500 | 3,610 | 1,600 |
| 159,000 | 176,000 | 59,000 |
| 0.95 | 0.86 | 1.10 |
| 0.50 | 0.26 | 0.70 |
Table 5
Table 5 (continuing)
1) zero: crack △ do not occur: part occur the crack *: many cracks 2 appear) ◎: do not change zero basically: have some to change △: sizable variation *: big variation
| Embodiment 19 | Embodiment 20 | Embodiment 21 | Embodiment 22 |
| Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) |
| 2.33 | 2.40 | 2.20 | 2.40 |
| 75 | 80 | 85 | 80 |
| GF33 | GF33 | GF33 | GF33 |
| 64 | 96 | 130 | 3 |
| 27 | 25 | 25 | 25 |
| 10 | 10 | 10 | 30 |
| 1,900 | 1,950 | 1,950 | 1,920 |
| 2,900 | 2,920 | 2,930 | 2,900 |
| 106,000 | 106,000 | 106,000 | 105,000 |
| 1,700 | 1,710 | 1,730 | 1,750 |
| 2,400 | 2,400 | 2,450 | 2,450 |
| 97,000 | 96,000 | 96,000 | 95,000 |
| 88 | 87 | 90 | 86 |
| 0.65 | 0.63 | 0.63 | 0.64 |
| ○ | ○ | ○ | ○ |
| ○ | ○ | ○ | ◎ |
| 550 | 620 | 750 | 120 |
Table 6
Table 6 (continuing)
1) zero: crack △ do not occur: part occur the crack *: many cracks 2 appear) ◎: do not change zero basically: have some to change △: sizable variation *: big variation
| Comparative Examples 19 | Comparative Examples 20 | Comparative Examples 21 |
| Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) |
| 2.38 | 2.33 | 2.60 |
| 79 | 75 | 60 |
| GF33 | GF33 | GF33 |
| 15 | 15 | 64 |
| 40 | 15 | 27 |
| 10 | 10 | 10 |
| 1,950 | 1,920 | 1,920 |
| 2,900 | 2,880 | 2,75 |
| 106,000 | 106,000 | 92,000 |
| 1,720 | 1,760 | 1,350 |
| 2,400 | 2,450 | 2,150 |
| 95,000 | 96,000 | 64,000 |
| 88 | 87 | 12 |
| 0.64 | 0.64 | 0.90 |
| ○ | ○ | ○ |
| △ | △ | ○ |
| 250 | 130 | 450 |
Table 7
| Embodiment 23 | Embodiment 24 | Embodiment 25 | Embodiment 26 | Embodiment 27 | |||
| The polymeric amide kind | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66/6I (80/20) | ||
| PPE 1) | Part is heavy | 10 | 25 | 33 | 43 | 25 | |
| Mixture (C1) 2) | wt％ | 0 | 0 | 0 | 0 | 20 | |
| Mixture (C2) 2) | wt％ | 0 | 0 | 0 | 0 | 0 | |
| The PPE+ mixture | Part is heavy | 10 | 25 | 33 | 43 | 30 | |
| The quantity of GF weighting agent | wt％ | 33 | 33 | 33 | 33 | 33 | |
| Just behind the molding | Tensile strength | 9.8×10 4Pa | 1,900 | 1,850 | 1,800 | 1,700 | 1,920 |
| Flexural strength | 9.8×10 4Pa | 2,880 | 2,850 | 2,700 | 2,610 | 2,900 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 110,000 | 110,000 | 100,000 | 93,000 | 112,000 | |
| After the suction balance | Tensile strength | 9.8×10 4Pa | 1,780 | 1,800 | 1,770 | 1,660 | 1,850 |
| Scratch and stretch intensity | 9.8×10 4Pa | 2,600 | 2,700 | 2,650 | 2,580 | 2,740 | |
| Flexural modulus of elasticity | 9.8×10 4Pa | 105,000 | 106,000 | 98,000 | 91,000 | 110,000 | |
| Outward appearance (80 ℃ of die temperatures) | Gloss | 83 | 85 | 88 | 87 | 89 | |
| Dimensional change | ％ | 0.55 | 0.53 | 0.50 | 0.48 | 0.53 | |
| Weld strength | 9.8×10 4Pa | 600 | 590 | 560 | 500 | 700 | |
| Light transmission | ◎ | ◎ | ◎ | ◎ | ○ | ||
Table 7 (continuing)
1) quantity 2 of per 100 parts of polyamide resin weight) by the % (weight) 3 of PPE resin) replace PPE resin 4 with the PPE resin of 33 parts of heavy toxilic acid modifications) by the quantity 5 of resin combination) and ◎: clearly see water surface zero: see slightly water surface *: not exclusively see water surface
| Embodiment 28 | Embodiment 29 | Embodiment 30 | Comparative Examples 27 | Comparative Examples 28 | Comparative Examples 29 |
| Ny66/6I (80/20) | Ny66/6I (80/20) | Ny66 | Ny6 | Ny6 | Ny66/6I (80/20) |
| 33 | 33 | 03) | 33 | 33 | 100 |
| 0 | 0 | 0 | 0 | 0 | 20 |
| 30 | 30 | 100 | 30 | 30 | 0 |
| 43 | 43 | 33 | 43 | 43 | 100 |
| 33 | 33 | 33 | 33 | 33 | 33 |
| 2,070 | 2,300 | 1,980 | 2,000 | 1,780 | 1,720 |
| 2,950 | 3,300 | 2,800 | 2,900 | 2,520 | 2,630 |
| 115,000 | 160,000 | 112,000 | 102,000 | 95,200 | 94,000 |
| 1,950 | 2,200 | 1,900 | 1,450 | 1,220 | 1,680 |
| 2,850 | 3,150 | 2,730 | 2,400 | 2,150 | 2,600 |
| 111,000 | 162,000 | 110,000 | 87,000 | 65,000 | 93,000 |
| 85 | 80 | 85 | 8 | 68 | 45 |
| 0.51 | 0.40 | 0.49 | 0.85 | 0.65 | 0.40 |
| 720 | 750 | 800 | 600 | 570 | 470 |
| ◎ | ◎ | ◎ | × | × | ◎ |
Claims (3)
1. Amilan polyamide resin composition, it contains:
(A) a kind of polyamide component, this component is the 30-95% (weight) of Amilan polyamide resin composition, it is a kind of partially aromatic polyamide, the hexa-methylene adipamide units that forms by (a) 70-95% (weight) hexanodioic acid and hexamethylene-diamine and (b) the hexa-methylene isophthaloyl amine unit that forms of 5-30% (weight) m-phthalic acid and hexamethylene-diamine form, its sulphuric acid soln viscosities il r is 1.5-2.8;
(B) at least a inorganic filler of 5-70% (weight), it is selected from glass fibre, carbon fiber, mica, talcum, kaolin, wollastonite, lime carbonate and potassium titanate.
2. according to the Amilan polyamide resin composition of claim 1, wherein the terminal carboxyl(group) of polymeric amide ratio is 65% or higher, and said composition also contains and satisfies following formula (the 1)-copper compound of (3) ratio and the mixture of iodine compound and/or manganic compound:
(1) 0.5ppm≤copper≤150ppm
(2) 20≤iodine/copper≤30 (grammeatom ratio)
(3) 0.5ppm≤manganese≤60ppm
3. according to the Amilan polyamide resin composition of claim 1, wherein said composition also contains polyphenylene oxide, and its content is that per 100 parts of reunion amide resinss contain 5-80 part weight polyphenylene ether.
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| CN1072688C (en) * | 1996-12-26 | 2001-10-10 | 中国科学院长春应用化学研究所 | Preparation of polyadipic acid and hexanediamine composite materials |
| JP4542035B2 (en) * | 2002-07-23 | 2010-09-08 | 株式会社カネカ | Polyamide resin composition and method for producing the same |
| CZ298882B6 (en) * | 2003-03-28 | 2008-03-05 | Výzkumný ústav stavebních hmot, a. s. | Heat resistant structural insulating material |
| JP4469149B2 (en) * | 2003-08-07 | 2010-05-26 | ダイセルポリマー株式会社 | Thermoplastic resin composition and molded article |
| CA2579806A1 (en) * | 2004-09-27 | 2006-04-06 | Kuraray Co., Ltd. | Binder fiber and separator for alkaline cell using same |
| DE102004063220A1 (en) * | 2004-12-29 | 2006-07-13 | Degussa Ag | Transparent molding compounds |
| EP1788027B1 (en) * | 2005-11-18 | 2007-07-18 | EMS-Chemie AG | Reinforced polyamide moulding compositions |
| CN101432362B (en) * | 2006-04-27 | 2011-04-06 | 旭化成化学株式会社 | Resin composition, and automotive underhood component produced using the resin composition |
| CN101104735B (en) * | 2006-07-11 | 2012-10-17 | 上海普利特复合材料有限公司 | High glazing and high liquidity glass fiber-reinforced nylon 6 composite material and preparation method thereof |
| KR101422585B1 (en) * | 2006-07-26 | 2014-07-24 | 바스프 에스이 | Thermoplastic moulding compositions with high stiffness |
| US9505912B2 (en) * | 2006-08-23 | 2016-11-29 | Basf Se | Polyamide molding materials with improved thermal aging and hydrolysis stability |
| CN104448809A (en) * | 2013-09-25 | 2015-03-25 | 上海杰事杰新材料(集团)股份有限公司 | Glass fiber/mineral composite enhanced modified semi-aromatic nylon material and preparation method thereof |
| EP2930212B1 (en) * | 2014-04-08 | 2019-04-10 | Ems-Patent Ag | Electrically conductive polyamide moulding compositions |
-
1993
- 1993-12-23 CN CN 93112789 patent/CN1035771C/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| CN1104225A (en) | 1995-06-28 |
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