WO2017154342A1 - スプルブッシュ - Google Patents
スプルブッシュ Download PDFInfo
- Publication number
- WO2017154342A1 WO2017154342A1 PCT/JP2017/000869 JP2017000869W WO2017154342A1 WO 2017154342 A1 WO2017154342 A1 WO 2017154342A1 JP 2017000869 W JP2017000869 W JP 2017000869W WO 2017154342 A1 WO2017154342 A1 WO 2017154342A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- flow path
- raw material
- material resin
- sprue bush
- cooling medium
- Prior art date
Links
- 229920005989 resin Polymers 0.000 claims abstract description 120
- 239000011347 resin Substances 0.000 claims abstract description 120
- 239000002994 raw material Substances 0.000 claims abstract description 109
- 239000002826 coolant Substances 0.000 claims abstract description 67
- 239000000843 powder Substances 0.000 claims description 59
- 238000011144 upstream manufacturing Methods 0.000 claims description 40
- 239000011148 porous material Substances 0.000 claims description 18
- 239000010410 layer Substances 0.000 description 30
- 238000001816 cooling Methods 0.000 description 28
- 238000000034 method Methods 0.000 description 21
- 238000003475 lamination Methods 0.000 description 13
- 238000005245 sintering Methods 0.000 description 13
- 239000002184 metal Substances 0.000 description 11
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000011247 coating layer Substances 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 8
- 238000000465 moulding Methods 0.000 description 7
- 238000002347 injection Methods 0.000 description 6
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000001746 injection moulding Methods 0.000 description 4
- 230000001678 irradiating effect Effects 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000007769 metal material Substances 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
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- 238000007789 sealing Methods 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/2701—Details not specific to hot or cold runner channels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F5/00—Manufacture of workpieces or articles from metallic powder characterised by the special shape of the product
- B22F5/007—Manufacture of workpieces or articles from metallic powder characterised by the special shape of the product of moulds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/2737—Heating or cooling means therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y80/00—Products made by additive manufacturing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F10/00—Additive manufacturing of workpieces or articles from metallic powder
- B22F10/20—Direct sintering or melting
- B22F10/28—Powder bed fusion, e.g. selective laser melting [SLM] or electron beam melting [EBM]
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/10—Sintering only
- B22F3/105—Sintering only by using electric current other than for infrared radiant energy, laser radiation or plasma ; by ultrasonic bonding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/12—Both compacting and sintering
- B22F3/16—Both compacting and sintering in successive or repeated steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/2725—Manifolds
- B29C2045/2733—Inserts, plugs, bushings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C2045/2766—Heat insulation between nozzle and mould
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C64/00—Additive manufacturing, i.e. manufacturing of three-dimensional [3D] objects by additive deposition, additive agglomeration or additive layering, e.g. by 3D printing, stereolithography or selective laser sintering
- B29C64/10—Processes of additive manufacturing
- B29C64/141—Processes of additive manufacturing using only solid materials
- B29C64/153—Processes of additive manufacturing using only solid materials using layers of powder being selectively joined, e.g. by selective laser sintering or melting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B33—ADDITIVE MANUFACTURING TECHNOLOGY
- B33Y—ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3-D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3-D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- B33Y10/00—Processes of additive manufacturing
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Definitions
- the present invention relates to a sprue bush. More specifically, the present invention relates to a sprue bush used for a mold.
- the injection molding method is a method for obtaining a molded product from a molten raw material resin using an injection molding die.
- a mold cavity 203 ′ composed of one mold (core mold) 201 ′ of the injection mold 200 ′ and the other mold (cavity mold) 202 ′.
- the molten raw material resin is injected into (see FIG. 9A).
- the injected molten raw resin is subjected to cooling and solidification in the mold cavity 203 'to form a molded product.
- Injection of molten raw material resin into the mold cavity 203 ' is generally performed via the sprue bush 100'.
- a raw resin flow path 10 ' is provided in the sprue bush 100' used in the injection mold 200 '.
- the raw material resin flow path 10 ′ extends from one end portion 10 a ′ into which the molten raw material resin is introduced to the other end portion 10 b ′ leading to the mold cavity 203 ′.
- the raw material resin flow path 10 ′ is tapered to facilitate removal of the molded product. Specifically, the width dimension W ′ of the raw material resin flow path 10 ′ gradually increases as it extends from the one end 10a ′ to the other end 10b ′. As shown in FIG. 9A, the width W 1 ′ on the upstream side 10A ′ of the raw material resin flow path 10 ′ is relatively small, whereas the width on the downstream side 10B ′ of the raw material resin flow path 10 ′. The dimension W 2 ′ is relatively large.
- the tapered raw material resin flow path 10 ' is preferable from the viewpoint of taking out a molded product, but is not necessarily preferable from the viewpoint of cooling and solidifying the molten raw material resin.
- the tapered raw material resin flow path 10 ' becomes longer, the influence on the downstream side of the relatively large width dimension W' increases accordingly, and the molten raw material resin becomes difficult to cool and solidify.
- the time required from the injection of the molten raw material resin to the removal of the molded product increases, resulting in a longer molding cycle. Therefore, as shown in FIG. 9B, a cooling medium flow path 20 'may be provided around the raw resin flow path 10'.
- the cooling medium When the cooling medium is caused to flow through the cooling medium flow path 20 ′, the cooling heat of the cooling medium is transmitted to the molten raw material resin in the raw material resin flow path 10 ′ due to the sprue bush 100 ′ being made of a metal member.
- the molten raw material resin in the raw material resin flow path 10 ′ tends to be cooled and solidified more easily on the upstream side 10A ′ than on the downstream side 10B ′ due to the relatively small width dimension of the upstream side 10A ′. Have.
- the raw material resin flow path 10 ' may be substantially blocked.
- the molten raw material resin cannot be suitably injected through the raw material resin flow path 10 ', and a predetermined amount of the molten raw material resin cannot be filled into the mold cavity 203'. Therefore, it becomes impossible to finally obtain a molded product having a desired shape.
- an object of the present invention is to provide a sprue bush that can more suitably cool the molten raw material resin in the raw material resin flow path.
- a sprue bush having a raw material resin flow path and a cooling medium flow path provided around the raw material resin flow path, A sprue bush is provided in which a low heat transfer portion is provided in a local region between the upstream portion of the raw material resin flow channel and the cooling medium flow channel, which is relatively smaller in heat transfer than a region other than the local region.
- the molten raw material resin in the raw material resin flow path can be more suitably cooled.
- Sectional drawing which showed typically the sprue bush which concerns on one Embodiment of this invention
- Sectional view schematically showing a sprue bush having a hollow portion in a vacuum state Sectional drawing which showed typically the sprue bush which has a hollow part used as a heat carrier flow path
- Sectional drawing which showed typically the sprue bush which has a hollow part in which the powder body was provided
- Sectional drawing which showed typically the sprue bush which has a cooling-medium flow path provided with the coating layer Sectional drawing
- FIG. c) During lamination Sectional drawing schematically showing a conventional sprue bush (FIG. 9A: no cooling medium flow path, FIG. 9B:
- the sprue bush 100 is a metal member composed of a flange portion 101 and a base portion 102 integrated with the flange portion 101, as shown in FIG. As shown in the figure, the sprue bush 100 includes a raw material resin flow channel 10 and a cooling medium flow channel 20 provided around the raw material resin flow channel 10.
- the raw resin flow path 10 of the sprue bush 100 extends from one end 10a where the molten raw resin is introduced to the other end 10b which communicates with the mold cavity. Based on the flow of the molten raw material resin at the time of molding, the one end portion 10a corresponds to the “upstream side” end portion, and the other end portion 10b corresponds to the “downstream side” end portion.
- the raw material resin flow path 10 is tapered. More specifically, the raw material resin flow path 10 is configured such that the width dimension W gradually increases as it extends from the one end 10a to the other end 10b. In other words, the width W 1 of the upstream side 10A of the starting resin channel 10 whereas relatively small, the width W 2 of the downstream side 10B of the starting resin channel 10 is relatively large.
- the cooling medium flow path 20 of the sprue bush 100 is a flow path for flowing the cooling medium, and is a flow path contributing to cooling of the molten raw material resin in the raw material resin flow path 10. That is, at the time of molding, the molten raw material resin in the raw material resin flow channel 10 is subjected to a temperature drop due to the cooling medium flowing through the cooling medium flow channel 20.
- the “cooling medium” here refers to a fluid that can give a cooling effect to the molten raw material resin in the raw material resin flow path 10, and is, for example, cooling water or a cooling gas.
- the “upstream side of the raw material resin flow path” refers to a portion located on the proximal side with respect to the one end portion 10a into which the molten raw material resin is introduced.
- the “downstream side of the raw material resin flow path” in this specification refers to a portion located on the distal side with respect to the one end portion 10a into which the molten raw material resin is introduced.
- the boundary between the upstream side and the downstream side of the raw material resin flow path is not particularly limited, but is, for example, “a half-division point of the entire longitudinal dimension of the raw material resin flow path”.
- the “upstream side of the raw material resin flow path” is, for example, a region extending from one end portion 10a of the raw material resin flow path 10 to the “half-division point of the entire longitudinal dimension of the raw material resin flow path 10”. Equivalent to.
- the “downstream side of the raw material resin flow path” corresponds to, for example, a region extending from the “half-division point of the entire longitudinal dimension of the raw material resin flow path 10” to the other end portion 10 b of the raw material resin flow path 10.
- the local region 100A between the upstream side 10A of the raw material resin flow channel 10 and the cooling medium flow channel 20 is more relative to the region 100B than the local region 100A. Therefore, a low heat transfer portion 30 with a small heat transfer is provided. That is, the low heat transfer portion 30 of the sprue bushing of the present invention has a local or limited form between the raw material resin flow path 10 and the cooling medium flow path 20.
- the “low heat transfer portion” is a portion of the sprue bush that reduces or inhibits the phenomenon in which the cooling heat caused by the cooling medium in the cooling medium flow path 20 is transmitted to the molten raw resin in the raw resin flow path 10. Is actually referring to.
- the cooling heat due to the cooling medium in the cooling medium flow path 20 is reduced. It becomes difficult to transmit to the upstream side 10A.
- the difficulty in transmitting the cooling heat to the upstream side 10A means that the cooling of the molten raw material resin on the upstream side 10A is more suitably suppressed. Therefore, the phenomenon that the molten raw material resin is cooled and solidified on the upstream side 10A prior to the downstream side 10B is less likely to occur, and blockage of the raw material resin flow path 10 can be prevented.
- the molten raw material resin can be more suitably injected through the raw material resin flow path 10. Therefore, in the sprue bush 100 of the present invention, a predetermined amount of molten raw material resin can be filled in the mold cavity, and a molded product having a desired shape can be finally obtained.
- the sprue bush 100 according to an embodiment of the present invention can be manufactured by using a “powder sintering lamination method” described later.
- the present invention is not limited to this, and only a part of the sprue bush 100 can be formed by a powder sintering lamination method, and the remaining part can be manufactured by cutting a metal structure prepared in advance.
- Examples of the “part of the sprue bush” include the base 102 (or a part thereof) of the sprue bush (see FIG. 1).
- Examples of the “remaining portion of the sprue bush” include a flange portion 101 of the sprue bush (or a portion obtained by adding a part of the base portion 102 thereto) (see FIG. 1).
- the “powder sintering lamination method” used for the production of a sprue bush is a method capable of producing a three-dimensional shaped object by irradiating a powder material with a light beam.
- a powder layer formation and a solidified layer formation are alternately and repeatedly performed based on the following steps (i) and (ii) to produce a three-dimensional shaped object.
- the obtained three-dimensional shaped object can be used as a sprue bush or a part thereof.
- An example is a powder sintering lamination method in which a metal powder is used as a powder material, and a three-dimensional shaped product manufactured thereby is used as a sprue bush or a part thereof.
- the squeezing blade 23 is moved to form a powder layer 22 having a predetermined thickness on the modeling plate 21 (see FIG. 8A).
- a light beam L is applied to a predetermined portion of the powder layer 22 to form a solidified layer 24 from the powder layer 22 (see FIG. 8B).
- a new powder layer is formed on the obtained solidified layer and irradiated with a light beam again to form a new solidified layer.
- the solidified layer 24 is laminated (see FIG. 8C), and finally, a three-dimensional structure composed of the laminated solidified layer 24 is formed.
- a shaped object can be obtained.
- a non-irradiated portion where a light beam is not partially irradiated when forming a solidified layer is used.
- the predetermined regions serving as the raw material resin flow path and the cooling medium flow path are not irradiated with the light beam and are not irradiated.
- the raw material resin flow path 10 and the cooling medium flow path 20 will be obtained in the sprue bush 100 used as a three-dimensional shaped molded article.
- a part of the sprue bush 100 (for example, the base 102 of the sprue bush) is formed by the powder sintering lamination method
- the remaining part of the sprue bush (for example, the flange part 101 of the sprue bush) is formed.
- a part of the raw material resin flow path 10 and a part of the cooling medium flow path 20 may be formed in the metal structure using a cutting tool.
- an end mill can be used as the cutting tool.
- the end mill may be a cemented carbide two-blade ball end mill.
- a part of the raw material resin flow path 10 formed in the part of the sprue bush and a part of the raw material resin flow path 10 formed in the remaining part of the sprue bush are connected to each other. Further, a part of the cooling medium flow path 20 formed in the part of the sprue bush and a part of the cooling medium flow path 20 formed in the remaining part of the sprue bush are also connected to each other.
- a desired sprue bush can be obtained by combining the precursors of the sprue bushes with each other.
- the low heat transfer section provided in the sprue bush is roughly divided into two specific modes.
- the first specific mode is a mode using a hollow part.
- the low heat transfer portion is formed of a hollow portion.
- the hollow portion may be (1) used in a vacuum state, (2) used as a heat medium flow path for flowing a heat medium, or (3) used as a space for providing a powder body.
- the hollow portion When used in a vacuum state, since there are few gas molecules that transmit heat in the hollow portion, the hollow portion can be suitably functioned as a “heat insulating region”. Further, (2) in the case of the heat medium flow path, heat conduction by the cooling medium in the cooling medium flow path is reduced by the heat generated from the heat medium, so that the hollow portion is “cooled”. It can function suitably as a “heat conduction lowering region”. (3) When the powder body is provided, since the powder particles are in “point” contact with each other in the hollow portion and the heat conduction of the powder body is relatively low, the hollow portion is referred to as a “cooling heat conduction lowering region”. It can function suitably.
- the second specific mode is a mode in which the material of the sprue bush is locally changed.
- the low heat transfer portion is made of a porous material. Due to the presence of a large number of voids in the porous material, the cooling heat caused by the cooling medium in the cooling medium flow path is reduced by the porous material. Therefore, such a porous material can be suitably functioned as a “cooling heat conduction lowering region”.
- At least one of the above-described two specific embodiments can suitably realize the “low heat transfer portion provided locally between the upstream side of the raw material resin flow path and the cooling medium flow path”. This will be described in detail below.
- the “hollow part” refers to a spatial region of the sprue bush 100 formed at least between the upstream side 10A of the raw material resin flow channel 10 and the cooling medium flow channel 20.
- the cooling of the molten raw material resin on the upstream side 10A of the raw material resin flow path 10 is more suitably suppressed, and the molten raw material resin is cooled on the upstream side 10A before the downstream side 10B.
- the phenomenon of solidification is less likely to occur. That is, the blockage of the raw material resin flow path 10 can be prevented more suitably.
- the hollow part 40 may be in a vacuum state (see FIG. 3).
- the “vacuum state” here refers to a spatial state at a pressure lower than atmospheric pressure.
- the hollow part 40 is in a state with relatively little air. That is, the hollow portion 40 has fewer gas molecules that transmit heat.
- the cooling heat resulting from the cooling medium of the cooling medium flow path 20 to the upstream side 10A of the raw material resin flow path 10 due to that.
- This means that the cooling of the molten raw material resin on the upstream side 10A is more suitably suppressed. Therefore, the phenomenon that the molten raw material resin is cooled and solidified on the upstream side 10A prior to the downstream side 10B is less likely to occur, and blockage of the raw material resin flow path 10 can be more suitably prevented.
- the hollow portion 40 does not need to be in a completely vacuum state, and may be one in which air has entered from the outside. Air has a lower thermal conductivity than metal materials.
- the thermal conductivity of a metal material for example, iron material
- the thermal conductivity of air is about 0.02 W ⁇ m ⁇ 1 ⁇ K. -1 . Therefore, even if air unintentionally enters the hollow portion, the cooling heat from the cooling medium is reduced due to the presence of the hollow portion 40.
- the hollow portion 40 in a vacuum state can be obtained by the following method, for example. First, when forming a solidified layer by a powder sintering lamination method, a hollow region is formed by finally removing the powder in a local region without irradiating a certain local region with a light beam. It is not limited to this, You may form a hollow part by giving a cutting process with respect to a local area
- the heat medium flow path hollow part 40 may be a heat medium flow path 40a as shown in FIG. 4, for example.
- a part of the heat medium flow path 40a is positioned between the upstream side 10A of the raw material resin flow path 10 and the cooling medium flow path 20 (see FIG. 4).
- the “heat medium flow path” here refers to a flow path for flowing the heat medium.
- the heat medium may be a fluid such as hot water, steam or hot air.
- the cooling medium flows through the cooling medium flow path 20 and the heat medium flows through the heat medium flow path 40a. Since at least a part of the heat medium flow path 40a is positioned between the upstream side 10A of the raw material resin flow path 10 and the cooling medium flow path 20, the cooling heat caused by the cooling medium in the cooling medium flow path 20 is heat. It is reduced in the area of the medium flow path 40a and its vicinity. That is, the cooling heat of the cooling medium flow path 20 is not easily transmitted to the upstream side 10 ⁇ / b> A of the raw material resin flow path 10. Thereby, the phenomenon that the molten raw material resin is cooled and solidified on the upstream side 10A prior to the downstream side 10B is less likely to occur, and blockage of the raw material resin flow path 10 can be more suitably prevented.
- the heat medium flow path 40a can be suitably obtained by connecting a heat medium pipe provided with a fluid pump or the like to the hollow part 40, for example.
- a powder body may be used.
- the powder body 50 may be provided in the hollow portion 40.
- the “powder body” here refers to an aggregate of powder particles made of at least one of metal powder and resin powder, for example.
- the metal powder may be, for example, an iron-based metal powder having an average particle size of about 5 ⁇ m to 100 ⁇ m.
- the resin powder may be nylon, polypropylene, ABS, or the like having an average particle size of about 30 ⁇ m to 100 ⁇ m.
- the hollow body 40 When the hollow body 40 is provided with a powder body, the effect of improving the structural strength of the sprue bush 100 can be achieved. Since the hollow portion 40 forms a “space” inside the sprue bush, it can be said that the presence of the hollow portion 40 is generally not preferable in terms of the structural strength of the sprue bush 100.
- the powder body 50 when the powder body 50 is provided in the hollow portion 40, the strength reduction caused by the hollow portion 40 can be compensated. That is, the powder body 50 provided in the hollow portion 40 can function as a reinforcing material having a structural strength.
- the hollow portion 40 is filled with more powder body 50.
- the hollow part 40 filled with the powder body 50 can be obtained through implementation of the powder sintering lamination method. Specifically, when the solidified layer is formed by the powder sintering lamination method, the region where the powder body is provided is not irradiated with a light beam, and is set as a non-irradiated portion. Then, if the powder in the non-irradiated part is not removed and left to the end, the hollow part 40 in which the powder body 50 is provided in the sprue bush 100 can be obtained.
- the present invention is not limited thereto, and a hollow region 40 is formed by cutting a local region where the metal structure is present, and powder is supplied to the hollow portion 40, so that “the hollow provided with the powder body 50 is provided. Part 40 "can also be obtained.
- the low heat transfer unit 30 may be made of a porous material 60.
- the “porous material” as used herein refers to a porous material having a large number of minute voids (that is, pores).
- the average dimension of each void is not particularly limited, but is preferably about 10 nm to 1 mm, more preferably about 20 nm to 500 nm, for example, about 100 nm.
- the air is substantially present in the gap of the porous material 60.
- the thermal conductivity of the air is smaller than the thermal conductivity of the metal material, the cooling heat from the cooling medium in the cooling medium flow path 20 is reduced by the porous material 60 in which air exists. That is, it becomes difficult for the cooling heat to be transmitted from the cooling medium flow path 20 to the upstream side 10A of the raw material resin flow path 10, and the phenomenon that the molten raw material resin is cooled and solidified on the upstream side 10A before the downstream side 10B is less likely to occur.
- the porous material 60 provided as the low heat transfer unit 30 may be obtained through a powder sintering lamination method.
- a region composed of the porous material 60 can be obtained by controlling the irradiation condition of the light beam. More specifically, when the irradiation energy of the light beam is lowered with respect to a part of the region that becomes the solidified layer, the sintered density of the part can be relatively reduced. For example, the sintered density can be 40% to 90%. Such a region of the solidified layer having a low sintered density can be used as the region of the porous material 60.
- a sintered density by the irradiation energy of the light beam as low as about 2 ⁇ 3J / mm 2 can be about 70-80%.
- the region of the porous material 60 can also be formed by such factors.
- the first and second specific modes described above are related to the low heat transfer section provided between the upstream side of the raw material resin flow path and the cooling medium flow path. Can also reduce “heat transfer to the upstream side of the raw material resin flow path”.
- Cooling medium flow path Coating layer formation
- the sprue bush 100 shown in FIG. 7 has a coating layer 70. More specifically, the coating layer 70 is provided on at least a part 20 ⁇ / b> A of the inner wall surface of the cooling medium flow path 20.
- the “coating layer” refers to a layer that covers at least a part of the inner wall surface of the cooling medium flow path 20.
- “At least a part 20A of the inner wall surface of the cooling medium flow path 20” particularly refers to the inner wall surface proximal to the upstream side 10A of the raw material resin flow path 10, as shown in FIG.
- the coating layer 70 is preferably a layer made of a low thermal conductivity material.
- the low thermal conductivity material used for the coating layer 70 is not particularly limited, and examples thereof include an epoxy resin and a silicone resin.
- the coating layer 70 of the low thermal conductivity material is provided on at least a part 20 ⁇ / b> A of the inner wall surface of the cooling medium flow path 20, the cooling heat caused by the cooling medium in the cooling medium flow path 20 is coated. Will be reduced at layer 70. Specifically, due to the coating layer 70 being made of a low thermal conductivity material, it becomes difficult for cooling heat to be transmitted to the upstream side 10 ⁇ / b> A of the raw material resin flow path 10. Therefore, the cooling of the molten raw material resin on the upstream side 10A is more suitably suppressed, and the phenomenon that the molten raw material resin is cooled and solidified on the upstream side 10A before the downstream side 10B is less likely to occur.
- the sprue bush according to an embodiment of the present invention can be used for injection of molten raw material resin into a mold cavity constituted by a core side mold and a cavity side mold of an injection mold. .
- Raw material resin flow path 10A Upstream side 20 of raw material resin flow path Cooling medium flow path 30
- Low heat transfer section 40 Hollow section 40a Heat medium flow path 50
- Powder body 60 Porous material
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- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Moulds For Moulding Plastics Or The Like (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
原料樹脂流路およびその原料樹脂流路の周囲に設けられた冷却媒体流路を有して成るスプルブッシュであって、
原料樹脂流路の上流側部分と冷却媒体流路との間の局所領域において、その局所領域以外の領域よりも相対的に小さい熱伝達となる低熱伝達部が設けられているスプルブッシュが提供される。
(i)粉末層の所定箇所に光ビームを照射し、かかる所定箇所の粉末を焼結又は溶融固化させて固化層を形成する工程。
(ii)得られた固化層の上に新たな粉末層を形成し、同様に光ビームを照射して更なる固化層を形成する工程。
以下では、低熱伝達部の具体的態様について説明する。
本発明の一実施形態に係るスプルブッシュ100では、図2に示すように、低熱伝達部が中空部40から成る。ここでいう「中空部」とは、原料樹脂流路10の上流側10Aと冷却媒体流路20との間に少なくとも形成されるスプルブッシュ100の空間領域を指している。かかる中空部40を低熱伝達部として用いることで、冷却媒体流路20の冷却媒体から生じる冷却熱を中空部40で伝わりにくくする。かかる冷却熱が中空部40で伝わりにくいと、原料樹脂流路10の上流側10Aにおける溶融原料樹脂の冷却がより好適に抑制され、下流側10Bよりも先に上流側10Aで溶融原料樹脂が冷却固化する現象が生じにくくなる。つまり、原料樹脂流路10の閉塞がより好適に防止され得る。
中空部40は、真空状態にしてよい(図3参照)。ここでいう「真空状態」とは大気圧より低い圧力の空間状態を指す。中空部40が真空状態となる場合、中空部40は、相対的に空気が少ない状態となる。すなわち、中空部40には、熱を伝える気体分子が少なくなっている。中空部40に熱を伝える気体分子が少ないと、それに起因して、冷却媒体流路20の冷却媒体に起因する冷却熱が原料樹脂流路10の上流側10Aへと伝わりにくくなる。これは、上流側10Aにおける溶融原料樹脂の冷却がより好適に抑制されることを意味している。したがって、下流側10Bよりも先に上流側10Aで溶融原料樹脂が冷却固化する現象が生じにくくなり、原料樹脂流路10の閉塞がより好適に防止され得る。
中空部40は、例えば図4に示すように熱媒体流路40aとなっていてもよい。図示する態様では、原料樹脂流路10の上流側10Aと冷却媒体流路20との間において熱媒体流路40aの一部が位置付けられている(図4参照)。ここでいう「熱媒体流路」とは、熱媒体を流すための流路のことを指している。熱媒体は、温水、蒸気または熱風などの流体であってよい。
本発明の一実施形態に係るスプルブッシュ100では粉末体が用いられてもよい。図5に示すように、例えば中空部40に粉末体50が設けられていてよい。ここでいう「粉末体」とは、例えば金属粉末および樹脂粉末の少なくとも一方から成る粉末粒子の集合体を指す。金属粉末は、例えば平均粒径5μm~100μm程度の鉄系金属粉末であってよい。また、樹脂粉末は、平均粒径30μm~100μm程度のナイロン、ポリプロピレンまたはABSなどであってよい。
本発明の一実施形態に係るスプルブッシュ100では、例えば図6に示すように、低熱伝達部30がポーラス材60から成っていてもよい。ここでいう「ポーラス材」とは多数の微小な空隙(すなわち、孔)を備えた多孔質材のことを指している。各空隙の平均寸法は、特に限定されるものではないが、好ましくは10nm~1mm程度、より好ましくは20nm~500nm程度、例えば約100nmである。
図7に示されるスプルブッシュ100はコーティング層70を有している。より具体的にはコーティング層70は冷却媒体流路20の内壁面の少なくとも一部20Aに設けられている。ここでいう「コーティング層」とは、冷却媒体流路20の内壁面の少なくとも一部を被覆する層のことを指している。「冷却媒体流路20の内壁面の少なくとも一部20A」は図7に示すように原料樹脂流路10の上流側10Aに近位する内壁面を特に指している。コーティング層70は低熱伝導率材料から成る層であることが好ましい。コーティング層70に用いられる低熱伝導率材料としては、特に限定されるものではないがエポキシ樹脂およびシリコーン樹脂などを挙げることができる。
100A 局所領域(原料樹脂流路の上流側部分と冷却媒体流路との間の局所領域)
100B 局所領域以外の領域
10 原料樹脂流路
10A 原料樹脂流路の上流側
20 冷却媒体流路
30 低熱伝達部
40 中空部
40a 熱媒体流路
50 粉末体
60 ポーラス材
Claims (6)
- 原料樹脂流路および該原料樹脂流路の周囲に設けられた冷却媒体流路を有して成るスプルブッシュであって、
前記原料樹脂流路の上流側部分と前記冷却媒体流路との間の局所領域において、該局所領域以外の領域よりも相対的に小さい熱伝達となる低熱伝達部が設けられている、スプルブッシュ。 - 前記低熱伝達部が中空部から成る、請求項1に記載のスプルブッシュ。
- 前記中空部が真空状態となっている、請求項2に記載のスプルブッシュ。
- 前記中空部が熱媒体流路となっている、請求項2に記載のスプルブッシュ。
- 前記中空部に粉末体が設けられている、請求項2に記載のスプルブッシュ。
- 前記低熱伝達部がポーラス材から成る、請求項1に記載のスプルブッシュ。
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KR1020187025870A KR20180111953A (ko) | 2016-03-09 | 2017-01-12 | 스프루 부싱 |
EP17762689.2A EP3427915A4 (en) | 2016-03-09 | 2017-01-12 | MOULE NOZZLE |
US16/083,340 US20190061217A1 (en) | 2016-03-09 | 2017-01-12 | Sprue-bush |
CN201780015597.9A CN108778668A (zh) | 2016-03-09 | 2017-01-12 | 浇道套 |
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KR102293892B1 (ko) | 2018-09-19 | 2021-08-24 | 주식회사 엘지화학 | 황-탄소 복합체의 제조방법, 그에 의해 제조된 황-탄소 복합체, 상기 황-탄소 복합체를 포함하는 양극, 및 상기 양극을 포함하는 리튬 이차 전지 |
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JP2007283503A (ja) * | 2006-04-12 | 2007-11-01 | Kanto Itami Denki Kk | スプルブッシュ |
CN101535026B (zh) * | 2006-09-27 | 2012-11-21 | 日本碍子株式会社 | 浇道套及其制造方法 |
JP5421294B2 (ja) * | 2009-01-15 | 2014-02-19 | 株式会社Opmラボラトリー | スプルーブッシュの製造方法 |
JP5124743B1 (ja) * | 2012-01-20 | 2013-01-23 | ロイアルエンジニアリング株式会社 | 射出成形用ブッシュ |
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- 2017-01-12 KR KR1020187025870A patent/KR20180111953A/ko not_active IP Right Cessation
- 2017-01-12 US US16/083,340 patent/US20190061217A1/en not_active Abandoned
- 2017-01-12 CN CN201780015597.9A patent/CN108778668A/zh active Pending
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JP2001293754A (ja) * | 2000-04-14 | 2001-10-23 | Ricoh Co Ltd | 光ディスク成形金型 |
JP2003112246A (ja) * | 2001-10-03 | 2003-04-15 | Japan Steel Works Ltd:The | 金属合金射出成形用金型 |
JP2011218735A (ja) * | 2010-04-13 | 2011-11-04 | Shin-Nihon Tech Inc | 射出成形用スプルーブッシュおよび射出成形型装置 |
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EP3427915A4 (en) | 2019-02-20 |
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JP6217993B2 (ja) | 2017-10-25 |
US20190061217A1 (en) | 2019-02-28 |
EP3427915A1 (en) | 2019-01-16 |
CN108778668A (zh) | 2018-11-09 |
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