JP3096374B2 - Mixed granulated product of synthetic resin powder and filler and method for producing the same - Google Patents

Mixed granulated product of synthetic resin powder and filler and method for producing the same

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Publication number
JP3096374B2
JP3096374B2 JP11932493A JP11932493A JP3096374B2 JP 3096374 B2 JP3096374 B2 JP 3096374B2 JP 11932493 A JP11932493 A JP 11932493A JP 11932493 A JP11932493 A JP 11932493A JP 3096374 B2 JP3096374 B2 JP 3096374B2
Authority
JP
Japan
Prior art keywords
synthetic resin
granulated product
resin powder
filler
powder
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.)
Expired - Fee Related
Application number
JP11932493A
Other languages
Japanese (ja)
Other versions
JPH06320535A (en
Inventor
喜夫 鈴木
Original Assignee
川鉄鉱業株式会社
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 川鉄鉱業株式会社 filed Critical 川鉄鉱業株式会社
Priority to JP11932493A priority Critical patent/JP3096374B2/en
Publication of JPH06320535A publication Critical patent/JPH06320535A/en
Application granted granted Critical
Publication of JP3096374B2 publication Critical patent/JP3096374B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/12Making granules characterised by structure or composition

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、合成樹脂粉末とフィラ
ーとの混合造粒物及びその製造方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granulated mixture of a synthetic resin powder and a filler and a method for producing the same.

【0002】[0002]

【従来の技術】合成樹脂に無機質フィラーを混入して樹
脂の特性を改質する際、樹脂粉末又はペレットとフィラ
ー粉末とをそれぞれ原料のまま単独で、もしくは両者を
予め混合後、直接、成形機に供給する方法が知られてい
る。この場合、フィラーは粉末であるため、成形機のホ
ッパー内でブリッジ現象(いわゆる棚吊り)あるいはス
クリューへの食い込み不良等が発生し、生産性の低下及
び品質のバラツキ等の問題が生じる。
2. Description of the Related Art When modifying the properties of a resin by mixing an inorganic filler into a synthetic resin, a resin powder or a pellet and a filler powder are used alone as raw materials, or both are mixed in advance, and then directly into a molding machine. Is known. In this case, since the filler is a powder, a bridging phenomenon (so-called shelving) or poor penetration into the screw occurs in the hopper of the molding machine, which causes problems such as a reduction in productivity and a variation in quality.

【0003】そこで、樹脂ペレットとフィラーの造粒品
とをそれぞれ単独で、もしくは両者を予め混合後、成形
機に供給する方法(特開昭51−90336号)、樹脂
粉末とフィラー粉末とを攪拌機内で高速攪拌し、樹脂を
軟化又は溶融させることにより、樹脂とフィラーとの混
合物を得る方法等が提案されている。
[0003] Therefore, a method in which a resin pellet and a granulated filler are used alone, or a mixture of the two is supplied in advance to a molding machine (JP-A-51-90336). There has been proposed a method of obtaining a mixture of a resin and a filler by stirring the resin at a high speed to soften or melt the resin.

【0004】[0004]

【発明が解決しようとする課題】しかし、前者の方法に
おいては、成形後フィラーが粉末で使用したときのよう
には樹脂中に良好に分散せず、品質低下の原因となり易
く、また樹脂とフィラーとの配合率のバラツキを生じ易
い。後者の場合は、樹脂やフィラーの種類によっては、
受ける熱履歴及び機械的な剪断のため、変質やひいては
品質の低下を起こす等の問題点がある。
However, in the former method, the filler after molding does not disperse well in the resin as when it is used as a powder, and is liable to cause quality deterioration. Tends to occur. In the latter case, depending on the type of resin or filler,
Due to the heat history and mechanical shearing, there are problems such as deterioration and eventually deterioration in quality.

【0005】本発明は、上記従来の問題点を解決したも
のであって、その目的は取扱性、作業性が優れた粒状物
とし、樹脂に対し粉末同様の高分散性を与え、かつ配合
率のバラツキを無くし、品質の安定した樹脂成形品を得
ることができる、合成樹脂粉末とフィラーとの混合造粒
物及びその製造方法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned conventional problems, and has as its object to provide a granular material having excellent handleability and workability, to provide a resin with high dispersibility similar to powder, It is an object of the present invention to provide a mixed granulated product of a synthetic resin powder and a filler and a method for producing the same, which can obtain a resin molded product having a stable quality by eliminating the variation of the above.

【0006】[0006]

【課題を解決するための手段】本発明は上記の目的を達
成するためなされたもので、ポリプロピレン、ナイロ
ン、ポリスチレン、ポリ塩化ビニルから選ばれる少なく
とも1種の合成樹脂粉末と粉末状無機質フィラーとを、
前記合成樹脂粉末を軟化又は溶融させないで混合して造
粒して得られた造粒物であって、該造粒物の粒径が0.
1〜5mmであることを特徴とする合成樹脂粉末とフィ
ラーとの混合造粒物である。
The present invention SUMMARY OF] has been made for achieving the above object, polypropylene, nylon
, Polystyrene, polyvinyl chloride
And one kind of synthetic resin powder and powdery inorganic filler,
A granulated product obtained by mixing and granulating the synthetic resin powder without softening or melting, wherein the particle size of the granulated product is 0.1.
A mixed granulated product of a synthetic resin powder and a filler, which is 1 to 5 mm.

【0007】該造粒物は、合成樹脂粉末を軟化又は溶融
させないで造粒して得られたものであるから、熱履歴及
び機械的な剪断を受けることがなく、変質やひいては品
質の低下を起こすことがない。また、造粒物の粒径が
0.1mmに満たないものは充分な流動性が得られず取
扱い難くなり、5mmを超えるものは樹脂成形時の分散
性が不良となるので造粒物の粒径が0.1〜5mmの範
囲内にあることが肝要である。
[0007] Since the granulated product is obtained by granulating the synthetic resin powder without softening or melting, the granulated product is not subjected to heat history and mechanical shearing, and is not deteriorated or deteriorated in quality. Never wake up. If the particle size of the granulated material is less than 0.1 mm, sufficient fluidity cannot be obtained and it is difficult to handle. If the particle size exceeds 5 mm, the dispersibility at the time of resin molding becomes poor. It is important that the diameter be in the range of 0.1 to 5 mm.

【0008】上記の造粒物は、合成樹脂粉末と粉末状無
機質フィラーとを予め混合した後、水又は有機質溶媒又
は両者の混合液を分散媒として加え、攪拌型造粒機によ
り造粒後、乾燥することにより得ることができる。な
お、必要に応じて添加剤を配合することも可能である。
The above-mentioned granulated product is prepared by mixing a synthetic resin powder and a powdered inorganic filler in advance, adding water or an organic solvent or a mixed solution of both as a dispersion medium, and granulating with a stirring granulator. It can be obtained by drying. In addition, it is also possible to mix | blend an additive as needed.

【0009】本発明に用いられる合成樹脂粉末は、熱可
塑性樹脂の粉末であり、ポリプロピレン、ナイロン、ポ
リスチレン、ポリ塩化ビニルから選ばれる少なくとも1
種の合成樹脂粉末である。粉末の粒子径は100μm以
下である。
The synthetic resin powder used in the present invention is heat-resistant.
Powder of plastic resin, polypropylene, nylon,
At least one selected from polystyrene and polyvinyl chloride
Kind of synthetic resin powder. The particle size of the powder is 100 μm or less.

【0010】粉末状無機質フィラーとしては、例えば、
酸化チタン、シリカ、タルク、カーボンブラック等の粉
末を用いることができ、その種類は特に限定されない。
粉末の粒子径は100μm以下である。合成樹脂粉末と
粉末状無機質フィラーとの配合比は、必要に応じて設定
でき、特に限定されるものではない。
Examples of the powdery inorganic filler include:
Powders such as titanium oxide, silica, talc, and carbon black can be used, and the type is not particularly limited.
The particle size of the powder is 100 μm or less. The mixing ratio of the synthetic resin powder and the powdery inorganic filler can be set as required, and is not particularly limited.

【0011】本発明方法においては分散媒として水を用
いる他、有機質溶媒、さらに両者の混合液を用いること
ができる。有機質溶媒としては、乾燥により除去され造
粒物中に残留しないもので、メタノール、エタノール、
ジエチルエーテル、ベンゼン、ベンゼン、トルエン等が
用いられる。比較的低沸点のものを用いることで乾燥コ
ストを削減できる。疎水性の無機質フィラー等を用いる
場合には有機質溶媒を用いるか又は水と有機質溶媒との
混合液を用いる。水と有機質溶媒の混合割合は、造粒性
の確保、乾燥コストの削減、有機質溶媒コストの削減等
の観点を総合して決められるであろう。有機質溶媒は、
造粒後は回収して再使用され得る。
In the method of the present invention, in addition to using water as a dispersion medium, an organic solvent and a mixed solution of both can be used. Organic solvents that are removed by drying and do not remain in the granulated material include methanol, ethanol,
Diethyl ether, benzene, benzene, toluene and the like are used. Drying cost can be reduced by using a material having a relatively low boiling point. When a hydrophobic inorganic filler or the like is used, an organic solvent is used or a mixed solution of water and an organic solvent is used. The mixing ratio of water and the organic solvent will be determined based on the viewpoints of ensuring granulation properties, reducing drying costs, reducing organic solvent costs, and the like. Organic solvents are
After granulation, it can be collected and reused.

【0012】[0012]

【実施例】以下、実施例を挙げて説明する。合成樹脂粉
末として使用したポリプロピレン(以下PPと記す)
は、JIS K 7116によるメルトフローインデッ
クス(MFI)が9.05g/10分、JIS K 7
113及びJIS K 7116に従って測定した引張
強度、曲げ強度及び曲げ弾性率がそれぞれ3.10、
3.82及び135kgf/mm2 であるPPで平均粒
子径が約50μmの粉末である。
Embodiments will be described below with reference to embodiments. Polypropylene used as synthetic resin powder (hereinafter referred to as PP)
Means that the melt flow index (MFI) according to JIS K 7116 is 9.05 g / 10 min, and JIS K 7116
The tensile strength, flexural strength and flexural modulus measured according to JIS K 113 and JIS K 7116 are 3.10, respectively.
It is a powder having an average particle diameter of about 50 μm with PP of 3.82 and 135 kgf / mm 2 .

【0013】また無機質フィラーとしては酸化チタンを
用い、酸化チタン粉末は平均粒子径が0.3μmのルチ
ル型粉末を使用し、またチタン酸カリウムウイスカー
(以下PTWと記す)は、平均繊維長が20.5μm、
繊維径は0.5μmのものを用いた。
Titanium oxide is used as the inorganic filler, rutile type powder having an average particle diameter of 0.3 μm is used as the titanium oxide powder, and potassium titanate whisker (hereinafter referred to as PTW) has an average fiber length of 20 μm. .5 μm,
The fiber diameter was 0.5 μm.

【0014】[0014]

【実施例1】PP粉末:酸化チタン粉末=70:30w
t%の配合比でよく混合し、この混合物5kgを攪拌型
造粒機(ヘンシェルミキサー)に入れ、水1.5リット
ルを加えた後、1000rpmの回転数で5分間常温で
造粒した。その後流動乾燥機で乾燥し、表1に示す粒度
の造粒物を得た。この造粒物をベント付射出成形機に供
給し、試験片を成形後、各物性を測定した。結果は表2
に示すとおりであった。
Example 1 PP powder: titanium oxide powder = 70: 30 w
The mixture was mixed well at a mixing ratio of t%, 5 kg of this mixture was put into a stirring granulator (Henschel mixer), 1.5 liter of water was added, and the mixture was granulated at 1,000 rpm for 5 minutes at room temperature. Then, it was dried with a fluidized drier to obtain a granulated product having a particle size shown in Table 1. The granulated product was supplied to an injection molding machine equipped with a vent, and after a test piece was molded, each physical property was measured. Table 2 shows the results
Was as shown in FIG.

【0015】[0015]

【実施例2】PP粉末:PTW=70:30wt%の配
合比でよく混合し、この混合物5kgを攪拌型造粒機
(ヘンシェルミキサー)に入れ、水:メタノール=1:
1の混合液2.3リットルを加えた後、1000rpm
の回転数で5分間造粒した。その後流動乾燥機で乾燥
し、表1に示す粒度の造粒物を得た。この造粒物を実施
例1と同様、ベント付射出成形機に供給し、試験片を成
形後、各物性を測定した。結果は表2に示すとおりであ
った。
Example 2 PP powder: PTW = 70: 30 wt% was mixed well, 5 kg of this mixture was put into a stirring granulator (Henschel mixer), and water: methanol = 1: 1.
After adding 2.3 liters of the mixed solution of Example 1, 1000 rpm
At 5 rpm for 5 minutes. Then, it was dried with a fluidized drier to obtain a granulated product having a particle size shown in Table 1. The granulated product was supplied to a vented injection molding machine in the same manner as in Example 1, and after the test piece was molded, each physical property was measured. The results were as shown in Table 2.

【0016】[0016]

【比較例1】PP粉末:酸化チタン造粒物=70:30
wt%の配合比でV型ブレンダーで5分間混合して混合
物を得た。この混合物を実施例1と同様、ベント付射出
成形機に供給し、試験片を成形後、各物性を測定した。
結果は表2に示すとおりであった。なお、上記酸化チタ
ン造粒物は、酸化チタン粉末3kgをヘンシェルミキサ
ーに投入後、水0.6リットルを加えて800rpmで
3分間造粒後、流動乾燥機により乾燥して得た造粒物で
あり、表1に粒度を示した。
[Comparative Example 1] PP powder: titanium oxide granulated product = 70:30
The mixture was obtained by mixing at a blending ratio of wt% for 5 minutes in a V-type blender. This mixture was supplied to a vented injection molding machine in the same manner as in Example 1, and after the test piece was molded, each physical property was measured.
The results were as shown in Table 2. The titanium oxide granules were obtained by adding 3 kg of titanium oxide powder to a Henschel mixer, adding 0.6 liter of water, granulating at 800 rpm for 3 minutes, and drying with a fluidized drier. Yes, and Table 1 shows the particle size.

【0017】[0017]

【比較例2】PP粉末:PTW=70:30wt%の配
合比で混合し、この混合物5kgをヘンシェルミキサー
に入れ、窒素シール下にて槽内温度が185℃になるま
で約30分間、1100rpmの回転数で攪拌しポリプ
ロピレンを溶融させ、次いでミキサーを冷却しながら6
00rpmで攪拌してPP粉末とPTWの混合物を得た
(表1)。これを実施例1と同様にベント付射出成形機
に供給し、試験片を成形後、各物性を測定した。結果は
表2に示すとおりであった。
COMPARATIVE EXAMPLE 2 PP powder: PTW = 70: 30 wt% was mixed at a mixing ratio, 5 kg of this mixture was put into a Henschel mixer, and the temperature in the tank was reduced to 1185 rpm for about 30 minutes under a nitrogen blanket until the temperature reached 185 ° C. Stir at speed to melt the polypropylene and then cool while mixing
The mixture was stirred at 00 rpm to obtain a mixture of PP powder and PTW (Table 1). This was supplied to a vented injection molding machine in the same manner as in Example 1, and after the test piece was molded, each physical property was measured. The results were as shown in Table 2.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【表2】 [Table 2]

【0020】なお、表2における各測定方法は次のとお
りである。 〔フィラーの配合率測定法〕試験片を500℃の電気マ
ッフル炉中で2時間燃焼させ、残存した白色粉末をフィ
ラーとして計量し、配合率を算出した。
The measuring methods in Table 2 are as follows. [Method of Measuring Mixing Ratio of Filler] A test piece was burned for 2 hours in an electric muffle furnace at 500 ° C., and the remaining white powder was weighed as a filler to calculate a mixing ratio.

【0021】〔強度測定法〕引張試験及び曲げ試験は、
JIS K 7113及びJIS K 7116に従っ
て測定した。なお、試験片の作製は、ベント付射出成形
機(スクリュー径:25mm,ノズル温度:220℃)
にて実施した。
[Strength measuring method] The tensile test and the bending test
It was measured according to JIS K 7113 and JIS K 7116. In addition, the preparation of the test piece was performed using an injection molding machine with a vent (screw diameter: 25 mm, nozzle temperature: 220 ° C.).
Was carried out.

【0022】〔PTWの射出成形後の平均繊維長測定方
法〕配合率測定方法と同様に、試験片の樹脂分を燃焼さ
せた後、残存したPTWを画像解析装置により繊維長を
測定した。
[Method of measuring average fiber length after injection molding of PTW] In the same manner as in the method of measuring the compounding ratio, the resin content of the test piece was burned, and the remaining PTW was measured for fiber length by an image analyzer.

【0023】〔分散性の測定及び評価方法〕試験片を厚
さ50±10μmのフイルム状にスライスし、軟X線装
置で撮影後、フィラー凝集物の有無を顕微鏡(100
倍)で観察し、凝集物が生じないものを良とし、凝集物
が生じたものを不良とした。不良のものの凝集物の最大
径は約50μmであった。
[Method of Measuring and Evaluating Dispersibility] A test piece was sliced into a film having a thickness of 50 ± 10 μm and photographed with a soft X-ray apparatus.
X), and those without aggregates were evaluated as good, and those with aggregates were evaluated as poor. The maximum diameter of the aggregates of the defective ones was about 50 μm.

【0024】[0024]

【発明の効果】本発明の造粒物は造粒物であるから、樹
脂に配合する際成形機ホッパー内での棚吊り現象を生ぜ
ず、安定供給することができ、作業性が良く、また、造
粒物は所定の配合比で混合されているため、成形後の配
合率のバラツキは激減する。製造に当たっては、合成樹
脂粉末を軟化、溶融させず、樹脂やフィラーが熱履歴や
剪断を受けることがないから変質することなく造粒で
き、また水又は有機質溶媒を分散媒として攪拌型造粒機
で造粒するので、溶媒は回収可能である。また、水や有
機溶媒を用いるため、親水性材料、疏水性材料いずれに
も対応できる利点がある。そして、造粒物は粉末に匹敵
する分散性を有し、射出成形の能率向上、品質の安定化
が達成される等の効果を奏する。
Since the granulated product of the present invention is a granulated product, it can be stably supplied without causing a shelving phenomenon in a molding machine hopper when compounded with a resin, and has good workability. Since the granules are mixed at a predetermined compounding ratio, the dispersion of the compounding ratio after molding is drastically reduced. In the production, the synthetic resin powder is not softened or melted, and the resin or filler is not subjected to heat history or shearing, so that granulation can be performed without deterioration, and a stirring granulator using water or an organic solvent as a dispersion medium. The solvent can be recovered because the granulation is carried out. Further, since water or an organic solvent is used, there is an advantage that it can be applied to both hydrophilic and hydrophobic materials. The granulated material has a dispersibility comparable to that of powder, and has effects such as improvement in efficiency of injection molding and stabilization of quality.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポリプロピレン、ナイロン、ポリスチレ
ン、ポリ塩化ビニルから選ばれる少なくとも1種の合成
樹脂粉末と粉末状無機質フィラーとを、前記合成樹脂粉
末を軟化又は溶融させないで混合して造粒して得られた
造粒物であって、該造粒物の粒径が0.1〜5mmであ
ることを特徴とする合成樹脂粉末とフィラーとの混合造
粒物。
1. Polypropylene, nylon, polystyrene
Down, and at least one synthetic resin powder and powdered inorganic filler selected from polyvinyl chloride, a granulated product obtained by granulation is mixed at not soften or melt the synthetic resin powder, A mixed granulated product of a synthetic resin powder and a filler, wherein the granulated product has a particle size of 0.1 to 5 mm.
【請求項2】 合成樹脂粉末と粉末状無機質フィラーと
を予め混合した後、水又は有機質溶媒又は両者の混合液
を分散媒として加え、攪拌型造粒機により造粒後、乾燥
することを特徴とする請求項1記載の合成樹脂粉末とフ
ィラーとの混合造粒物の製造方法。
2. A method comprising mixing a synthetic resin powder and a powdery inorganic filler in advance, adding water or an organic solvent or a mixed solution of both as a dispersion medium, granulating with a stirring granulator, and drying. A method for producing a mixed granulated product of a synthetic resin powder and a filler according to claim 1.
JP11932493A 1993-04-23 1993-04-23 Mixed granulated product of synthetic resin powder and filler and method for producing the same Expired - Fee Related JP3096374B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11932493A JP3096374B2 (en) 1993-04-23 1993-04-23 Mixed granulated product of synthetic resin powder and filler and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11932493A JP3096374B2 (en) 1993-04-23 1993-04-23 Mixed granulated product of synthetic resin powder and filler and method for producing the same

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JPH06320535A JPH06320535A (en) 1994-11-22
JP3096374B2 true JP3096374B2 (en) 2000-10-10

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EP1389514B2 (en) 2001-05-24 2015-11-04 Toray Industries, Inc. Tablet, process for producing the same, and molded article obtained therefrom

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