JP2016098240A - Polyamide resin molded article - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a polyamide resin molded article excellent in flowability during molding, high in mechanical strength, rigidity and toughness and exhibiting low contractility.SOLUTION: There is provided a polyamide resin molded article by molding a polyamide resin composition containing 100 pts.wt. of (A) a polyamide resin having a ratio of an amino terminal group concentration (a) [mol/g] and a carboxyl terminal group concentration (b) [mol/g] ((a)/(b)) of 0.3 to 0.8 and 10 to 235 pts.wt. of (B) a glass fiber and having weight average fiber length of the glass fiber in the polyamide resin molded article in a range of 300 to 800 μm.SELECTED DRAWING: None

Description

  The present invention relates to a glass fiber reinforced polyamide resin molded article having high mechanical strength, rigidity, toughness and low shrinkage.

  Polyamide resins have excellent mechanical properties such as tensile strength, bending strength, and elastic modulus, as well as good heat resistance and chemical resistance, so they are widely used in electrical and electronic parts, automotive parts, building material parts, mechanical parts, etc. It's being used. Among them, glass fiber reinforced polyamide resin has excellent heat resistance, oil resistance, and toughness, and is widely used as a material for electronic device parts such as mobile phones and personal computer casings, and parts in the engine compartment of automobiles. . In recent years, molded products such as electronic equipment parts and automobile parts are required to be thinner, smaller, and lighter, and the demand for improving mechanical properties is increasing. On the other hand, glass fiber reinforced polyamide resins having high strength, high rigidity and high toughness have been studied.

  Regarding such a glass fiber reinforced polyamide resin, as a glass fiber reinforced thermoplastic resin excellent in mechanical properties and moldability, for example, a glass fiber length distribution in a resin obtained by adding glass fiber to a thermoplastic resin and melt-kneading the resin. Among them, a glass fiber reinforced thermoplastic resin composition in which the content of 500 μm or more is 15 to 70% by weight and the content of 1500 μm or more is 10% by weight or less has been proposed (for example, see Patent Document 1). In addition, as a reinforced polyamide resin composition excellent in surface appearance stability, impact resistance characteristics, and high-temperature rigidity, it contains a specific copolymer polyamide and a fibrous reinforcing material, and the weight average fiber length of the fibrous reinforcing material in the pellets A long fiber reinforced polyamide resin composition pellet that is substantially the same as the length of the pellet has been proposed (see, for example, Patent Document 2). However, these long glass fiber reinforced resin compositions have low fluidity. For example, when a thin part having a thickness of 1 mm or less is molded, there is a problem that appearance defects of short shot parts and flow end parts occur.

  On the other hand, as a resin composition excellent in molded article surface smoothness, for example, it is a resin composition containing a polyamide resin and glass fibers, and the weight average fiber length of the glass in the composition is in the range of 100 to 400 μm. There is proposed a welding resin composition in which the ratio of glass fibers having a fiber length of 60 μm or less accounts for 10 to 50% by weight of all glass fibers (see, for example, Patent Document 3). Also, there is a method for producing a resin composition pellet in which a resin and a fibrous filler having a weight average fiber length of 1 mm or more are supplied to an extruder, and the weight average fiber length of the fibrous filler in the pellet is 180 to 360 μm. It has been proposed (see, for example, Patent Document 4). However, molded articles obtained using these glass fiber reinforced resin compositions have a problem that the molding shrinkage ratio is large because the mechanical strength and rigidity are low and the reinforcing effect is low.

JP-A-8-134264 JP 2014-015592 A JP-A-10-231421 International Publication No. 2005/099984

  An object of the present invention is to provide a polyamide resin molded article that is excellent in fluidity during molding, has high mechanical strength, rigidity, and toughness and exhibits low shrinkage.

The present invention employs the following means as a result of intensive studies to solve the above problems.
(1) The ratio ((a) / (b)) of (A) amino end group concentration (a) [mol / g] to carboxyl end group concentration (b) [mol / g] is 0.3 to 0.8. (B) A polyamide resin molded product obtained by molding a polyamide resin composition comprising 10 to 235 parts by weight of glass fiber with respect to 100 parts by weight of the polyamide resin, A polyamide resin molded article having a weight average fiber length of glass fibers in the range of 300 to 800 μm.
(2) The polyamide resin molded article according to (1), wherein the polyamide resin is at least one selected from the group consisting of polycaproamide, polyhexamethylene adipamide, polyhexamethylene sebacamide, and copolymers thereof. .
(3) The polyamide resin molded product according to (1) or (2), which is a personal computer casing or a tablet casing.

  According to the present invention, a polyamide resin molded article having excellent fluidity during molding, high mechanical strength, rigidity, toughness, low shrinkage and reduced warpage can be obtained.

  The polyamide resin composition used for the polyamide resin molded product of the present invention (hereinafter sometimes referred to as “molded product”) has (A) amino end group concentration (a) [mol / g] and carboxyl end group concentration. (B) A polyamide resin having a [mol / g] ratio ((a) / (b)) of 0.3 to 0.8 (hereinafter sometimes referred to as “(A) polyamide resin”) is blended. Do it. (A) By mix | blending a polyamide resin, the mechanical strength, rigidity, and toughness of a molded article can be improved. Examples of the (A) polyamide resin include a ring-opening polymer of cyclic lactam, a polycondensate of aminocarboxylic acid, a polycondensate of dibasic acid and diamine, and the like. Specifically, polycaproamide (polyamide 6), polytetramethylene adipamide (polyamide 46), polypentamethylene adipamide (polyamide 56), polyhexamethylene adipamide (polyamide 66), polyhexamethylene Bacamide (polyamide 610), polyhexamethylene dodecane (polyamide 612), polyundecanamide (polyamide 11), polydodecanamide (polyamide 12), polycaproamide / polyhexamethylene adipamide copolymer (polyamide 6/66) , Polycaproamide / polyhexamethylene terephthalamide copolymer (polyamide 6 / 6T), polyhexamethylene adipamide / polyhexamethylene terephthalamide copolymer (polyamide 66 / 6T), polyhexamethylene adipamide / polyamide Hexamethylene isophthalamide copolymer (polyamide 66 / 6I), polyhexamethylene terephthalamide / polyhexamethylene isophthalamide copolymer (polyamide 6T / 6I), polyhexamethylene terephthalamide / polyhexamethylene sebacamide copolymer (polyamide 6T / 610) Polyhexamethylene terephthalamide / polydodecanamide copolymer (polyamide 6T / 12), polyhexamethylene adipamide / polyhexamethylene terephthalamide / polyhexamethylene isophthalamide copolymer (polyamide 66 / 6T / 6I), polyhexamethylene azide Pamide / polycaproamide / polyhexamethylene isophthalamide copolymer (polyamide 66/6 / 6I), polyxylene adipamide (polyamide X 6), polyhexamethylene terephthalamide / poly-2-methylpentamethylene terephthalamide copolymer (polyamide 6T / 5MT), polynonamethylene terephthalamide (polyamide 9T), polydecamethylene terephthalamide (polyamide 10T) and their co-polymers Examples include coalescence. Two or more of these may be used. Among these, a polyamide resin having a melting point of 300 ° C. or lower is preferable because the processing temperature can be appropriately lowered. Furthermore, since the mechanical strength, rigidity, and toughness can be improved in a balanced manner, polycaproamide (polyamide 6), polyhexamethylene adipamide (polyamide 66), and polyhexamethylene sebacamide (polyamide 610) can be obtained. More preferred.

  The (A) polyamide resin used in the present invention has a ratio ((a) / (b)) of the amino end group concentration (a) [mol / g] to the carboxyl end group concentration (b) [mol / g] of 0. .3 to 0.8. The end group of the polyamide resin may contribute to the reaction between the polyamide resins or the reaction with other components in the polyamide resin composition. In particular, the amino terminal group has a large polarity and high reactivity, and thus has a feature of large interaction with glass fiber. Therefore, in the present invention, in order to improve the mechanical strength by the interaction between the polyamide resin and the glass fiber and to easily adjust the weight average fiber length of the glass fiber in the molded product to a desired range, The amino terminal group concentration (a) [mol / g] and the carboxyl terminal group concentration (b) [mol / g] of the polyamide resin composition are used as indices that affect the adhesion to the glass fiber and the thickening of the polyamide resin composition. The ratio (a) / (b) was focused on. In addition, although each terminal group density | concentration of a polyamide resin may change with reaction etc. in a polyamide resin composition, in this invention, (a) / (b) as a raw material mix | blended with a polyamide resin composition Focused on. When (a) / (b) is less than 0.3, the adhesiveness between the polyamide resin and the glass fiber in the molded product becomes insufficient, so that the mechanical strength of the molded product decreases. Moreover, the shrinkage rate at the time of shaping | molding becomes large, and the curvature of a molded article becomes large. On the other hand, when (a) / (b) exceeds 0.8, the reactivity of the polyamide resin becomes excessively high, so the polyamide resin composition thickens when producing the polyamide resin composition, It becomes easy to break. For this reason, the fiber length of the glass fiber in a molded product also becomes short, and the mechanical strength of a molded product falls. Moreover, the shrinkage rate at the time of shaping | molding becomes large, and the curvature of a molded article becomes large.

  In the present invention, the amino terminal group concentration of the polyamide resin can be measured by the following method. First, 0.5 g of polyamide resin is precisely weighed and dissolved in 25 ml of a phenol / ethanol mixed solvent (volume ratio 83.5: 16.5). About the obtained solution, thymol blue is used as an indicator, and the concentration of amino end groups can be measured by neutralization titration using a 0.02N hydrochloric acid aqueous solution. The carboxyl end group concentration of the polyamide resin can be measured by the following method. First, 0.5 g of polyamide resin is precisely weighed and dissolved in 25 ml of benzyl alcohol solution. The resulting solution can be subjected to neutralization titration with potassium hydroxide using phenolphthalein as an indicator to measure the carboxyl end group concentration.

The polymerization method of the (A) polyamide resin used in the present invention is not particularly limited, and examples thereof include melt polymerization, interfacial polymerization, solution polymerization, bulk polymerization, solid phase polymerization, and a combination of these methods. Usually, melt polymerization is preferably used. For example, polyamide 610 resin can be polymerized by the following method. Hexamethylenediamine, sebacic acid equimolar salt, and monocarboxylic acid are added, and the same amount of pure water as that added is added, the inside of the polymerization vessel is replaced with nitrogen, and heating is started while stirring. Polyamide 610 can be obtained by reacting at a final ultimate temperature of 280 ° C. while adjusting the can internal pressure to a maximum of 20 kg / cm ² . In general, the obtained polymer is discharged into a water bath and pelletized with a strand cutter. As the amount of monocarboxylic acid increases, the amino end group is blocked and the amino end group concentration decreases. Moreover, not only the said polymerization method but the commercially available polyamide resin which has a desired terminal group density | concentration can be used, for example.

  The polyamide resin composition used in the present invention is formed by blending (B) glass fiber. (B) By mix | blending glass fiber, mechanical strength and rigidity improve and the molded article which shows low shrinkage can be obtained. (B) Examples of the cross-sectional shape of the glass fiber include an irregular cross-sectional shape such as a circular shape, an eyebrows shape, and a flat shape, and any of them may be used. (B) The glass fiber is preferably surface-treated using a known coupling agent (for example, a silane coupling agent, a titanate coupling agent, etc.) or other surface treatment agent. The affinity with the polyamide resin can be increased to improve the adhesion, and the mechanical strength can be further improved. The content of the coupling agent or the surface treatment agent is preferably 0.1 parts by weight or more with respect to 100 parts by weight of the (B) glass fiber, and the mechanical strength can be further improved. On the other hand, the content of the coupling agent or surface treatment agent is preferably 2 parts by weight or less, and gas generation during molding can be suppressed. Moreover, (B) glass fiber may be coat | covered or converged with thermosetting resins, such as an ethylene / vinyl acetate copolymer, and can improve workability | operativity when manufacturing a polyamide resin composition.

  In this invention, the compounding quantity of (B) glass fiber is 10-235 weight part with respect to 100 weight part of (A) polyamide resin. (B) When the compounding quantity of glass fiber is less than 10 weight part, mechanical strength will fall and shrinkability will increase. (B) As for the compounding quantity of glass fiber, 30 weight part or more is preferable. On the other hand, when the compounding quantity of (B) glass fiber exceeds 235 weight part, manufacture of a polyamide resin composition will become difficult. (B) As for the compounding quantity of glass fiber, 200 weight part or less is preferable.

  In the molded product of the present invention, it is important that the weight average fiber length of the glass fiber in the molded product is in the range of 300 to 800 μm. When the weight average fiber length of the glass fiber is less than 300 μm, the mechanical strength is lowered. Moreover, the shrinkage rate at the time of shaping | molding becomes large, and the curvature of a molded article becomes large. On the other hand, when the weight average fiber length of the glass fiber exceeds 800 μm, the fluidity at the time of molding is lowered, so that, for example, when a part having a thickness of 1 mm or less is molded, poor appearance or short shot occurs. The weight average fiber length of the glass fiber is preferably 500 μm or less.

In the present invention, the weight average fiber length of the glass fibers in the molded product can be measured by the following method. 10 g of a molded product containing polyamide resin and glass fiber is heated in air at 550 ° C. for 8 hours to remove the resin. The remaining glass fibers are observed using an optical microscope at a magnification of 120 times, and the fiber lengths of 1000 or more randomly selected glass fibers are measured. The weight average fiber length (Lw) can be calculated by the following equation, where (Ni) is the number of fibers having a circumference ratio (π), fiber length (Li), density (ρi), and fiber diameter (ri).
Lw = Σ (Ni × π × ri ² × Li ² × ρi) / Σ (Ni × π × ri ² × Li × ρi)
When the fiber diameter and density are constant, Lw can be calculated by the following equation.
Lw = Σ (Ni × Li ² ) / Σ (Ni × Li)

  The molded article of the present invention can be obtained by the following method. For example, (A) polyamide resin and other components as needed are supplied from the main feeder of a twin screw extruder, (B) glass fibers and other components are supplied as needed from the side feeder, and a resin composition is obtained by melt kneading. And a method of molding it. The screw element is preferably a combination of a reverse disk and a kneading disk between the main feeder and the side feeder, and it is preferable to melt the polyamide resin by applying high shear. It is preferable to join the glass fiber and knead in a low shear state. Then, the strand of a polyamide resin composition is obtained by extruding a molten polyamide resin and glass fiber from a die in a low shear state and water cooling. A molded article can be obtained by vacuum-drying and molding the obtained polyamide resin composition, for example, under conditions of 80 ° C. and 12 hours. Examples of the molding method include injection molding, injection compression molding, press molding, and extrusion molding. Among these, injection molding and injection compression molding are preferred from the viewpoint of shape flexibility and productivity. In particular, a continuously stable molded product can be obtained by a molding method using an injection molding machine. There are no particular restrictions on the injection molding conditions. For example, injection time: 0.5 to 15 seconds, back pressure: 0.1 to 15 MPa, holding pressure: 3 to 150 MPa, holding pressure: 1 to 30 seconds, cylinder temperature : 200-300 ° C, mold temperature: 25-100 ° C is preferable. Under these conditions, the fiber length of the glass fiber in the molded product can be adjusted by appropriately selecting the injection time, back pressure and mold temperature.

  Other components may be contained in the molded product as long as the effects of the present invention are not impaired. Other components include, for example, antioxidants and heat stabilizers (hindered phenols, hydroquinones, phosphites, and substituted products thereof), long-term heat stability (copper compounds, dipentaerythritol, etc.), long-term Heat stability aids (alkali halides such as potassium iodide and sodium iodide), weathering agents (resorcinol, salicylate, benzotriazole, benzophenone, hindered amine, etc.), mold release agents and lubricants (montanic acid) And its metal salt, its ester, its half ester, stearyl alcohol, stearamide, various bisamides, bisurea, polyethylene wax, dipentaerythritol, etc.), pigment (cadmium sulfide, phthalocyanine, carbon black, etc.), dye (nigrosine, etc.), Crystal nucleating agent (tal , Silica, kaolin, clay, etc.), plasticizers (octyl p-oxybenzoate, N-butylbenzenesulfonamide, etc.), antistatic agents (alkyl sulfate type anionic antistatic agents, polyoxyethylene sorbitan monostearate, etc. Nonionic antistatic agents, betaine amphoteric antistatic agents, etc.). Other polymers may be contained, and examples of the polymer include polyethylene, polypropylene, ABS resin, and PPS resin. It may also contain an ethylene / propylene copolymer, ethylene / butene copolymer, ethylene / octene copolymer, ethylene / glycidyl methacrylate copolymer, styrene / ethylene / butadiene / styrene copolymer elastomer, ionomer, etc. Good.

  You may contain a flame retardant in a molded article in the range which does not impair the effect of this invention. Examples of the flame retardant include halogen flame retardants such as bromine compounds and bromine-containing polymers, non-halogen flame retardants such as phosphinic acid metal salts, triazines, and red phosphorus. Two or more of these may be used. Examples of the halogen-based flame retardant include aromatic bromine substituted products and aliphatic bromine substituted products. Specifically, bromine compounds of diphenyl ether such as tetrabromodiphenyl ether, octabromodiphenyl ether, decabromodiphenyl ether, bromide of triphenylene oxide, tetrabromobisphenol A, tribromophenol, tris (tribromophenyl) phosphite, hexabromo Cyclododecane, tetrabromocyclooctane, imide condensate of tetrabromophthalic anhydride and diamine, pentabromotoluene, hexabromobenzene, tris (tribromophenoxy) cyanurate, 1,2-bis (pentabromophenoxy) ethane, etc. Bromobisphenol A, diglycidyl ether polymers and tribromophenol adducts, tetrabromobisphenol A polycarbonate, brominated poly Styrene, and a bromine-containing polymers such as brominated polyphenylene ether.

  Specific examples of phosphinic acid metal salts include calcium dimethylphosphinate, aluminum dimethylphosphinate, calcium ethylmethylphosphinate, aluminum ethylmethylphosphinate, calcium diethylphosphinate, aluminum diethylphosphinate, and methyl-n-propylphosphine. Acid calcium, methyl-n-propylphosphinic acid aluminum, methanebis (methylphosphinic acid) calcium, methanebis (methylphosphinic acid) aluminum, benzene-1,4-bis (methylphosphinic acid) calcium, benzene-1,4-bis ( Methyl phosphinic acid) aluminum, calcium methylphenylphosphinate, aluminum methylphenylphosphinate, calcium diphenylphosphinate, diphenylphosphine Like fin aluminum and the like.

  Examples of triazines include melamine cyanurate, melam, melem double salt, melamine phosphate (melamine polyphosphate, melamine polyphosphate, melam, melem double salt, etc.), melamine sulfate (melamine sulfate, dimelamine sulfate, pyrosulfate). Melamine, etc.), melamine sulfonates (melamine methanesulfonate, melam methanesulfonate, melem methanesulfonate, melamine methanesulfonate, melam, melem double salt, melamine toluenesulfonate, melam toluenesulfonate, melamine toluenesulfonate, Melam, melem double salt, etc.).

  The molded product of the present invention has excellent fluidity during molding, high mechanical strength, rigidity, toughness, low shrinkage, and reduced warpage. It can be suitably used for applications in the shape of a thin frame.

  Evaluation of each characteristic in Examples and Comparative Examples was performed by the following methods.

(1) Amino end group concentration 0.5 g of polyamide resin was precisely weighed and dissolved in 25 ml of a phenol / ethanol mixed solvent (volume ratio 83.5: 16.5), and then thymol blue was used as an indicator, and 0.02N hydrochloric acid. Neutralization titration was performed using an aqueous solution.

(2) Carboxyl end group concentration 0.5 g of polyamide resin was precisely weighed and dissolved in 25 ml of benzyl alcohol solution, and then neutralized with potassium hydroxide using phenolphthalein as an indicator.

(3) Weight average fiber length of glass fiber Using a NEX1000 injection molding machine manufactured by Nissei Plastic Industry Co., Ltd., injection time is 10 seconds, cooling time is 10 seconds, back pressure is 2 MPa, holding pressure is 50 MPa, holding pressure time. 5 seconds, the injection pressure is set to an injection pressure 10% higher than the lowest injection pressure that can be filled up to the final filling part, and a film gate is arranged on the upper end, and the length is 80 mm, the width is 80 mm, and the thickness is 1 mm. A square plate-like test piece was obtained by injection-molding the pellets obtained in each Example / Comparative Example using a mold under the conditions of a cylinder temperature of 280 ° C. and a mold temperature of 80 ° C. 10 g of the central part of the square plate was heated in air at 550 ° C. for 8 hours to remove the resin. The remaining glass fiber was observed at 120 times magnification using an optical microscope, and the fiber length of 1000 or more randomly selected glass fibers was measured. In the range of Examples and Comparative Examples, since the fiber diameter and density are constant, the weight average fiber length (Lw) is the number of fibers having the fiber length (Li) and the fiber diameter (ri) (Ni). And calculated by the following formula.
Lw = Σ (Ni × Li ² ) / Σ (Ni × Li).

(4) Mechanical strength / test specimen: A multi-purpose specimen having a thickness of 4 mm was molded from the pellets obtained in each of the examples and comparative examples in accordance with ISO294-1.
Test conditions: Based on ISO 527, tensile strength was measured under the conditions of a tensile speed of 50 mm / min and a distance between gauge points of 115 mm.
Test atmosphere: Air temperature was 23 ° C. and humidity was 50% RH.

(5) Rigidity / test specimen: A multi-purpose specimen having a thickness of 4 mm was molded from the pellets obtained in each of the examples and comparative examples in accordance with ISO294-1.
Test conditions: Based on ISO 178, the flexural modulus was measured under the conditions of a yield rate of 2 mm / min and a span distance of 64 mm.
Test atmosphere: Air temperature was 23 ° C. and humidity was 50% RH.

(6) Toughness / test piece: A multi-purpose test piece having a thickness of 4 mm was molded from the pellets obtained in each of the examples and comparative examples in accordance with ISO294-1. An 80 mm × 10 mm × 4 mm test piece was cut from the central portion of the multi-purpose test piece, and the obtained test piece was notched according to JISK7144 to obtain an impact test piece.
Test condition: Charpy impact strength was measured according to ISO179.
Test atmosphere: Air temperature was 23 ° C. and humidity was 50% RH.

(7) Mold Shrinkage Ratio The square plate-shaped test piece of (3) above was used as a mold shrinkage ratio test piece. With the gate of the molding shrinkage rate test piece as the upper end, the length of the inner portion of 1 mm from the left end, the length of the inner portion of 40 mm from the left end, and the length of the inner portion of 1 mm from the right end were measured. For each of the measured values of the three points, the molding shrinkage from the mold dimensions was calculated by the following formula, and the average value of the three points was obtained. Measurement was performed on five test specimens for molding shrinkage, and the average value was taken as the mold shrinkage.
Mold Shrinkage [%] = <{(Mold Size-Mold Shrinkage Test Piece Size) / Mold Size}> × 100.

(8) Surface appearance of molded product The surface of the molding shrinkage test piece of (7) above was visually evaluated. Those in which glass fiber float was observed were judged as poor, and those in which glass fiber float was not found were judged good.

(9) Fluidity Using a NEX1000 injection molding machine manufactured by Nissei Plastic Industry Co., Ltd., setting the cylinder temperature to 280 ° C., the injection pressure to 60 MPa, and the mold temperature of 80 ° C., each example and comparative example From the pellets obtained by the above, a rod flow test piece having a width of 10 mm × 1.0 mm was injection molded, and the rod flow length at a holding pressure of 0 was measured.

(10) Polyamide resin viscosity number Measured according to ISO307 using a solution of polyamide resin in 96% sulfuric acid.

<Polyamide resin>
(A1) Polyamide 610 resin: melting point 225 ° C., viscosity number 110 ml / g, amino end group concentration (a): 3.32 [10 ⁻⁵ mol / g], carboxyl end group concentration (b): 5.22 [10 ⁻⁵ mol / g], (a) / (b) = 0.64
(A2) Polyamide 610 resin: melting point 225 ° C., viscosity number 130 ml / g, amino end group concentration (a): 3.17 [10 ⁻⁵ mol / g], carboxyl end group concentration (b): 7.43 [10 ⁻⁵ mol / g], (a) / (b) = 0.43
(A3) Polyamide 610 resin: melting point 225 ° C., viscosity number 110 ml / g, amino end group concentration (a): 2.28 [10 ⁻⁵ mol / g], carboxyl end group concentration (b): 12.81 [10 ⁻⁵ mol / g], (a) / (b) = 0.18
(A4) Polyamide 610 resin: melting point 225 ° C., viscosity number 130 ml / g, amino end group concentration (a): 6.16 [10 ⁻⁵ mol / g], carboxyl end group concentration (b): 5.60 [10 ⁻⁵ mol / g], (a) / (b) = 1.10
(A5) Polyamide 66 resin: melting point 265 ° C., viscosity number 120 ml / g, amino end group concentration (a): 2.73 [10 ⁻⁵ mol / g], carboxyl end group concentration (b): 8.44 [10 ⁻⁵ mol / g], (a) / (b) = 0.32.
(A6) Polyamide 6 resin: melting point 225 ° C., viscosity number 110 ml / g, amino end group concentration (a): 4.84 [10 ⁻⁵ mol / g], carboxyl end group concentration (b): 7.34 [10 ⁻⁵ mol / g], (a) / (b) = 0.66.

<Glass fiber>
(B1) Glass fiber: Chopped strand shape manufactured by Nippon Electric Glass Co., Ltd. T275H (cross-sectional diameter 10.5 μm, fiber length 3 mm, surface-treated silane coupling agent)
(B2) Glass fiber: Roving shape (cross-sectional diameter 13.0 μm, surface-treated silane coupling agent).

Examples 1, 2, 5, 6 and Comparative Examples 1 and 2
(A) Polyamide resin is supplied from the main feeder with the composition shown in Table 1 using a twin screw extruder TEX44αII manufactured by Nippon Steel, Ltd., and (B) glass fiber is supplied from the side feeder. The mixture was melt-kneaded and pelletized at 280 ° C. and a discharge rate of 200 kg / h. In addition, the screw arrangement of the twin screw extruder was an arrangement in which a reverse disk and a kneading disk were combined between the main feeder and the side feeder, and no reverse disk and kneading disk were used between the side feeder and the die head ( Screw arrangement A). The obtained resin composition pellets were vacuum dried at 80 ° C. for 12 hours. Using the dried pellets, each test piece was molded under the conditions of a cylinder temperature of 280 ° C. and a mold temperature of 80 ° C. using a NEX1000 injection molding machine manufactured by Nissei Plastic Industry Co., Ltd., and evaluated by the method described above.

Example 3
Except that the resin melting temperature was 295 ° C., resin composition pellets were obtained in the same manner as in Example 1, and each test piece was molded and evaluated.

Example 4
Except that the discharge rate was 170 kg / h, resin composition pellets were obtained in the same manner as in Example 3, and each test piece was molded and evaluated.

Comparative Example 3
The screw arrangement of the twin screw extruder is the same as that of Example 1 except that the reverse disk and the kneading disk are combined (screw arrangement B) between the main feeder and the side feeder and between the side feeder and the die head. A resin composition pellet was obtained, and each test piece was molded and evaluated.

Comparative Example 4
Using a single screw extruder, (A) polyamide resin is supplied from the main feeder with the composition shown in Table 1, and glass fiber roving (B2) is guided to an impregnation die filled with molten polyamide resin. The outside was coated. The strand discharged from the tip of the die was cooled and solidified and pelletized to a length of 10 mm to obtain a resin composition pellet. Using the obtained pellets, each test piece was molded in the same manner as in Example 1 and evaluated.

  Table 1 shows the composition, production conditions, and evaluation results of each Example and Comparative Example.

Claims (3)

(A) Polyamide having a ratio ((a) / (b)) of amino end group concentration (a) [mol / g] to carboxyl end group concentration (b) [mol / g] of 0.3 to 0.8 A polyamide resin molded product obtained by molding a polyamide resin composition obtained by blending 10 to 235 parts by weight of (B) glass fiber with respect to 100 parts by weight of resin, the glass fiber in the polyamide resin molded product A polyamide resin molded product having a weight average fiber length in the range of 300 to 800 μm. 2. The polyamide resin molded article according to claim 1, wherein the polyamide resin (A) is at least one selected from the group consisting of polycaproamide, polyhexamethylene adipamide, polyhexamethylene sebacamide, and copolymers thereof. . The polyamide resin molded product according to claim 1, which is a personal computer casing or a tablet casing.