JPH0873770A - Granulated composition of inorganic powder for resin filling - Google Patents

Granulated composition of inorganic powder for resin filling

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Publication number
JPH0873770A
JPH0873770A JP23018794A JP23018794A JPH0873770A JP H0873770 A JPH0873770 A JP H0873770A JP 23018794 A JP23018794 A JP 23018794A JP 23018794 A JP23018794 A JP 23018794A JP H0873770 A JPH0873770 A JP H0873770A
Authority
JP
Japan
Prior art keywords
resin
powder
filling
inorganic powder
talc
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
Application number
JP23018794A
Other languages
Japanese (ja)
Inventor
Shigeaki Koike
重章 小池
Yutaka Mukai
豊 向井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eneos Corp
Original Assignee
Japan Energy Corp
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 Japan Energy Corp filed Critical Japan Energy Corp
Priority to JP23018794A priority Critical patent/JPH0873770A/en
Publication of JPH0873770A publication Critical patent/JPH0873770A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To improve the reinforcing effect and handleability of an inorg. powder for resin filling and prevent dusting of the powder by compounding it with a sodium alkanesulfonate and granulating the resulting compsn. CONSTITUTION: 100 pts.wt. inorg. powder for resin filling is compounded with 10--50 pts.wt. sodium alkanesulfonate and the resulting compsn. is granulated, The powder pref. comprises at least one powder selected from among talc, calcium carbonate, barium sulfate, mica. kaolin, titanium dioxide, silica, zeolite, and sepiolite and has an average particle size of 0.1-20μm. Sodium alkanesulfonate having a rather high softening point or m.p. and the number of carbon atoms of 11-18 is pref. For kneading and granulating the powder and the alkanesulfonate, a melt kneader such as an extruder or a pressure kneader usually used for melting and kneading a resin can be used.

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、樹脂充填用粉体の造粒
組成物に関するもので、本発明の造粒組成物は、加工・
成形温度が350℃以下の熱可塑性樹脂に対し、その機
械的、熱的特性を改良すると同時に、帯電防止機能を付
与する無機フィラーマスタバッチとして用いられる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granulation composition for resin-filling powder.
It is used as an inorganic filler masterbatch that imparts an antistatic function to a thermoplastic resin having a molding temperature of 350 ° C. or lower while improving its mechanical and thermal properties.

【0002】本発明の造粒組成物を配合した樹脂は、ほ
こり付着による汚れを嫌う家電部品、OA機器部品、自
動車部品用等の工業用部品、フィルム等や透明フィルム
の製造に利用できる。
The resin containing the granulating composition of the present invention can be used for producing industrial parts such as home electric appliance parts, OA equipment parts, automobile parts, etc., which are not susceptible to dirt due to dust adhesion, films and the like and transparent films.

【0003】[0003]

【従来の技術】樹脂充填用無機粉体は、樹脂の機械的物
性の改良や白色化、光沢の付与等のために樹脂に配合さ
れる。この配合は、一般には粉体のまま、押出機(単軸
押出機、二軸押出機等)に取り付けられたホッパーから
計量機を経由して供給し、押出機により溶融樹脂と混練
する手法がとられている。この配合に際して粉体を取扱
うとき、当然に粉立ちが生じ、作業環境の悪化や他の製
品等への汚染の問題が生じることから、取扱場所を制
限、隔離したり、自動化の工夫等により、作業環境の悪
化や製品等の汚染防止対策がとられている。さらに、ホ
ッパー内に無機粉体が残存し、無機粉体のグレードや種
類を変更して別の製品を製造するときには、変更毎にホ
ッパー内および供給ライン等の清掃が必要となる。大型
機では、ホッパー内に人が入り掃除し、大型機、小型機
を問わず、部分的に分解掃除等が必要であり、これらの
作業は生産性を低下させる大きな要因ともなっている。
また、粉体の場合、ホッパーからの供給の際、ホッパー
内で閉塞したり流動性が悪く、定量的に安定供給できな
い等、ハンドリング上の問題も有していた。
2. Description of the Related Art Inorganic powder for resin filling is blended with resin for the purpose of improving the mechanical properties of resin, whitening, and imparting gloss. This compound is generally supplied as a powder from a hopper attached to an extruder (single-screw extruder, twin-screw extruder, etc.) via a weighing machine, and kneaded with the molten resin by the extruder. It is taken. When handling powders during this blending, powdering naturally occurs, which causes problems such as deterioration of working environment and contamination of other products.Therefore, by restricting the handling place, isolating, or devising automation, Measures are taken to prevent work environment deterioration and product contamination. Further, when the inorganic powder remains in the hopper and the grade or type of the inorganic powder is changed to manufacture another product, the inside of the hopper, the supply line, and the like need to be cleaned after each change. In a large-sized machine, a person enters the hopper for cleaning, and disassembly and cleaning is required for both large-sized machines and small-sized machines, and these operations are also a major factor in reducing productivity.
Further, in the case of powder, there is a problem in handling such that the powder is clogged in the hopper when it is supplied from the hopper, the fluidity is poor, and the powder cannot be stably supplied quantitatively.

【0004】このために、従来は、無機粉体を樹脂に高
配合させたマスタバッチを使用することが行われてい
る。しかしながら、マスタバッチは使用する樹脂の種類
に合わせたベース樹脂を用いて調製されるため、異な
る、多種類の樹脂で使用する場合、それぞれの樹脂に合
わせたマスタバッチが必要である。したがって、マスタ
バッチを生産、販売する側においても、多品種のマスタ
バッチを揃えなければならず、しかも、このマスタバッ
チは希釈して用いるため、使用量が少なく、少量多品種
生産となり、単価コストが高いものとなっていた。
For this reason, conventionally, a master batch in which an inorganic powder is highly mixed with a resin is used. However, since the masterbatch is prepared by using the base resin according to the type of resin used, when using a large number of different resins, it is necessary to prepare a masterbatch for each resin. Therefore, even on the side that produces and sells master batches, it is necessary to prepare a wide variety of master batches. In addition, since this master batch is used by diluting it, it is used in small quantities, resulting in small-lot production of a wide variety of products, resulting in unit cost reduction. Was high.

【0005】異なる樹脂に共通して使用できるマスタバ
ッチができれば、生産、販売、消費のところで、在庫
量、単価コストの低減が可能となるので、このようなマ
スタバッチの開発が要請されていた。
If a masterbatch that can be commonly used for different resins is made, the stock quantity and unit cost can be reduced at the time of production, sale, and consumption, so that the development of such a masterbatch has been demanded.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記課題を解
決するもので、本発明の目的は、樹脂の種類を問わずに
使用できるマスタバッチであり、同時に、樹脂充填用無
機粉体の粉立ちを防止し、ハンドリング性を改良すると
ともに、生産性の向上および在庫の削減、単価コストの
低減にもつながる、樹脂充填用無機粉体の造粒組成物を
提供することにある。また、他の目的としては、少なく
とも樹脂充填用無機粉体の機能を損なわず、帯電防止機
能を付与する樹脂充填用無機粉体の造粒組成物を提供す
ることにある。
DISCLOSURE OF THE INVENTION The present invention is to solve the above problems, and an object of the present invention is to provide a masterbatch which can be used regardless of the type of resin, and at the same time, powder of inorganic powder for resin filling. It is an object of the present invention to provide a granulating composition of an inorganic powder for resin filling, which prevents standing and improves handling properties, and also leads to improvement of productivity, reduction of inventory, and reduction of unit cost. Another object is to provide a granulation composition of a resin-filling inorganic powder that imparts an antistatic function without impairing at least the function of the resin-filling inorganic powder.

【0007】[0007]

【課題を解決するための手段】本発明者らは、樹脂充填
用無機粉体の粉立ち防止方法について鋭意検討したとこ
ろ、アルカンスルホン酸ナトリウムをバインダーとして
当該充填用無機粉体を造粒することができ、この造粒組
成物を樹脂に配合すると、充填用無機粉体本来の補強材
等として機能を損うことなく、前記アルカンスルホン酸
ナトリウムが樹脂に対して帯電防止剤として作用するこ
とを見い出し本発明に到達したものである。
Means for Solving the Problems The inventors of the present invention have made extensive studies as to a method for preventing powdering of the inorganic powder for resin filling, and found that the inorganic powder for filling is granulated with sodium alkanesulfonate as a binder. When this granulation composition is blended with a resin, the sodium alkanesulfonate acts as an antistatic agent for the resin without impairing the function as the original reinforcing material of the inorganic powder for filling. The present invention has been found out.

【0008】本発明の樹脂充填用粉体の造粒組成物は、
樹脂充填用無機粉体100重量部にアルカンスルホン酸
ナトリウム10〜50重量部を配合して造粒したことよ
りなるもので、好ましくは、前記樹脂充填用無機粉体と
して、タルク、炭酸カルシウム、硫酸バリウム、マイ
カ、カオリン、二酸化チタン、シリカ、ゼオライト、セ
ピオライトから選らばれた1種または2種以上を用い、
またこれらの樹脂充填用無機粉体として平均粒径0.1
〜20ミクロンのものを用いることからなるものであ
る。
The granulating composition of the resin filling powder of the present invention is
It is composed by mixing 100 parts by weight of the inorganic powder for resin filling with 10 to 50 parts by weight of sodium alkanesulfonate and granulating. Preferably, the inorganic powder for resin filling is talc, calcium carbonate, sulfuric acid. Using one or more selected from barium, mica, kaolin, titanium dioxide, silica, zeolite, sepiolite,
The average particle size of these resin-filling inorganic powders is 0.1
.About.20 microns.

【0009】上記アルカンスルホン酸ナトリウムは、ノ
ルマルパラフィンをスルホン化して得られたもので、一
般に市販されているものをそのまま使用できるが、樹脂
と溶融混練される添加剤成分となることから、ある程度
軟化温度や融点が高い方が適し、炭素数が11〜18の
ものを用いることが好ましい。
The above-mentioned sodium alkanesulfonate is obtained by sulfonation of normal paraffin, and commercially available products can be used as they are, but since they become additive components to be melt-kneaded with a resin, they are softened to some extent. The higher the temperature and the higher the melting point, the more suitable it is, and it is preferable to use one having 11 to 18 carbon atoms.

【0010】本発明に使用される樹脂充填用無機粉体と
しては、樹脂の機械的、熱的特性を改良するために一般
に樹脂に添加、混合されている無機フィラーの粉体であ
れば、何れも支障なく用いることができる。この樹脂充
填用無機粉体としては、タルク、炭酸カルシウム、硫酸
バリウム、マイカ、ニ酸化チタン、シリカ等があげら
れ、それぞれ一般に市販されているものがそのまま使用
できる。
The resin-filling inorganic powder used in the present invention may be any inorganic filler powder which is generally added to and mixed with the resin in order to improve the mechanical and thermal properties of the resin. Can be used without any trouble. Examples of the inorganic powder for resin filling include talc, calcium carbonate, barium sulfate, mica, titanium dioxide, silica and the like, and those generally commercially available can be used as they are.

【0011】この樹脂充填用無機粉体は、平均粒径が
0.1〜20ミクロンのものを用いることが好ましい。
0.1ミクロン以下のものは、嵩密度が小さく、アルカ
ンスルホン酸ナトリウムとの混練、造粒が行ない難くな
り、20ミクロン以上のものは、樹脂の機械的物性の改
良や白色化、光沢の付与等の改質効果が得られ難くなる
傾向にある。
The resin-filling inorganic powder preferably has an average particle size of 0.1 to 20 μm.
Those with a particle size of 0.1 micron or less have a low bulk density, making it difficult to knead and granulate with sodium alkanesulfonate, and those with a particle size of 20 microns or more improve the mechanical properties of the resin, whiten, and impart gloss. It tends to be difficult to obtain the effect of modifying such as.

【0012】また、この樹脂充填用無機粉体とアルカン
スルホン酸ナトリウムとの配合割合は、樹脂充填用無機
粉体100重量部に対し、アルカンスルホン酸ナトリウ
ムを10〜50重量部、より好ましくは、10〜40重
量部配合するとよい。アルカンスルホン酸ナトリウムの
配合量を50重量部以上とすると、アルカンスルホン酸
ナトリウムが水分を吸収して軟化するため、造粒粒子同
士がくっつき塊状になったり、水分の吸収量が多くなる
ため樹脂に混練、配合した際、成形不良の原因になるこ
とから好ましくなく、また、アルカンスルホン酸ナトリ
ウムの配合量を10重量部以下とすると造粒性が悪くな
り好ましくない。
The blending ratio of the resin-filling inorganic powder and sodium alkane sulfonate is 10 to 50 parts by weight of sodium alkane sulfonate, more preferably 100 parts by weight of the resin-filling inorganic powder. It is recommended to add 10 to 40 parts by weight. When the blending amount of sodium alkane sulfonate is 50 parts by weight or more, sodium alkane sulfonate absorbs water and softens, so that granulated particles stick to each other and form lumps, or the amount of water absorbed increases, so When kneading and blending, it is not preferable because it causes defective molding, and when the blending amount of sodium alkanesulfonate is 10 parts by weight or less, the granulation property is deteriorated, which is not preferable.

【0013】アルカンスルホン酸ナトリウムと上記樹脂
充填用無機粉体との混練、造粒は、樹脂の溶融混練に一
般に利用されている押出機(単軸押出機、二軸押出機
等)や加圧ニーダー等の溶融混練機が使用できる。
The kneading and granulation of sodium alkanesulfonate and the above-mentioned resin-filling inorganic powder are carried out by an extruder (single-screw extruder, twin-screw extruder, etc.) generally used for melt-kneading a resin and pressurization. A melt kneader such as a kneader can be used.

【0014】アルカンスルホン酸ナトリウムと上記樹脂
充填用無機粉体を予備混合した後、混練機、押出機のホ
ッパーより一括投入して溶融混練した後、ストランドを
押出して空冷した後、ペレタイザーで造粒する方法ある
いは溶融混練機でまずアルカンスルホン酸ナトリウムを
溶融し、途中のホッパーより樹脂充填用無機粉体を投入
して混練した後、ストランドを押出して空冷した後、ペ
レタイザーで造粒する方法が採用できる。
After preliminarily mixing sodium alkanesulfonate and the above-mentioned resin-filling inorganic powder, they are collectively charged from a hopper of a kneader or an extruder and melt-kneaded, and then a strand is extruded and air-cooled, and then granulated by a pelletizer. Or a method in which sodium alkane sulfonate is first melted with a melt kneader, inorganic powder for resin filling is added from the hopper in the middle and kneaded, then the strands are extruded and air cooled, and then granulated with a pelletizer. it can.

【0015】このようにして得られる樹脂充填用無機粉
体の造粒組成物は、アルカンスルホン酸ナトリウムの熱
的安定性の問題から成形、加工温度が350℃以下とい
う制限は有るが、あらゆる種類の樹脂に配合することが
でき、その樹脂の機械的、熱的特性を改良することがで
きる。
The granulating composition of the resin-filling inorganic powder thus obtained has a limitation that the molding and processing temperature is 350 ° C. or less due to the problem of thermal stability of sodium alkanesulfonate, but all kinds are possible. It is possible to improve the mechanical and thermal properties of the resin.

【0016】[0016]

【実施例】【Example】

(実施例1)平均粒径10μmのタルク〔日本タルク
(株)製、MS-P〕60重量部とアルカンスルホン酸ナ
トリウム〔日鉱石油化学(株)製、SAS195〕40重
量部をスーパーミキサー〔カワタ(株)製、SM−V−2
0型〕を用いて予備混合した後、加圧ニーダー(森山製
作所製、DS1−5MHB−E)により溶融混練し、続
いて押出造粒機(森山製作所製、PR−3600)によ
り押出し、空冷した後、ペレット化して3〜5mmの造粒
タルクを得た。
(Example 1) Talc having an average particle size of 10 μm [Japan Talc
Co., Ltd., MS-P] 60 parts by weight and sodium alkane sulfonate [Nippon Petrochemical Co., Ltd., SAS195] 40 parts by weight are mixed with a super mixer [Kawata Co., Ltd., SM-V-2].
0 type], followed by melt kneading with a pressure kneader (manufactured by Moriyama Seisakusho, DS1-5MHB-E), subsequently extruded by an extrusion granulator (Moriyama Seisakusho, PR-3600), and air-cooled. Then, it was pelletized to obtain granulated talc having a size of 3 to 5 mm.

【0017】得られた造粒タルクをポリ袋に約1kg採取
して約10回振ってポリ袋の中を観察したが、粉立ちは
見られなかった。
About 1 kg of the obtained granulated talc was collected in a plastic bag and shaken about 10 times to observe the inside of the plastic bag, but no dusting was observed.

【0018】(実施例2)実施例1で用いたのと同じタ
ルクとアルカンスルホン酸ナトリウムを用い、配合量を
80重量部と20重量部とした以外は、実施例1と同じ
方法で造粒タルクを得た。
(Example 2) Granulation was carried out in the same manner as in Example 1 except that the same talc and sodium alkanesulfonate as used in Example 1 were used and the compounding amounts were 80 parts by weight and 20 parts by weight. Got talc.

【0019】得られた造粒タルクをポリ袋に約1kg採取
して約10回振ってポリ袋の中を観察したが、粉立ちは
見られなかった。
About 1 kg of the obtained granulated talc was collected in a plastic bag and shaken about 10 times to observe the inside of the plastic bag, but no dusting was observed.

【0020】(実施例3)粒径1〜5μmの炭酸カルシ
ウム〔丸尾カルシウム(株)製、スーパーS〕80重量部
と実施例1で用いたアルカンスルホン酸ナトリウム20
重量部を用いて、実施例1と同じ方法で造粒炭酸カルシ
ウムを得た。
Example 3 80 parts by weight of calcium carbonate having a particle size of 1 to 5 μm (Super S manufactured by Maruo Calcium Co., Ltd.) and sodium alkanesulfonate used in Example 1 20
Granulated calcium carbonate was obtained in the same manner as in Example 1 using parts by weight.

【0021】得られた造粒炭酸カルシウムをポリ袋に約
1kg採取して約10回振ってポリ袋の中を観察したが、
粉立ちは見られなかった。
About 1 kg of the obtained granulated calcium carbonate was collected in a plastic bag and shaken about 10 times to observe the inside of the plastic bag.
No dusting was seen.

【0022】(実施例4)平均粒径約0.6μmの硫酸バ
リウム〔日本化学工業(株)製、UD〕80重量部と実施
例1で用いたアルカンスルホン酸ナトリウム20重量部
を用いて、実施例1と同じ方法で造粒硫酸バリウムを得
た。
Example 4 Using 80 parts by weight of barium sulfate (UD, manufactured by Nippon Kagaku Kogyo Co., Ltd.) having an average particle size of about 0.6 μm and 20 parts by weight of sodium alkanesulfonate used in Example 1, Granulated barium sulfate was obtained in the same manner as in Example 1.

【0023】得られた造粒硫酸バリウムをポリ袋に約1
kg採取して約10回振ってポリ袋の中を観察したが、粉
立ちは見られなかった。
About 1 part of the obtained granulated barium sulfate was placed in a plastic bag.
Although kg was collected and shaken about 10 times to observe the inside of the plastic bag, no dusting was observed.

【0024】(実施例5)実施例1で得た造粒タルクを
ポリプロピレンペレット(三菱化成(株)製、4700J
G)とタルクの濃度が10および20重量%になるよう
に予備混合した後、連続混練機(KCK製、70−22
VEX型)により混練押出してペレット化し、タルク強
化ポリプロピレンを得た。
Example 5 The granulated talc obtained in Example 1 was converted into polypropylene pellets (4700J manufactured by Mitsubishi Kasei Co., Ltd.).
G) and talc were pre-mixed so that the concentrations thereof were 10 and 20% by weight, and then a continuous kneader (made by KCK, 70-22
Vex type) was kneaded and extruded into pellets to obtain talc-reinforced polypropylene.

【0025】得られたタルク強化ペレットを、射出成形
機〔山城精機(株)製、SVA−60−52型〕により、
試験片に射出成形した。射出成形して得た試験片を用い
て、曲げ弾性率、荷重たわみ温度(0.45MPa)、
表面抵抗率を測定した。測定結果を表1に示した。
The obtained talc-reinforced pellets were processed by an injection molding machine [Yamashiro Seiki Co., Ltd., SVA-60-52 type].
The test piece was injection molded. Using a test piece obtained by injection molding, flexural modulus, deflection temperature under load (0.45 MPa),
The surface resistivity was measured. The measurement results are shown in Table 1.

【0026】(実施例6)実施例2で得た造粒タルクを
実施例5で用いたポリプロピレンペレットとタルクの濃
度が10および20重量%になるように予備混合した
後、実施例5と同じ方法でペレット化し、得られたタル
ク強化ペレットを試験片に射出成形した。射出成形して
得た試験片を用いて、曲げ弾性率、荷重たわみ温度、表
面抵抗率を測定した。測定結果を表1に示した。
(Example 6) The granulated talc obtained in Example 2 was premixed with the polypropylene pellets used in Example 5 so that the concentrations of talc were 10 and 20% by weight, and then the same as in Example 5. The talc-reinforced pellets obtained were pelletized by the method and injection-molded into test pieces. Bending elastic modulus, deflection temperature under load, and surface resistivity were measured using a test piece obtained by injection molding. The measurement results are shown in Table 1.

【0027】(実施例7)実施例2で得た造粒タルクを
PETペレット(帝人製 TR−4550BHK)とタ
ルクの濃度が10および20重量%になるように予備混
合した後、実施例5と同じ方法でペレット化し、得られ
たタルク強化ペレットを試験片に射出成形した。射出成
形して得た試験片を用いて、曲げ弾性率、荷重たわみ温
度、表面抵抗率を測定した。測定結果を表1に示した。
(Example 7) The granulated talc obtained in Example 2 was premixed with PET pellets (TR-4550BHK manufactured by Teijin Ltd.) so that the concentration of talc was 10 and 20% by weight, and then, as in Example 5. The pellets were pelletized in the same manner and the resulting talc reinforced pellets were injection molded into test pieces. Bending elastic modulus, deflection temperature under load, and surface resistivity were measured using a test piece obtained by injection molding. The measurement results are shown in Table 1.

【0028】(実施例8)実施例3で得た造粒炭酸カル
シウムを実施例5で用いたポリプロピレンペレットと炭
酸カルシウムの濃度が10および20重量%になるよう
に予備混合した後、実施例5と同じ方法でペレット化
し、得られた炭酸カルシウム配合ペレットを試験片に射
出成形した。射出成形して得た試験片を用いて、曲げ弾
性率、荷重たわみ温度、表面抵抗率を測定した。測定結
果を表1に示した。
Example 8 The granulated calcium carbonate obtained in Example 3 was premixed with the polypropylene pellets used in Example 5 so that the concentration of calcium carbonate was 10 and 20% by weight, and then Example 5 The pellets were pelletized in the same manner as above, and the resulting pellets containing calcium carbonate were injection-molded into test pieces. Bending elastic modulus, deflection temperature under load, and surface resistivity were measured using a test piece obtained by injection molding. The measurement results are shown in Table 1.

【0029】(実施例9)実施例4で得た造粒硫酸バリ
ウムを実施例5で用いたポリプロピレンペレットと硫酸
バリウムの濃度が10および20重量%になるように予
備混合した後、実施例5と同じ方法でペレット化し、得
られた硫酸バリウム配合ペレットを試験片に射出成形し
た。射出成形して得た試験片を用いて、曲げ弾性率、荷
重たわみ温度、表面抵抗率を測定した。測定結果を表1
に示した。
Example 9 The granulated barium sulfate obtained in Example 4 was premixed with the polypropylene pellets used in Example 5 so that the concentration of barium sulfate was 10 and 20% by weight, and then Example 5 was used. The barium sulfate-containing pellets obtained were pelletized by the same method as described above, and the obtained pellets were injection-molded. Bending elastic modulus, deflection temperature under load, and surface resistivity were measured using a test piece obtained by injection molding. Table 1 shows the measurement results
It was shown to.

【0030】(比較例1)実施例2においてアルカンス
ルホン酸ナトリウムのかわりに低分子量PE(三洋化成
工業品 130−P)を用いて得られたマスタバッチを
PPと混合、成形し同様に試験した。
Comparative Example 1 A master batch obtained by using low molecular weight PE (Sanyo Kasei Kogyo 130-P) in place of sodium alkanesulfonate in Example 2 was mixed with PP, molded and tested in the same manner. .

【0031】[0031]

【表1】 [Table 1]

【0032】[0032]

【発明の効果】樹脂充填用無機粉体をアルカンスルホン
酸ナトリウムでペレット化することにより、従来の低分
子量PEを用いたマスタバッチよりも高い補強効果を発
現し、粉立ちが防止でき、取扱性に優れた造粒組成物を
得た。さらに、これらの造粒組成物は、成形、加工温度
が350℃以下の全ての樹脂について共通して使用でき
ることから、在庫量の削減、単価コストの低減を図るこ
とができる。
EFFECTS OF THE INVENTION By pelletizing the inorganic powder for resin filling with sodium alkanesulfonate, a higher reinforcing effect than that of the conventional master batch using low molecular weight PE can be exhibited, powdering can be prevented, and handleability is improved. An excellent granulation composition was obtained. Furthermore, since these granulation compositions can be commonly used for all resins having a molding and processing temperature of 350 ° C. or less, it is possible to reduce the stock amount and the unit cost.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 樹脂充填用無機粉体100重量部にアル
カンスルホン酸ナトリウム10〜50重量部を配合して
造粒したことよりなる樹脂充填用粉体の造粒組成物。
1. A granulation composition of a resin-filling powder, which comprises mixing 100 parts by weight of an inorganic powder for resin-filling with 10 to 50 parts by weight of sodium alkanesulfonate and granulating.
【請求項2】 請求項1の樹脂充填用無機粉体として、
タルク、炭酸カルシウム、硫酸バリウム、マイカ、カオ
リン、二酸化チタン、シリカ、ゼオライト、セピオライ
トから選らばれた1種または2種以上を用いることを特
徴とする樹脂充填用粉体の造粒組成物。
2. The resin-filling inorganic powder according to claim 1,
A granulating composition for a resin-filling powder, which comprises using one or more selected from talc, calcium carbonate, barium sulfate, mica, kaolin, titanium dioxide, silica, zeolite, and sepiolite.
【請求項3】 請求項1の樹脂充填用無機粉体が平均粒
径0.1〜20ミクロンのものであることを特徴とする
樹脂充填用粉体の造粒組成物。
3. A granulation composition for resin-filling powder, wherein the resin-filling inorganic powder according to claim 1 has an average particle size of 0.1 to 20 μm.
JP23018794A 1994-09-01 1994-09-01 Granulated composition of inorganic powder for resin filling Pending JPH0873770A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23018794A JPH0873770A (en) 1994-09-01 1994-09-01 Granulated composition of inorganic powder for resin filling

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23018794A JPH0873770A (en) 1994-09-01 1994-09-01 Granulated composition of inorganic powder for resin filling

Publications (1)

Publication Number Publication Date
JPH0873770A true JPH0873770A (en) 1996-03-19

Family

ID=16903961

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23018794A Pending JPH0873770A (en) 1994-09-01 1994-09-01 Granulated composition of inorganic powder for resin filling

Country Status (1)

Country Link
JP (1) JPH0873770A (en)

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