METHOD AND DEVICE OF MANUFACTURING FIBER-REINFORCED RESIN MATERIAL
20170266846 · 2017-09-21
Assignee
Inventors
Cpc classification
B29C48/402
PERFORMING OPERATIONS; TRANSPORTING
B29B7/60
PERFORMING OPERATIONS; TRANSPORTING
B29B7/488
PERFORMING OPERATIONS; TRANSPORTING
B29C48/40
PERFORMING OPERATIONS; TRANSPORTING
B29C48/385
PERFORMING OPERATIONS; TRANSPORTING
B29B15/105
PERFORMING OPERATIONS; TRANSPORTING
B29B7/483
PERFORMING OPERATIONS; TRANSPORTING
B29B7/845
PERFORMING OPERATIONS; TRANSPORTING
B29B7/487
PERFORMING OPERATIONS; TRANSPORTING
International classification
B29B7/90
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method of manufacturing a fiber-reinforced resin material, includes preparing a kneaded material by melting a thermoplastic resin and kneading the molten thermoplastic resin with reinforcing fibers; preparing a reinforcing fiber-impregnated material including a supercritical fluid by accommodating the kneaded material in a sealed space and supplying the supercritical fluid into the sealed space such that the molten thermoplastic resin is impregnated into the reinforcing fibers included in the kneaded material; and manufacturing the fiber-reinforced resin material by extracting the reinforcing fiber-impregnated material from the sealed space and leaving the reinforcing fiber-impregnated material to stand in a reduced-pressure atmosphere such that the supercritical fluid foams.
Claims
1. A method of manufacturing a fiber-reinforced resin material, the method comprising: preparing a kneaded material by melting a thermoplastic resin and kneading the molten thermoplastic resin with reinforcing fibers; preparing a reinforcing fiber-impregnated material including a supercritical fluid by accommodating the kneaded material in a sealed space and supplying the supercritical fluid into the sealed space such that the molten thermoplastic resin is impregnated into the reinforcing fibers included in the kneaded material; and manufacturing the fiber-reinforced resin material by extracting the reinforcing fiber-impregnated material from the sealed space and leaving the reinforcing fiber-impregnated material to stand in a reduced-pressure atmosphere such that the supercritical fluid foams.
2. The method according to claim 1, wherein when the fiber-reinforced resin material is manufactured, the fiber-reinforced resin material is manufactured by cutting the reinforcing fibers while the supercritical fluid foams.
3. A device of manufacturing a fiber-reinforced resin material, the device comprising: a melting portion configured to melt a thermoplastic resin; a kneading portion configured to supply reinforcing fibers to molten thermoplastic resin and to knead the reinforcing fibers and the molten thermoplastic resin with each other; a supercritical fluid supplying portion having a sealed space where a supercritical fluid is supplied to a kneaded material including the thermoplastic resin and the reinforcing fibers; and a pressure-reduced portion configured to leave a reinforcing fiber-impregnated material including the kneaded material and the supercritical fluid to stand in a reduced-pressure atmosphere.
4. The device according to claim 3, wherein the pressure-reduced portion includes a cutter.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0037] Features, advantages, and technical and industrial significance of exemplary embodiments of the disclosure will be described below with reference to the accompanying drawings, in which like numerals denote like elements, and wherein:
[0038]
[0039]
[0040]
[0041]
[0042]
[0043]
[0044]
DETAILED DESCRIPTION OF EMBODIMENTS
[0045] Hereinafter, methods and devices of manufacturing a fiber-reinforced resin material according to first and second embodiments of the disclosure will be described with reference to the drawings.
[0046] (First Embodiment of Method and Device of Manufacturing Fiber-Reinforced Resin Material)
[0047]
[0048] First, the first embodiment of the method of manufacturing a fiber-reinforced resin material will be described with reference to the flowchart shown in
[0049] In the method of manufacturing a fiber-reinforced resin material, first, a kneaded material is prepared by melting a thermoplastic resin and kneading the molten thermoplastic resin with reinforcing fibers (first step S1).
[0050] Here, examples of the thermoplastic resin include: crystalline plastics which have a high area ratio of a crystalline region in which molecular chains are arranged in order and have a high crystallinity degree, for example, polyethylene (PE), polypropylene (PP), nylon (for example, PA: nylon 6 or nylon 66), polyacetal (POM), or polyethylene terephthalate (PET); and amorphous plastics which has an extremely low crystallinity degree or is not crystalline, for example, polystyrene (PS), polyphenylene sulfide (PPS), polyvinyl chloride (PVC), polymethyl methacrylate (PMMA), an ABS resin, or a thermoplastic epoxy. Among these thermoplastic resins, one kind is used.
[0051] On the other hand, examples of the reinforcing fibers to be mixed with the molten thermoplastic resin include: ceramic fibers such as boron, alumina, silicon carbide, silicon nitride, or zirconia; inorganic fibers such as glass fibers or carbon fibers; metal fibers such as copper, steel, aluminum, or stainless steel; and organic fibers such as polyamide or polyester. Among these reinforcing fibers, one kind may be used alone, or a mixed material of two or more kinds may be used.
[0052] After the kneaded material is prepared by kneading the molten thermoplastic resin and the reinforcing fibers with each other in the first step, a reinforcing fiber-impregnated material including a supercritical fluid is prepared by accommodating the kneaded material in a sealed space and supplying the supercritical fluid into the sealed space such that the molten thermoplastic resin is impregnated into the reinforcing fibers included in the kneaded material (second step S2).
[0053] The supercritical fluid refers to a fluid having diffusibility which is a gas property and meltability which is a liquid property. As the supercritical fluid, nitrogen (critical temperature Tc=−147° C., critical pressure Pc=3.4 MPa) or carbon dioxide (critical temperature Tc=about 31° C., critical pressure Pc=about 7.4 MPa) is used. The supercritical fluid is prepared using a general a supercritical fluid generator and then is supplied into the sealed space.
[0054] The sealed space into which the supercritical fluid is supplied is maintained at a high pressure in order to maintain the supercritical state of the supercritical fluid.
[0055] After the reinforcing fiber-impregnated material including the supercritical fluid is prepared in the second step, a fiber-reinforced resin material is manufactured by extracting the reinforcing fiber-impregnated material from the sealed space and leaving the reinforcing fiber-impregnated material to stand in a reduced-pressure atmosphere such that the supercritical fluid foams (third step S3).
[0056] By extracting the reinforcing fiber-impregnated material including the supercritical fluid from the sealed space and leaving the reinforcing fiber-impregnated material to stand in a reduced-pressure atmosphere (for example, in an atmospheric pressure atmosphere), the supercritical fluid foams, and the reinforcing fibers are disintegrated from a bundle and can be dispersed in the thermoplastic resin.
[0057] According to the manufacturing method shown in
[0058] Next, the first embodiment of the device of manufacturing a fiber-reinforced resin material will be described with reference to
[0059] Briefly, the device 10 shown in
[0060] The melting portion 1 is formed of a twin screw extruder including two full flight screws 1a that are rotatably provided (
[0061] The kneading portion 2 is formed of another twin screw extruder. In the kneading portion 2, the reinforcing fibers F in the form of a bundle T are supplied to the molten thermoplastic resin R which is supplied from the melting portion 1, and a kneaded material including the thermoplastic resin R and the reinforcing fibers F is prepared while being rotated by full flight screws 2a.
[0062] A plurality of seal rings 2b are provided at intermediate positions of each of the full flight screws 2a of the twin screw extruder forming the kneading portion 2, and the sealed space 3 is formed by the respective seal rings 2b of the full flight screws 2a. The kneaded material is supplied to the sealed space 3 (X2 direction), and the supercritical fluid is supplied to the kneaded material in the sealed space 3.
[0063] As shown in
[0064] As a sealing mechanism of the sealed space 3, an appropriate mechanism which stops the flows of the materials in the twin screw extruder to increase the internal pressure (material filling rate) of the sealed space is applied, and examples thereof include the seal ring 2b, a reverse kneading disk screw, a reverse full flight screw, and a gate valve.
[0065] The pressure-reduced portion 4 is provided downstream of the sealed space 3, and the reinforcing fiber-impregnated material including the kneaded material and the supercritical fluid is supplied to the pressure-reduced portion 4 (X3 direction). In the pressure-reduced portion 4, the reinforcing fiber-impregnated material is left to stand in a reduced-pressure atmosphere such that the supercritical fluid foams. As a result, the fiber-reinforced resin material is manufactured and transported from the device 10 (X4 direction).
[0066] The pressure-reduced portion 4 is a region which is provided outside the high-pressure sealed space 3 and where the high-pressure state is naturally converted into a reduced-pressure state.
[0067] According to the device 10, intermediate materials were caused to pass through the respective components in order. As a result, the steps from the thermoplastic resin melting step to the fiber-reinforced resin material manufacturing step can be performed continuously and efficiently, and a fiber-reinforced resin material having excellent mechanical properties can be manufactured.
[0068] (Second Embodiment of Method and Device of Manufacturing Fiber-Reinforced Resin Material)
[0069]
[0070] The second embodiment of the method is different from the first embodiment of the method, in that a fiber-reinforced resin material is manufactured by cutting the reinforcing fibers in a third step S3′.
[0071] That is, in the third step S3′, the fiber-reinforced resin material is manufactured by cutting the reinforcing fibers by mechanical cutting or the like while the supercritical fluid foams.
[0072] More specifically, by cutting the reinforcing fibers using a cutter such as a kneading screw having a high shearing force, the shearing force is applied in a state where the thermoplastic resin is sufficiently impregnated into the reinforcing fibers. The shearing force transmitted from the thermoplastic resin to the reinforcing fibers is as uniform as possible in the entire region, and a variation in the fiber diameter of the reinforcing fibers can be reduced or eliminated.
[0073] A device 10A of manufacturing a fiber-reinforced resin material shown in
[0074] Examples of a method of cutting the reinforcing fibers include a mechanical cutting method using a kneading screw, a cutting method of adding an acid to the reinforcing fibers to damage the reinforcing fibers, and a cutting method of transmitting a rotating force of a screw to the reinforcing fibers through the resin.
[0075] According to the device 10A, the reinforcing fibers whose fiber diameter is maintained are uniformly dispersed in the thermoplastic resin, and a fiber-reinforced resin material having excellent mechanical properties can be manufactured continuously and efficiently.
[0076] (Experiment for Verifying Mechanical Properties of Fiber-Reinforced Resin Material, and Result thereof)
[0077] The present inventors prepared fiber-reinforced resin materials according to Example and Comparative Example and performed an experiment for verifying mechanical properties thereof.
[0078] In Example and Comparative Example, the fiber-reinforced resin material was prepared using a thermoplastic resin (PA6, AMILAN CM1017, manufactured by Toray Industries Inc.) and carbon fibers (PAN-based, T700 12K, manufactured by Toray Industries Inc.) having a content of 30 vol %. 60 wt % (with respect to the weight of fiber-reinforced resin material) of PA6 as the thermoplastic resin was supplied to the melting portion of the twin screw extruder, and the temperature of the melting portion was set such that the resin temperature of PA6 supplied to the kneading portion was 260° C. Next, 40 wt % (with respect to the weight of fiber-reinforced resin material) of the carbon fibers were supplied to an open vent port of the kneading portion, and a kneaded material including PA6 and the carbon fibers was prepared. The screw rotating speed of the twin screw extruder, which formed not only the kneading portion but also the sealed space and the pressure-reduced portion, was 100 rpm. The temperature of each component of the twin screw extruder was set such that the temperature of the fiber-reinforced resin material in the kneading portion, the sealed space, and the pressure-reduced portion was 260° C. Carbon dioxide in the supercritical state was supplied from the supercritical fluid injection portion to the sealed space in an addition amount of 5 wt % and was kneaded with the fiber-reinforced resin material. The fiber-reinforced resin material extruded from the device through the pressure-reduced portion was supplied onto a flat tool for press forming having a size of 400 mm×400 mm and was press-formed into a flat plate. In Example, the supercritical fluid was supplied to the kneaded material during the manufacturing process. However, in Comparative Example, the supercritical fluid was not supplied to the kneaded material during the manufacturing process.
[0079]
TABLE-US-00001 TABLE 1 Bending Bending Elastic Strength Modulus (MPa) (GPa) Comparative Example 273 16 Example 295 17
[0080] It was found from
[0081] It was verified from Table 1 that the bending strength of Example was improved by about 8% as compared to Comparative Example.
[0082] Hereinabove, the embodiments of the disclosure have been described with reference to the drawings, but specific configurations thereof are not particularly limited to the above-described embodiments. Within a range not departing from the scope of the disclosure, design changes and the like can be made and are embraced in the disclosure.