JP2003220607A - Apparatus for preventing generation of eye mucus - Google Patents
Apparatus for preventing generation of eye mucusInfo
- Publication number
- JP2003220607A JP2003220607A JP2002021826A JP2002021826A JP2003220607A JP 2003220607 A JP2003220607 A JP 2003220607A JP 2002021826 A JP2002021826 A JP 2002021826A JP 2002021826 A JP2002021826 A JP 2002021826A JP 2003220607 A JP2003220607 A JP 2003220607A
- Authority
- JP
- Japan
- Prior art keywords
- strand
- die plate
- temperature
- gas
- die
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 210000003097 mucus Anatomy 0.000 title abstract 5
- 238000007664 blowing Methods 0.000 claims description 11
- 229910052573 porcelain Inorganic materials 0.000 claims description 4
- 210000004709 eyebrow Anatomy 0.000 claims description 2
- 230000002265 prevention Effects 0.000 claims description 2
- 229920005989 resin Polymers 0.000 abstract description 9
- 239000011347 resin Substances 0.000 abstract description 9
- 238000004140 cleaning Methods 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 22
- 239000000945 filler Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- -1 polyethylene Polymers 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 6
- 235000021395 porridge Nutrition 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 239000011324 bead Substances 0.000 description 4
- 231100000040 eye damage Toxicity 0.000 description 4
- 229920002223 polystyrene Polymers 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 229920005992 thermoplastic resin Polymers 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 239000011231 conductive filler Substances 0.000 description 3
- 210000000744 eyelid Anatomy 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 229920001955 polyphenylene ether Polymers 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 229920001400 block copolymer Polymers 0.000 description 2
- 239000010951 brass Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003365 glass fiber Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000004953 Aliphatic polyamide Substances 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920012196 Polyoxymethylene Copolymer Polymers 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229920010524 Syndiotactic polystyrene Polymers 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 229920003231 aliphatic polyamide Polymers 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- OJMOMXZKOWKUTA-UHFFFAOYSA-N aluminum;borate Chemical compound [Al+3].[O-]B([O-])[O-] OJMOMXZKOWKUTA-UHFFFAOYSA-N 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920003235 aromatic polyamide Polymers 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical class C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- UGGQKDBXXFIWJD-UHFFFAOYSA-N calcium;dihydroxy(oxo)silane;hydrate Chemical compound O.[Ca].O[Si](O)=O UGGQKDBXXFIWJD-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 1
- NJLLQSBAHIKGKF-UHFFFAOYSA-N dipotassium dioxido(oxo)titanium Chemical compound [K+].[K+].[O-][Ti]([O-])=O NJLLQSBAHIKGKF-UHFFFAOYSA-N 0.000 description 1
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 description 1
- 239000003889 eye drop Substances 0.000 description 1
- 229940012356 eye drops Drugs 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 229920005669 high impact polystyrene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 239000004797 high-impact polystyrene Substances 0.000 description 1
- 229960001545 hydrotalcite Drugs 0.000 description 1
- 229910001701 hydrotalcite Inorganic materials 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000003273 ketjen black Substances 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 239000012762 magnetic filler Substances 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229920006122 polyamide resin Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920005990 polystyrene resin Polymers 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000010456 wollastonite Substances 0.000 description 1
- 229910052882 wollastonite Inorganic materials 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、押出機のストラン
ドカットで樹脂ペレットを製造時、ダイプレートに発生
するメヤニの発生を抑制する技術に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for suppressing the occurrence of dents on a die plate when producing resin pellets by strand cutting of an extruder.
【0002】[0002]
【従来の技術】押出機ストランドカットする場合、メヤ
ニが発生する。メヤニは、ダイプレートのストランド孔
廻りに発生し、時間と共に成長していく。メヤニの発生
は、ストランド切れを起こしたり、炭化したメヤニにス
トランドに持っていかれ、ペレタイズされて、製品中に
入り、黒点になる。そのため、メヤニ対策の先行技術が
いくつか開示されている。特開平04−325223号
公報、特開平05−253997号公報、特開平05−
278094号公報の先行技術では、ダイ孔のダイプレ
ート出口の形状を円錐状に広げたり、ダイプレート表面
にストランド孔より大きい孔を作る技術で、メヤニの成
長を抑える技術が開示されている。特開平05−220
813号公報の先行技術では、ガス吹きつけ装置を使っ
て、ガスをダイプレート表面に50〜100m/秒で吹
き付け、メヤニを吹き飛ばす技術が開示されている。2. Description of the Related Art When an extruder is used for strand cutting, mesiness is generated. Meani is generated around the strand holes of the die plate and grows with time. As for the generation of mesiness, strand breakage occurs, or the mesiness is carbonized and carried to the strand, pelletized, enters the product, and becomes a black dot. For that reason, some prior arts for countermeasures against mesiness are disclosed. JP-A-04-325223, JP-A-05-253997, JP-A-05-
In the prior art of Japanese Patent No. 278094, a technique for suppressing the growth of the eyelid is disclosed by expanding the shape of the die plate outlet of the die hole into a conical shape or making a hole larger than a strand hole on the die plate surface. Japanese Patent Laid-Open No. 05-220
The prior art of Japanese Patent No. 813 discloses a technique in which a gas blowing device is used to blow a gas onto the surface of a die plate at 50 to 100 m / sec to blow away the eyelid.
【0003】[0003]
【発明が解決しようとする課題】開示された先行技術で
もメヤニ発生に関するトラブルを解決できていない。ダ
イプレート孔を加工する技術では、ダイプレート孔の廻
り掃除が不完全のため、除去できない樹脂が炭化し、炭
化物がストランドに同伴される等の不具合も発生する。
ダイプレート孔に50〜100m/秒のガスを吹き付け
る技術は、ダイプレートの孔群の配置が上下2列になる
と、下側のダイ孔群にガスが吹き付けられない等の課題
があった。メヤニは、発生を防止することと、且つメヤ
ニが発生しても成長させない技術課題があった。本発明
は、押出機ダイプレート表面に発生するメヤニの発生を
抑え、成長を抑制するメヤニ発生防止装置を得ることを
目的とする。However, even the disclosed prior arts have not been able to solve the troubles associated with the occurrence of eye damage. In the technique of processing the die plate holes, cleaning around the die plate holes is incomplete, so that the resin that cannot be removed is carbonized, and the carbides are also entrained in the strands.
The technique of blowing a gas of 50 to 100 m / sec into the die plate holes has a problem that when the die plate hole groups are arranged in two rows, that is, the gas cannot be blown to the lower die hole group. There is a technical problem that the porridge is prevented from being generated and that the porridge is not grown even if the porridge is generated. It is an object of the present invention to provide a porridge generation preventing device that suppresses the generation of porcelain that occurs on the surface of an extruder die plate and suppresses the growth.
【0004】[0004]
【課題を解決するための手段】本発明者は、メヤニに関
して、上記目的を達成するために鋭意検討した結果、メ
ヤニ発生の原因は、ダイプレートが構造上ダイ部の先端
にあり、又ダイ部より突き出ているので、ダイプレート
の表面の温度は低下し、そのため、ダイ孔廻りの金属部
の温度が低いので、その摩擦が大きくなる、というメヤ
ニが発生す機構を解明した。又、出来たメヤニは、スト
ランドに微振動を与えると、メヤニが成長する前に微振
動しているストランドに融着し、同伴されるされ、メヤ
ニが成長しないことも解明し、本発明に到達した。The inventors of the present invention have made extensive studies as to the purpose of achieving the above-mentioned object, and as a result, the cause of the occurrence of the cause is that the die plate is structurally at the tip of the die portion, and Since it is more protruding, the temperature of the surface of the die plate is lowered, and therefore the temperature of the metal part around the die hole is low, so that the friction is increased, and the mechanism that causes burr is clarified. Further, when the micro-vibration is applied to the strands, the resulting porridge melts and is entrained in the micro-vibrating strands before the porcelain grows, and it is clarified that the porcelain does not grow, reaching the present invention. did.
【0005】すなはち、本発明は次のとおりである。
1.押出機のストランドダイプレートにおいて、ダイプ
レートを温度制御し加熱する機構とストランドをガスで
振動させる機構を有することを特徴とするメヤニ発生防
止装置。
2.ダイプレートのストランド孔が上下2列に配置され
ていることを特徴とする上記1に記載のメヤニ発生防止
装置。
3.ストランドをガスで振動させる機構が250℃〜3
50℃の温度に制御したガスをストランドに秒速10〜
45m/秒に吹き付ける機構を特徴とする上記1または
2に記載のメヤニ発生防止装置。
本発明では、押出機のストランドカットするにおいて、
ダイプレートを温度制御し加熱する機構とストランドを
ガスで振動させる機構を有することを特徴とするメヤニ
発生防止装置を提供するものである。That is, the present invention is as follows. 1. A strand die plate for an extruder, which has a mechanism for controlling the temperature of the die plate to heat it and a mechanism for vibrating the strand with gas, and a device for preventing the occurrence of burr. 2. 2. The eyelid generation prevention device as described in 1 above, wherein the strand holes of the die plate are arranged in upper and lower two rows. 3. A mechanism for vibrating the strand with gas is 250 ° C to 3
Gas controlled to a temperature of 50 ° C is applied to the strands at a speed of 10 to 10
4. The device for preventing occurrence of eye damage according to 1 or 2 above, which has a mechanism of spraying at 45 m / sec. In the present invention, in the strand cutting of the extruder,
It is an object of the invention to provide an apparatus for preventing the occurrence of eye damage which has a mechanism for controlling the temperature of a die plate to heat it and a mechanism for vibrating a strand with gas.
【0006】以下、本発明を更に詳細に、図面を用いて
説明する。本発明の、ストランドカットダイプレートの
概略を図1に示す。図1中において、1はダイ部、2は
ダイプレート、3はストランド孔、4はストランド、5
はダイプレート温度センサー、6はヒーター、7はガス
吹きつけ装置である。本発明請求項1のダイプレートを
温度制御し加熱する機構とは、下記の通りである。The present invention will be described in more detail below with reference to the drawings. The outline of the strand cut die plate of the present invention is shown in FIG. In FIG. 1, 1 is a die part, 2 is a die plate, 3 is a strand hole, 4 is a strand, and 5
Is a die plate temperature sensor, 6 is a heater, and 7 is a gas blowing device. The mechanism for controlling the temperature and heating the die plate according to claim 1 of the present invention is as follows.
【0007】1.センサーが図2、3に示す位置、具体
的には、深さ方向は、ダイ表面の5〜40mmが好まし
く、横縦方向は図2にヒーターの内側ならどこでもかま
わない。
2.ヒーターは、図2に示すように、ストランド孔群の
廻りを覆って加熱する。ストランド孔の外周とヒーター
の端は、5〜20mmになるようにストランド孔廻りを
覆うことが好ましい。ヒーターは、真鍮鋳込みヒータ
ー、アルミ鋳込みヒーターが好ましく、図2に示すよう
にダイプレート表面と高さを同じくした方が好ましい。
ヒーターは、鋳込みとし、ボルトで固定することが好ま
しい。ボルトで固定できないと伝熱が不十分となり、メ
ヤニ発生防止の効果が大幅に低下する。1. The position of the sensor shown in FIGS. 2 and 3, specifically, the depth direction is preferably 5 to 40 mm of the die surface, and the horizontal and vertical directions may be anywhere inside the heater in FIG. 2. As shown in FIG. 2, the heater covers and heats around the strand hole group. It is preferable that the outer circumference of the strand hole and the end of the heater cover the area around the strand hole so as to be 5 to 20 mm. The heater is preferably a brass cast heater and an aluminum cast heater, and it is preferable that the heater has the same height as the die plate surface as shown in FIG.
The heater is preferably cast and fixed with bolts. If they cannot be fixed with bolts, heat transfer will be insufficient, and the effect of preventing the occurrence of eye damage will be greatly reduced.
【0008】熱電対とヒーターを使って温度制御をする
が、温度設定は、ダイ出口樹脂温度の−40℃〜+40
℃の範囲が好ましい。ダイ出口樹脂温度の−40℃より
低いとメヤニの発生は多くなる。又+40℃より高いと
樹脂が熱劣化して、樹脂が焼けが発生する。本発明請求
項1記載のストランドをガスで振動させる機構とは、2
50〜350℃にガス(空気、窒素、炭酸ガス)を10
〜50m/秒でストランド全体に吹き付ける装置であ
る。ストランドは、ダイプレートから出た後、すぐに2
5〜80℃の温水を張ったストランドバスで冷却され
て、引き取り速度10〜200m/分のストランドカッ
ターに搬送され、3mm×3mmのペレットにカッティ
ングされる。ストランドは、カッターの引き取り速度が
あるため、テンションが張っている。The temperature is controlled by using a thermocouple and a heater, but the temperature is set at the die outlet resin temperature of -40 ° C to +40.
The range of ° C is preferred. If the temperature of the resin at the die exit is lower than -40 ° C, the occurrence of mesiness increases. On the other hand, if the temperature is higher than + 40 ° C, the resin is thermally deteriorated and the resin is burnt. The mechanism for vibrating the strand according to claim 1 of the present invention with gas is 2
Gas (air, nitrogen, carbon dioxide) 10 at 50-350 ° C
It is a device that sprays on the entire strand at a speed of -50 m / sec. Strands immediately 2 after exiting the die plate
It is cooled in a strand bath filled with hot water of 5 to 80 ° C., conveyed to a strand cutter having a take-up speed of 10 to 200 m / min, and cut into pellets of 3 mm × 3 mm. The strands are tensioned due to the cutter take-off speed.
【0009】図1のストランド孔とストランドバスの間
の位置にあるストランドにガスを吹き付けると、ストラ
ンドが微振動を起こす。本発明は、特開平にダイプレー
トのストランド孔に直接吹きかけない。ストランド孔に
向かって直接吹きかけるとストランド切れが起こりやす
いので好ましくない。本発明のストランドに吹きかける
位置は、ストランドに微振動を与えるのが目的であるの
で、ストランド出口とストランドバスに入る中間付近が
最も好ましい。When gas is blown to the strand located between the strand hole and the strand bath in FIG. 1, the strand vibrates slightly. According to the present invention, the strand holes of the die plate are not directly sprayed. Spraying directly toward the strand holes is not preferable because strand breakage easily occurs. The position of spraying the strand of the present invention is for the purpose of giving a slight vibration to the strand, and therefore, the vicinity of the middle between the strand outlet and the strand bath is most preferable.
【0010】本発明の押出機は、二軸同方向回転押出
機、単軸押出機、ブス社のコニーダー(登録商法)が使
われる。ダイプレートのストランド孔直径は、1.5〜
7mm程度である。ランド長は、3〜10ストランド孔
直径である。孔の数は、押出機能力に比例する。通常当
業者の常識では、ストランド孔直径 4.0mmのと
き、5〜25kg/Hに設定する。ストランド孔は、一
列に配置するのが好ましい。例えば、ストランド孔直径
が4mmで1穴当たりの押出量が25kg/Hを越える
場合、ストランド孔直径を大きくし、押出量を上げ、且
つストランドカッターの引き取り速度を上げて、ペレッ
トサイズを、例えば3mm×3mmに合わせる。カッタ
ー引き取り速度が速すぎて、ストランド切れを起こす場
合、ストランド孔数を増やす。孔は、上下2列に配置す
る。通常は、千鳥配列という配列で上下2段に配置す
る。As the extruder of the present invention, a twin-screw co-rotating extruder, a single-screw extruder, and a co-kneader (registered trademark) manufactured by Bus Co. are used. Strand hole diameter of die plate is 1.5 ~
It is about 7 mm. The land length is 3 to 10 strand hole diameter. The number of holes is proportional to the extrusion force. Usually, according to the common sense of those skilled in the art, when the diameter of the strand hole is 4.0 mm, it is set to 5 to 25 kg / H. The strand holes are preferably arranged in a row. For example, when the strand hole diameter is 4 mm and the extrusion amount per hole exceeds 25 kg / H, the strand hole diameter is increased, the extrusion amount is increased, and the take-up speed of the strand cutter is increased to increase the pellet size to, for example, 3 mm. Adjust to × 3 mm. If the cutter take-off speed is too fast and strand breakage occurs, increase the number of strand holes. The holes are arranged in two rows above and below. Usually, they are arranged in two rows, upper and lower, in a staggered arrangement.
【0011】本発明のメヤニ発生防止に効果のある熱可
塑性樹脂は、ポリエチレン、中密度ポリエチレン、低密
度ポリエチレン、線状低密度ポリエチレン、ポリプロピ
レン、エチレン・プロピレン共重合体、エチレン・αオ
レフィン共重合体等、ホモポリオキシメチレン、ポリオ
キシメチレンコポリマー、ポリフェニレンスルヒド、シ
ンジオタクチックポリスチレン、ポリアミド系樹脂(ナ
イロン6、ナイロン66、芳香族ポリアミド、芳香族・
脂肪族ポリアミド共重合体等)、ポリエステル系樹脂
(ポリブチレンテレフタレート、ポリエチレンテレフタ
レート等)を挙げることができる。この中で高密度ポリ
エチレン、ポリプロピレン、ポリオキシメチレン、ポリ
フェニレンエーテル、ポリカーボネート、ポリスチレン
系樹脂、水素添加スチレン・ブタジエンブロック共重合
体、水素添加スチレン・イソプレンブロック共重合体等
が好ましい。またこれらの熱可塑性樹脂同士を混ぜ合わ
せても構わない。The thermoplastic resin of the present invention which is effective in preventing the occurrence of eye drops is polyethylene, medium density polyethylene, low density polyethylene, linear low density polyethylene, polypropylene, ethylene / propylene copolymer, ethylene / α-olefin copolymer. Etc., homopolyoxymethylene, polyoxymethylene copolymer, polyphenylene sulfide, syndiotactic polystyrene, polyamide resin (nylon 6, nylon 66, aromatic polyamide, aromatic
Examples thereof include aliphatic polyamide copolymers) and polyester resins (polybutylene terephthalate, polyethylene terephthalate, etc.). Among them, high density polyethylene, polypropylene, polyoxymethylene, polyphenylene ether, polycarbonate, polystyrene resin, hydrogenated styrene / butadiene block copolymer, hydrogenated styrene / isoprene block copolymer and the like are preferable. Further, these thermoplastic resins may be mixed together.
【0012】本発明に適用できる熱可塑性樹脂の充填剤
は、重質炭酸カルシウム、膠質炭酸カルシウム、軟質炭
酸カルシウム、シリカ、カオリン、クレー、酸化チタ
ン、硫酸バリウム、酸化亜鉛、アルミナ、水酸化マグネ
シウム、タルク、マイカ、ガラスフレーク、ハイドロタ
ルサイト、針状フィラー(ウオラストナイト、チタン酸
カリウム、塩基性硫酸マグネシウム、セプライト、ゾノ
トライト、ホウ酸アルミニウム)、ガラスビーズ、シリ
カビーズ、アルミナビーズ、カーボンビーズ、ガラスバ
ルーン、金属系導電性フィラー、非金属製導電性フィラ
ー、カーボン、磁性フィラー、圧電・焦電フィラー、摺
動性フィラー、封止材用フィラー、紫外線吸収フィラ
ー、制振用フィラー等とガラスファイバー、炭素繊維、
金属繊維、導電性フィラー(ケッチェンブラック、アセ
チレンブラック)、滴下防止剤(テフロン(登録商
標),シリコン樹脂)、難燃剤、油類、安定剤、潤滑
剤、相溶化剤、その他の添加剤を添加しても構わない。Thermoplastic resin fillers applicable to the present invention include heavy calcium carbonate, colloidal calcium carbonate, soft calcium carbonate, silica, kaolin, clay, titanium oxide, barium sulfate, zinc oxide, alumina, magnesium hydroxide, Talc, mica, glass flake, hydrotalcite, needle-like filler (wollastonite, potassium titanate, basic magnesium sulfate, celite, xonotlite, aluminum borate), glass beads, silica beads, alumina beads, carbon beads, glass Balloons, metallic conductive fillers, non-metallic conductive fillers, carbon, magnetic fillers, piezoelectric / pyroelectric fillers, slidable fillers, sealing material fillers, ultraviolet absorbing fillers, vibration damping fillers and glass fibers, Carbon fiber,
Metal fibers, conductive fillers (Ketjen black, acetylene black), anti-drip agents (Teflon (registered trademark), silicone resin), flame retardants, oils, stabilizers, lubricants, compatibilizers, and other additives You may add.
【0013】[0013]
【発明の実施の形態】本発明について、以下実施例に基
づき、具体的に説明する。押出機は、二軸同方向回転押
出機(ワーナー・アンド・フライドラー社製「ZSK−
25」、L/D=42)を使い、スクリュ構成を変えて
実施した。押出条件は、特に断りがない限り、熱可塑性
樹脂は旭化成株式会社のポリフェニレンエーテル68w
t%とエーアンドエムポリスチレン社製ゼネラルパーパ
スポリスチレン685の押出機で溶融混練したマスター
バッチを100重量部TOPからフィードし、供給量2
0kg/H、スクリュ回転数300rpmとした。バレ
ル温度は、290℃に設定した。ストランド孔は、2
個、孔径は、4mmとした。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described based on the following examples. The extruder is a twin-screw co-rotating extruder ("ZSK-" manufactured by Warner & Freidler).
25 ", L / D = 42), and the screw configuration was changed. Unless otherwise specified, the extrusion conditions are thermoplastic resins such as polyphenylene ether 68w manufactured by Asahi Kasei Corporation.
A master batch melt-kneaded with t% and an General Purpose Polystyrene 685 manufactured by A & M Polystyrene Co., Ltd. is fed from 100 parts by weight of TOP, and a supply amount is 2
The rotation speed was 0 kg / H and the screw rotation speed was 300 rpm. The barrel temperature was set to 290 ° C. 2 strand holes
The number of holes was 4 mm.
【0014】[0014]
【実施例1】ダイ出口樹脂温度は、350℃であったた
め、ダイプレートの設定温度を350℃にした。ガス吹
きつけ装置は、空気を使い、吹きつけ装置のガス排出口
の空気温度が300℃になるように温度設定をした。吹
きつけ装置のガス排出口のガス流速が350℃で40m
/秒に設定した。ガス吹きつけ装置を使いストランドに
該条件空気を吹き付けた。メヤニの発生は少なく、ダイ
プレートのメヤニ除去は、8時間に一回であった。Example 1 Since the die outlet resin temperature was 350 ° C, the die plate temperature was set to 350 ° C. The gas blowing device used air, and the temperature was set so that the air temperature at the gas outlet of the blowing device was 300 ° C. The gas flow rate at the gas outlet of the spraying device is 40 m at 350 ° C.
/ Sec. The conditioned air was blown onto the strands using a gas blowing device. The occurrence of dents was small and the dents on the die plate were removed once every 8 hours.
【0015】[0015]
【比較例1】実施例1のダイプレートの設定温度を28
0℃とした以外は、実施例1と同じ条件で実施した。メ
ヤニの発生が増えた。ダイプレートのメヤニ除去は、
1.5時間に一回であった。Comparative Example 1 The set temperature of the die plate of Example 1 was set to 28
It carried out on the same conditions as Example 1 except having set it as 0 degreeC. Increasing number of eyebrows. Removal of the die plate
It was once every 1.5 hours.
【0016】[0016]
【比較例2】実施例1のガス吹きつけ装置を外した以外
は、実施例1と同じ条件で実施した。メヤニの発生は実
施例1より増えて、ダイプレートのメヤニ除去は、3時
間に一回であった。COMPARATIVE EXAMPLE 2 The procedure of Example 1 was repeated except that the gas blowing device of Example 1 was removed. The generation of dents increased more than in Example 1, and the dent removal of the die plate was performed once every 3 hours.
【0017】[0017]
【比較例3】実施例1のガス吹きつけ装置を外した以外
は、比較例1と同じ条件で実施した。メヤニの発生量は
比較例1に比べさらに増えた。ダイプレートのメヤニ除
去は、1.0時間に一回であった。Comparative Example 3 The procedure of Comparative Example 1 was repeated except that the gas blowing device of Example 1 was removed. The amount of porridge generated was further increased compared to Comparative Example 1. The die plate was removed every 1.0 hour.
【0018】[0018]
【実施例2】実施例1を旭化成株式会社製ポリフェニレ
ンエーテル40重量部、エーアンドエムポリスチレン株
式会社製ポリスチレン685 15重量部、ハイインパ
クトポリスチレンH9302 15重量部、直径が13
μmのガラスファイバー 30重量部を実施例1と同じ
条件で押し出した。ダイ出口樹脂温度は342℃であっ
た。ダイプレートの設定温度を340℃とし、ガス吹き
つけ装置の温度設定を340℃、ガス流速を40m/秒
とした以外は、実施例1と同じ条件で押し出した。メヤ
ニの発生は少なく、ダイプレートのメヤニ除去は、6時
間に一回であったExample 2 Example 1 was repeated with 40 parts by weight of polyphenylene ether manufactured by Asahi Kasei Corporation, 15 parts by weight of polystyrene 685 manufactured by A & M Polystyrene Co., 15 parts by weight of high-impact polystyrene H9302, and diameter of 13
30 parts by weight of μm glass fiber was extruded under the same conditions as in Example 1. The die exit resin temperature was 342 ° C. Extrusion was performed under the same conditions as in Example 1 except that the die plate set temperature was 340 ° C., the temperature of the gas blowing device was 340 ° C., and the gas flow rate was 40 m / sec. The occurrence of dents was small, and the dents on the die plate were removed once every 6 hours.
【0019】[0019]
【実施例3】実施例1の運転条件を600rpm、押出
量を40kg/H、ダイプレートのストランド孔径を
3.5mmにし、ストランド孔数を上2個、下3個の千
鳥配列にしたダイプレートを設置した以外は、実施例1
と同一条件で行った。メヤニの発生は少なく、ダイプレ
ートのメヤニ除去は、8時間に一回であった。[Example 3] The operating conditions of Example 1 were 600 rpm, the extrusion rate was 40 kg / H, the die plate had a strand hole diameter of 3.5 mm, and the die plate had a staggered arrangement of two upper and three lower strand holes. Example 1 except that
The same conditions were used. The occurrence of dents was small and the dents on the die plate were removed once every 8 hours.
【0020】[0020]
【発明の効果】本発明のメヤニ発生防止装置を用いると
メヤニの発生を抑えることができる。[Effects of the Invention] By using the apparatus for preventing the occurrence of dents of the present invention, the occurrence of dents can be suppressed.
【図1】本発明に係るダイ部横断面図である。FIG. 1 is a cross-sectional view of a die portion according to the present invention.
【図2】本発明に係るダイ部正面図である。FIG. 2 is a front view of a die section according to the present invention.
【図3】本発明に係るダイ部を下方から見た断面図であ
る。FIG. 3 is a cross-sectional view of a die unit according to the present invention as seen from below.
1:ダイ部 2:ダイプレート 3:ストランド孔 4:ストランド 5:ダイプレート温度測定用熱電対 6:真鍮鋳込みヒーター 7:ガス吹きつけ装置 1: Die part 2: Die plate 3: Strand hole 4: Strand 5: Thermocouple for measuring die plate temperature 6: Brass cast heater 7: Gas blowing device
Claims (3)
て、ダイプレートを温度制御し加熱する機構とストラン
ドをガスで振動させる機構を有することを特徴とするメ
ヤニ発生防止装置。1. A strand die plate for an extruder, which has a mechanism for controlling the temperature of the die plate to heat it and a mechanism for vibrating the strand with a gas, and a device for preventing generation of porcelain.
に配置されていることを特徴とする請求項1に記載のメ
ヤニ発生防止装置。2. The eyebrow generation preventing device according to claim 1, wherein the strand holes of the die plate are arranged in upper and lower two rows.
50℃〜350℃の温度に制御したガスをストランドに
秒速10〜45m/秒に吹き付ける機構を特徴とする請
求項1または2に記載のメヤニ発生防止装置。3. A mechanism for vibrating the strand with gas is 2
The burn-in prevention device according to claim 1 or 2, which has a mechanism for blowing a gas, which is controlled at a temperature of 50 ° C to 350 ° C, to the strand at a speed of 10 to 45 m / sec.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002021826A JP2003220607A (en) | 2002-01-30 | 2002-01-30 | Apparatus for preventing generation of eye mucus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002021826A JP2003220607A (en) | 2002-01-30 | 2002-01-30 | Apparatus for preventing generation of eye mucus |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003220607A true JP2003220607A (en) | 2003-08-05 |
Family
ID=27744961
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2002021826A Pending JP2003220607A (en) | 2002-01-30 | 2002-01-30 | Apparatus for preventing generation of eye mucus |
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JP (1) | JP2003220607A (en) |
Cited By (7)
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WO2008090673A1 (en) * | 2007-01-24 | 2008-07-31 | Mitsubishi Chemical Corporation | Process for producing aromatic polycarbonate |
WO2009091073A1 (en) * | 2008-01-15 | 2009-07-23 | Yazaki Corporation | Method and apparatus for forming strands |
JP2010030176A (en) * | 2008-07-30 | 2010-02-12 | Toray Ind Inc | Method for manufacturing thermoplastic resin composition pellet |
WO2011136273A1 (en) * | 2010-04-28 | 2011-11-03 | Wpcコーポレーション株式会社 | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
WO2011135745A1 (en) * | 2010-04-28 | 2011-11-03 | Wpcコーポレーション株式会社 | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
CN101489749B (en) * | 2007-01-24 | 2013-01-30 | 三菱化学株式会社 | Process for producing aromatic polycarbonate |
WO2018050674A1 (en) * | 2016-09-13 | 2018-03-22 | Maag Automatik Gmbh | Method and device for extruding plastics |
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2002
- 2002-01-30 JP JP2002021826A patent/JP2003220607A/en active Pending
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Publication number | Priority date | Publication date | Assignee | Title |
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CN101489749B (en) * | 2007-01-24 | 2013-01-30 | 三菱化学株式会社 | Process for producing aromatic polycarbonate |
WO2008090673A1 (en) * | 2007-01-24 | 2008-07-31 | Mitsubishi Chemical Corporation | Process for producing aromatic polycarbonate |
US8715552B2 (en) | 2007-01-24 | 2014-05-06 | Mitsubishi Chemical Corporation | Production method of aromatic polycarbonate |
WO2009091073A1 (en) * | 2008-01-15 | 2009-07-23 | Yazaki Corporation | Method and apparatus for forming strands |
TWI383877B (en) * | 2008-01-15 | 2013-02-01 | Yazaki Corp | Method and apparatus for forming strands |
JP2010030176A (en) * | 2008-07-30 | 2010-02-12 | Toray Ind Inc | Method for manufacturing thermoplastic resin composition pellet |
WO2011136273A1 (en) * | 2010-04-28 | 2011-11-03 | Wpcコーポレーション株式会社 | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
JP2011230419A (en) * | 2010-04-28 | 2011-11-17 | Wpc Corporation Kk | Method for manufacturing composite pellet for extrusion molding and composite pellet for extrusion molding, manufactured by method |
EP2565004A1 (en) * | 2010-04-28 | 2013-03-06 | WPC Corporation | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
EP2565004A4 (en) * | 2010-04-28 | 2013-10-16 | Wpc Corp | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
WO2011135745A1 (en) * | 2010-04-28 | 2011-11-03 | Wpcコーポレーション株式会社 | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
AU2011246076B2 (en) * | 2010-04-28 | 2014-06-05 | Beijing Shengsheng Culture Limited Liability Company | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
US8871345B2 (en) | 2010-04-28 | 2014-10-28 | Wpc Corporation | Method for producing composite pellet for extrusion molding, and composite pellet for extrusion molding produced by the method |
WO2018050674A1 (en) * | 2016-09-13 | 2018-03-22 | Maag Automatik Gmbh | Method and device for extruding plastics |
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