JPS59122535A - Preparation of concentrated thermoplastic resin composition containing inorganic filler - Google Patents

Preparation of concentrated thermoplastic resin composition containing inorganic filler

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Publication number
JPS59122535A
JPS59122535A JP23454482A JP23454482A JPS59122535A JP S59122535 A JPS59122535 A JP S59122535A JP 23454482 A JP23454482 A JP 23454482A JP 23454482 A JP23454482 A JP 23454482A JP S59122535 A JPS59122535 A JP S59122535A
Authority
JP
Japan
Prior art keywords
inorganic filler
monomer
fibrous
weight
parts
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
JP23454482A
Other languages
Japanese (ja)
Inventor
Takeshi Yamamoto
健 山本
Minoru Uchida
実 内田
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.)
Mitsubishi Kasei Polytec Co
Original Assignee
Mitsubishi Monsanto Chemical Co
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 Mitsubishi Monsanto Chemical Co filed Critical Mitsubishi Monsanto Chemical Co
Priority to JP23454482A priority Critical patent/JPS59122535A/en
Publication of JPS59122535A publication Critical patent/JPS59122535A/en
Pending legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polymerisation Methods In General (AREA)

Abstract

PURPOSE:To prevent the formation of a resin containing only non-fibrous material, and to obtain a concentrated composition in high yield, by carrying out the suspension polymerization of an aromatic vinyl monomer in the presence of a mixture of non-fibrous and fibrous inorganic fillers which are surface-treated with an organic titanate compound. CONSTITUTION:100pts.wt. of an aromatic vinyl monomer or a mixture of the monomer and a monomer copolymerizable therewith is suspended in water together with 5-800pts.wt. of a mixture composed of 0.5-60wt% of a non-fibrous inorganic filler surface-treated with an organic titanate compound (0.01-2pts.wt. per 100pts.wt. of the filler) and 99.5-40wt% of a fibrous inorganic filler, and the monomer is polymerized. The non-fibrous filler is alumina, silica, etc. having an average particle diameter of 1-800mum, and the fibrous filler is glass fiber, etc., preferably strands obtained by collecting 100-several thousands fibers each having a diameter of <=20mum and cutting to a length of 1-15mm..

Description

【発明の詳細な説明】 本発明は、繊維状及び非繊維状の無機充填材を高濃度で
含有する無機充填材を含有する熱可塑性樹脂濃厚組成物
(以下「コンセントレート」という。)の製造方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the production of a concentrated thermoplastic resin composition containing an inorganic filler (hereinafter referred to as "concentrate") containing a high concentration of fibrous and non-fibrous inorganic fillers. Regarding the method.

熱可塑性樹脂に、ガラス繊維、炭素繊維等の無機繊維全
配合してなる組成物は成形が容易であシ、かつ、耐衝撃
性、寸法安定性等機械的性質が優れているので、各種の
構造部品、機能部品の材料として用いられている。
Compositions made of thermoplastic resins and inorganic fibers such as glass fibers and carbon fibers are easy to mold and have excellent mechanical properties such as impact resistance and dimensional stability. It is used as a material for structural and functional parts.

しかしながら、このような繊維強化熱可塑性樹脂は、成
形品の表面に繊維が浮き出て表面外観を劣化させること
、繊維の配向を生じやすく、それにともなって、機械的
性質に異方性が生じること等の問題点があった。
However, such fiber-reinforced thermoplastic resins tend to cause fibers to protrude on the surface of the molded product, deteriorating the surface appearance, and tend to cause fiber orientation, resulting in anisotropy in mechanical properties. There was a problem.

これらの問題点を解決するために、通常は、非繊維状の
無機充填材、例えは、メルク、ミルドファイバー等全添
加することが知られていた。
In order to solve these problems, it has been known that non-fibrous inorganic fillers such as Merck and milled fibers are generally added.

ら これ・繊維状、非繊維状の無機充填材の所要量を熱可塑
性樹脂に直接添加、混練するのは、該充填材の飛散、押
出機の閉塞摩耗等を生じ、かつ、均一に分散しない等の
問題が生じるので、本出願人の出願に係る特願昭j、t
−/ざ4/、77号明細書に記載されているように無機
充填材の共存下゛に芳香族ビニル単量体等を懸濁重合さ
せる方法等が提案されていた。この方法では、繊維状無
機充填材の周囲に非繊維状無機充填材及び熱可塑性樹脂
が固着したペレットが得られるが、重合系に加える非繊
維状無機充填材の量が堆加すると、上記ペレットに含ま
れない粉末状の非繊維状無機充填材含有熱可塑性樹脂が
生成し、所望のペレット状組成物の収率低下、後処理の
複雑化等の問題点があった。
Directly adding and kneading the required amount of fibrous or non-fibrous inorganic fillers to a thermoplastic resin will cause scattering of the fillers, clogging wear of the extruder, etc., and will not be uniformly dispersed. Problems such as these arise, so the patent application filed by the applicant should be
As described in Japanese Patent No. 4/77, a method has been proposed in which aromatic vinyl monomers and the like are subjected to suspension polymerization in the coexistence of an inorganic filler. In this method, pellets in which the non-fibrous inorganic filler and thermoplastic resin are fixed around the fibrous inorganic filler are obtained, but when the amount of the non-fibrous inorganic filler added to the polymerization system is deposited, the pellets become Powdered non-fibrous inorganic filler-containing thermoplastic resin that is not included in the process is produced, resulting in problems such as a decrease in the yield of the desired pellet-like composition and complication of post-processing.

本発明者等は、上記の問題点を有しないコンセントレー
トの製造方法を開発することFlffl的として、鋭意
研究を重ねた結果、本発明に到達したものである。
The present inventors have conducted intensive research to develop a method for producing a concentrate that does not have the above-mentioned problems, and have arrived at the present invention.

本発明の上記の目的は芳香族ビニル単量体、または芳香
族ビニル単量体及びこれと共重合可能な単量体からなる
単量体混合物を無機充填材□ の共存下に懸濁重合させ
てコンセントレートラ製造する方法において、上記単量
体、または、単量体混合物700重量部を有機チタネー
ト化合物によって表面処理された非繊維状無機充填材0
.t〜60重量係重量繊維状無機充填材99.j〜yo
重量%からなる無機充填材混合物l〜と00重量部とと
もに、700〜3000重量部の水中に懸濁させて重合
することにょシ達せられる。
The above object of the present invention is to carry out suspension polymerization of an aromatic vinyl monomer or a monomer mixture consisting of an aromatic vinyl monomer and a monomer copolymerizable therewith in the coexistence of an inorganic filler. In the method for producing a concentrate, 700 parts by weight of the above monomer or monomer mixture is mixed with 0 parts by weight of a non-fibrous inorganic filler surface-treated with an organic titanate compound.
.. t~60 weight ratio fibrous inorganic filler 99. j〜yo
An inorganic filler mixture consisting of l~ and 00 parts by weight is suspended and polymerized in 700 to 3000 parts by weight of water.

本発明に用いられる有機チタネート化合物としてハRo
   O:Rなる分子式を有する単核化\T1/ 合物、これらの単核化合物が皿座配位子による橋かけ結
合により結合した複核化合物、例えにI なる構造式を有する化合物が用いられる。
The organic titanate compound used in the present invention is Ro
A mononuclear \T1/ compound having the molecular formula O:R, a dinuclear compound in which these mononuclear compounds are bonded by a crosslinking bond using a dish ligand, for example, a compound having the structural formula I are used.

上記各式に用いられる置換基RとしてはH2OH3−、
C,、H5−、n−03H7−、i−晒−、n−、V 
e c−04H9−等のアルキル基、H2NC2へNH
C2A−9H2N−00 0000 5O2−等のスルホニル基、C6H5,1−03H50
6H4C6H,−、0H306H4−等の芳香族基、(
OnH,拳@* 0) 24            
                      2゜ヤ
The substituent R used in each of the above formulas is H2OH3-,
C,, H5-, n-03H7-, i-bleached-, n-, V
e alkyl group such as c-04H9-, NH to H2NC2
Sulfonyl group such as C2A-9H2N-00 0000 5O2-, C6H5,1-03H50
Aromatic groups such as 6H4C6H,-, 0H306H4-, (
OnH, fist @* 0) 24
2 degrees.

P−(/≦n≦20 ) 、 ArO−o−(Ar:芳
香族基)等111 0                     0の二
置換ホスフェート基、 OO ホスフェート基、(CaH2n+10 )2 F  (
/≦n≦、、zo)等のホスファイト基及び)(2Q=
CH2等が例示される。
P-(/≦n≦20), ArO-o-(Ar: aromatic group), etc. 11100 disubstituted phosphate group, OO phosphate group, (CaH2n+10)2F (
Phosphite groups such as /≦n≦,,zo) and )(2Q=
CH2 etc. are exemplified.

    0 ロホスフエート基、C,1H2n+、opQ等のホスフ
ァイト基等が例示される。
Examples include phosphite groups such as 0 lophosphate group, C, 1H2n+, and opQ.

置換基R及びR′は一種のチタネート化合物中において
全て同一である必要はなく適宜組合せて用いてよい。
The substituents R and R' do not need to be all the same in one type of titanate compound, and may be used in any combination as appropriate.

例えば、(1−03H,O) (n−017H35C−
0)3Ti 。
For example, (1-03H,O) (n-017H35C-
0)3Ti.

1 (1−C3H50) (CsyHxs C−0)3”’
 、 (1−c3H5o)1 0            0 ((C8H17)2 ” ’ )s Ti等が挙げられ
る。
1 (1-C3H50) (CsyHxs C-0)3”'
, (1-c3H5o)100((C8H17)2'')sTi, and the like.

1 また、非繊維状無機充填材としては、平均粒径が/〜と
00μm 程のアルミナ、シリカ、カオリン、クレー、
タルク、マイカ、珪酸カルシウム、炭酸カルシウム、酸
化マグネシウム、石英粉、長石粉、ガラスミルドファイ
バー、ガラスフレーク、ガラスピーズ等が例示される。
1 In addition, as non-fibrous inorganic fillers, alumina, silica, kaolin, clay, with an average particle size of about 00 μm,
Examples include talc, mica, calcium silicate, calcium carbonate, magnesium oxide, quartz powder, feldspar powder, glass milled fiber, glass flakes, and glass peas.

繊維状無機充填材としては、ガラス繊維、炭素繊維等が
好ましく、特に直径が2oμm以下2のこれらの繊維が
/りO〜数千本集束したストランドを、/〜/夕欄の長
さに切断したチョツプドストランド(choppea 
5trana )が°好ましい。
As the fibrous inorganic filler, glass fibers, carbon fibers, etc. are preferable, and in particular, a strand of several thousand of these fibers with a diameter of 2 μm or less is cut into a length of /~/. chopped strands (choppea)
5trana) is preferred.

非繊維状無機充填材を有機チタネート化合物で表面処理
するには、V型混合機、ヘンシェルミキサ、リボンプレ
ンダー等により非繊維状無機充填材を攪拌しながら所要
量の有機チタネート化合物を添加する方法、あるいは、
所要量の有機チタネート化合物をヘキサン、ヘプタン、
トルエン等の溶剤に所要量溶解して添加する方法等があ
る。
In order to surface-treat the non-fibrous inorganic filler with an organic titanate compound, the required amount of the organic titanate compound is added while stirring the non-fibrous inorganic filler using a V-type mixer, Henschel mixer, ribbon blender, etc. ,or,
Add the required amount of organic titanate compound to hexane, heptane,
There is a method in which the required amount is dissolved in a solvent such as toluene and added.

有機チタネート化合物の使用量は非繊維状無機充填材1
00重量部に対して0.01〜j重量部が好ましく、0
.07〜コ重量部がより好ましい0 使用量がo、oot重量部未満では効果がなく、夕重量
部を超えた場合特に不都合はないが、8本発明の効・果
が顕著には向上しないので不経済である。
The amount of organic titanate compound used is 1% of the non-fibrous inorganic filler.
It is preferably 0.01 to j parts by weight per 00 parts by weight, and
.. Parts by weight of 0 to 0 are more preferred. If the amount used is less than 0 or 0 parts by weight, there will be no effect, and if it exceeds 0 parts by weight, there will be no particular disadvantage, but 8 the effects and effects of the present invention will not be significantly improved. It is uneconomical.

なお、繊維状無機充填材は、ビニルグリシジル化合物、
シラン系カップリング剤等により、予じめ、表面処理さ
れている場合が通常であるので、本発、明方法に基づい
て有機チタネート化合物によシ処理するのは、非繊維状
無機充填材のみで十分であるが、予じめ表面処理がされ
ていない繊維状無機充填材を用いる場合は、有機チタネ
ート化合物処理を行なうのが好ましい。
In addition, the fibrous inorganic filler is a vinyl glycidyl compound,
Since the surface is usually previously treated with a silane coupling agent, etc., only non-fibrous inorganic fillers are treated with organic titanate compounds based on the method of the present invention. However, when using a fibrous inorganic filler that has not been surface-treated in advance, it is preferable to perform an organic titanate compound treatment.

本発明に係るコンセントレートを製造するにあたっては
、非繊維状無機充填材0.夕〜30重量係、及び残部、
すなわち、993タ〜グθ重量係が繊維状無機充填材か
らなる無機充填材混合物を、芳香族ビニル単量体、また
は、芳香族ビニル単量体及びこれと共重合可能な単量体
からなる単量体混合物700重量部に対して5〜200
重量部に相当する量となるように、上記単量体、または
、単量体混合物とともに、100〜3000重量部の水
中に懸濁させて、上記単量体、または、単量体混合物を
重合させる。
In manufacturing the concentrate according to the present invention, a non-fibrous inorganic filler of 0. Evening ~ 30 weight section and the rest,
That is, an inorganic filler mixture consisting of a fibrous inorganic filler with a 993 tag to θ weight ratio consisting of an aromatic vinyl monomer, or an aromatic vinyl monomer and a monomer copolymerizable therewith. 5 to 200 parts by weight of monomer mixture
Polymerize the monomer or monomer mixture by suspending it in 100 to 3000 parts by weight of water together with the monomer or monomer mixture in an amount corresponding to parts by weight. let

無機充填材混合物は、o、t−to重重量の非繊維状無
機充填材を含むのが適当であり 、”−’重量部未満で
あれば添加した効果は殆ど発揮さrL  7i:  い
 。
Suitably, the inorganic filler mixture contains o,t-to-weight of the non-fibrous inorganic filler, and if the amount is less than "-" parts by weight, the effect of the addition is almost negligible.

また、60重量%全超える量であると、得られたコンセ
ントレートがペレット状とならない。
Moreover, if the amount exceeds 60% by weight, the obtained concentrate will not become pellet-like.

無機充填材混合物の量が!重量部未満では、添加した効
果がなく、ざ00重量部を超えると、樹脂量が相対的に
少なくなシ、充填材を結束できなくなるので適当でない
The amount of inorganic filler mixture! If the amount is less than 100 parts by weight, there is no effect, and if it exceeds 00 parts by weight, the amount of resin is relatively small and the filler cannot be bound, so it is not suitable.

芳香族ビニル単量体としては、スチレン、α−メチルス
チレン、ビニルトルエン、α−ビニルナフタレン等の芳
香族環にビニル基が直接結合した単量体が挙げられる。
Examples of aromatic vinyl monomers include monomers in which a vinyl group is directly bonded to an aromatic ring, such as styrene, α-methylstyrene, vinyltoluene, and α-vinylnaphthalene.

また、芳香族ビニル単量体と共重合可能な単量体として
は、アクリロニトリル、メタクリレートリル、メチルア
クリレート、メチルメタクリレート、その他アクリル酸
又はメタクリル酸のアルキルエステル類が挙げられる。
Examples of monomers copolymerizable with the aromatic vinyl monomer include acrylonitrile, methacrylate, methyl acrylate, methyl methacrylate, and other alkyl esters of acrylic acid or methacrylic acid.

水の量は、上記単量体、または、単量体混合物700重
量部に対して700〜30θθ重量部が適当である。1
00重量部未満であれば攪拌が困難であり、また重合反
応の制御が容易でなくなる。水の量が3000重量部を
超えると、重合装置が大規模となるので不経済となる。
The appropriate amount of water is 700 to 30 parts by weight based on 700 parts by weight of the monomer or monomer mixture. 1
If the amount is less than 0.00 parts by weight, stirring will be difficult and the polymerization reaction will not be easily controlled. If the amount of water exceeds 3000 parts by weight, the polymerization apparatus will be large-scale and therefore uneconomical.

上記単量体等を懸濁させるには、ポリビニルアルコール
、ポリアクリルアミド、ゼラチンその他の粘 通常用いられる・濁安定剤を用いるのが好ましい0 重合反応は、熱重合、または通常のラジカル号明細書に
記載した方法により行なわれる。
In order to suspend the above monomers, etc., it is preferable to use polyvinyl alcohol, polyacrylamide, gelatin, or other commonly used viscosity stabilizers. It is carried out according to the method described.

本発明方法によると、従来技術による場合に比較して、
高濃度に非繊維状無機充填材を含有するコンセントレー
トか収率よく得られるので、このコンセントレート全ポ
リスチレン、ASm脂、ポリエステル等と配合した場合
に、成型品の外観、強度等の異方性か著しく改善された
According to the method of the present invention, compared to the case according to the prior art,
Concentrates containing a high concentration of non-fibrous inorganic fillers can be obtained in good yields, so when this concentrate is blended with all polystyrene, ASm resin, polyester, etc., it is possible to improve the anisotropy of the appearance, strength, etc. of molded products. or significantly improved.

また、重合にあたっても、非繊維状無機充填材の大部分
が、繊維状無機充填材のチョツプドストランドを中心と
してペレットを形成したコンセントレート中に含まれ、
粉末状の残渣が著しく減少する。したがって、重合終了
後の処理が容易となる。
In addition, during polymerization, most of the non-fibrous inorganic filler is contained in a concentrate formed into pellets centered on chopped strands of the fibrous inorganic filler.
Powdery residue is significantly reduced. Therefore, processing after completion of polymerization becomes easy.

次に、実施例及び比較例に基づいて本発明方法をさらに
具体的に説明する。
Next, the method of the present invention will be explained in more detail based on Examples and Comparative Examples.

実施例/〜グ 攪拌装置、冷却器、窒素ガス吹込口、温度計等を備えた
!tガラス製反応器に懸濁剤を溶解したイオン交換水、
及びに2S04を仕込んだ。続いて、ガラス繊維チョツ
プドストランド、非繊維状無機充填材として有機チタネ
ート化合物で表面処理した重質炭酸カルシウム(丸尾カ
ルシウム■製)、スチレン(第1表及び第一′表で「M
s、R−/Jと表示する。)、アクリロニトリル、開始
剤(ベンゾイルバーオキシト、BPO)、分子量調節剤
(テルピノレン)、酸化防止剤全仕込み反応器内全窒素
置換した後昇温した0反応器内の温度がと0℃に達した
後/、!時間の間にスチレン(第1表及び第2表で「M
SR−Ω」と表斥丁乙。)を連続添加した。反応終了後
未反L6.モノマーをストリッピングで除去した。生成
物ff:3.2メツシユの金網上でr・水洗した。
Example/~Equipped with a stirrer, cooler, nitrogen gas inlet, thermometer, etc.! Ion-exchanged water with a suspending agent dissolved in a glass reactor,
and 2S04 was added. Next, chopped glass fiber strands, heavy calcium carbonate (manufactured by Maruo Calcium ■) surface-treated with an organic titanate compound as a non-fibrous inorganic filler, and styrene ("M" in Tables 1 and 1') were used.
s, R-/J. ), acrylonitrile, initiator (benzoyl peroxide, BPO), molecular weight modifier (terpinolene), and antioxidant were all charged in the reactor.The temperature in the reactor rose to 0°C after replacing the entire reactor with nitrogen. After that/! Styrene ("M" in Tables 1 and 2)
SR-Ω,” said Omotesou Choitsu. ) was added continuously. After completion of the reaction, L6. Monomer was removed by stripping. Product ff: Washed with water on a 3.2 mesh wire mesh.

洗浄水をp紙によシル別し、残廣全得た。得られた残渣
は、殆どが重炭酸カルシウムであった。
The washing water was filtered through P paper to obtain all the residue. The resulting residue was mostly calcium bicarbonate.

その他の反応条件、及び結果を第1表に示す。Other reaction conditions and results are shown in Table 1.

比較例/、Ω 重質炭酸カルシウムを予じめ表面処理することなく用い
たこと以外は実質例と同様にして反応させた。反応条件
及び結果は第1表に示す。
Comparative Example/Ω A reaction was carried out in substantially the same manner as in the Example except that heavy calcium carbonate was used without surface treatment in advance. The reaction conditions and results are shown in Table 1.

実施例J 非繊維状無機充填材として刀−ボンミルドファイ〉(直
往/’ μmN長さ700 μm ) f用いた。反応
条件及び結果を第−表に示す。
Example J As a non-fibrous inorganic filler, katanabonmildophi (direct/'μmN length 700 μm) was used. The reaction conditions and results are shown in Table 1.

比較例3 カーボンミルドファイバーの表面処理をしなかったこと
以外は実施例!と同様にして反応させた。
Comparative Example 3 Example except that the surface treatment of carbon milled fiber was not performed! The reaction was carried out in the same manner.

反応条件及び結果を第2表に示す。The reaction conditions and results are shown in Table 2.

実施例g 非繊維状無機充填材としてウオラストナイト(Gグレー
ド)を用いた。反応条件及び結果を第2表に示す。
Example g Wollastonite (G grade) was used as a non-fibrous inorganic filler. The reaction conditions and results are shown in Table 2.

比較例グ ウオラストナイトの表面処理を行なわな一/J−った魚
身外は実施例とと同様にして反応を行なった0 反応条件及び結果を第2表に示す。
COMPARATIVE EXAMPLE A reaction was carried out in the same manner as in the example except for the fish flesh, which was not subjected to any surface treatment.The reaction conditions and results are shown in Table 2.

ユ)ポリアクリル酸系懸濁剤 2)ポリビニルアルコール、日本合成化学■製3)  
(i−C3H50)(n−C,□H35G −0−)3
Tiで表面処1 理(炭酸カルシウム700重量当り7重量部使用)  
     CH3 00 で表面処理(炭酸カルシウム700重量当り7重量部使
用) 5)  (1−C3H50) (n−C17H3,C−
0)3Tiで表面処理1 (炭酸カルシウム700重量部当り0゜5重量部便用) の  乍陽、りへ玉里 1)第1表注1)参照 2)〃  注2)参照 り カーボンミルドファイバ/θON量部尚りθ、fM
量部の(1−03H50) (n−C17H35c O
)3TiI で表面処理 4)ウオラストナイトG100重量部当り0.乙重量部
の(1−C3H,O) (n−C17H35Co )3
Tiで表1 面処理 S)輛処理 特許出願人 三菱モンサント化成株式会社代理2人 弁
理士 長谷用   − (ほか7名)
Y) Polyacrylic acid suspending agent 2) Polyvinyl alcohol, manufactured by Nippon Gosei 3)
(i-C3H50) (n-C, □H35G -0-)3
Surface treatment with Ti (7 parts by weight per 700 parts by weight of calcium carbonate)
Surface treatment with CH300 (7 parts by weight per 700 weight of calcium carbonate) 5) (1-C3H50) (n-C17H3,C-
0) Surface treatment with 3Ti 1 (0°5 parts by weight per 700 parts by weight of calcium carbonate) by Youyo and Rihe Tamari 1) See Table 1 Note 1) 2) See Note 2) Carbon milled fiber/ θON quantity θ, fM
Parts of (1-03H50) (n-C17H35c O
) Surface treatment with 3TiI 4) 0.0% per 100 parts by weight of wollastonite G. Otsu weight part (1-C3H,O) (n-C17H35Co)3
Ti Table 1 Surface treatment S) Vehicle treatment Patent applicant Mitsubishi Monsanto Kasei Co., Ltd. 2 representatives Patent attorney Hase - (7 others)

Claims (1)

【特許請求の範囲】[Claims] 芳香族ビニル単量体、または芳香族ビニル単量体及びこ
れと共重合可能な単量体からなる単量体混合物を無機充
填材の共存下に懸濁重合させて無機充填材を含有する熱
可塑性樹脂組成物を製造する方法において、上記単量体
、または、単量体混合物100重量部を有機チタネート
化合物によって表面処理された非繊維状無機充填材0゜
5−tO重量%及び繊維状無機充填材99.3−〜り0
重量%からなる無機充填材混合物l〜!Oθ重量部とと
もに、700〜3000重量部の水中に懸濁させて重合
することを特徴とする方法。
An aromatic vinyl monomer or a monomer mixture consisting of an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer is suspension-polymerized in the coexistence of an inorganic filler. In the method for producing a plastic resin composition, 100 parts by weight of the above monomer or monomer mixture is mixed with 0.5-tO weight % of a non-fibrous inorganic filler surface-treated with an organic titanate compound and a fibrous inorganic filler. Filler 99.3--0
Inorganic filler mixture consisting of % by weight l~! A method characterized in that polymerization is carried out by suspending 700 to 3000 parts by weight of water together with Oθ parts by weight.
JP23454482A 1982-12-28 1982-12-28 Preparation of concentrated thermoplastic resin composition containing inorganic filler Pending JPS59122535A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23454482A JPS59122535A (en) 1982-12-28 1982-12-28 Preparation of concentrated thermoplastic resin composition containing inorganic filler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23454482A JPS59122535A (en) 1982-12-28 1982-12-28 Preparation of concentrated thermoplastic resin composition containing inorganic filler

Publications (1)

Publication Number Publication Date
JPS59122535A true JPS59122535A (en) 1984-07-16

Family

ID=16972683

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23454482A Pending JPS59122535A (en) 1982-12-28 1982-12-28 Preparation of concentrated thermoplastic resin composition containing inorganic filler

Country Status (1)

Country Link
JP (1) JPS59122535A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63120758A (en) * 1986-11-10 1988-05-25 Idemitsu Petrochem Co Ltd Thermoplastic resin composition
JPS63183946A (en) * 1987-01-27 1988-07-29 Daicel Chem Ind Ltd Flame-retardant styrenic resin composition
JPS63183947A (en) * 1987-01-27 1988-07-29 Daicel Chem Ind Ltd Styrenic resin composition

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5431494A (en) * 1977-08-12 1979-03-08 Matsushita Electric Works Ltd Preparation of phenolic resin
JPS5543173A (en) * 1978-09-25 1980-03-26 Kanegafuchi Chem Ind Co Ltd Preparation of filler for vinyl chloride resin
JPS5710891A (en) * 1980-06-25 1982-01-20 Shibaura Eng Works Ltd Automatic vending machine
JPS57111305A (en) * 1980-12-29 1982-07-10 Mitsubishi Monsanto Chem Co Production of thermoplastic resin composition containing inorganic reinforcing material
JPS57149356A (en) * 1981-03-12 1982-09-14 Toyo Ink Mfg Co Ltd Electrically conductive resin composition

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5431494A (en) * 1977-08-12 1979-03-08 Matsushita Electric Works Ltd Preparation of phenolic resin
JPS5543173A (en) * 1978-09-25 1980-03-26 Kanegafuchi Chem Ind Co Ltd Preparation of filler for vinyl chloride resin
JPS5710891A (en) * 1980-06-25 1982-01-20 Shibaura Eng Works Ltd Automatic vending machine
JPS57111305A (en) * 1980-12-29 1982-07-10 Mitsubishi Monsanto Chem Co Production of thermoplastic resin composition containing inorganic reinforcing material
JPS57149356A (en) * 1981-03-12 1982-09-14 Toyo Ink Mfg Co Ltd Electrically conductive resin composition

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63120758A (en) * 1986-11-10 1988-05-25 Idemitsu Petrochem Co Ltd Thermoplastic resin composition
JPS63183946A (en) * 1987-01-27 1988-07-29 Daicel Chem Ind Ltd Flame-retardant styrenic resin composition
JPS63183947A (en) * 1987-01-27 1988-07-29 Daicel Chem Ind Ltd Styrenic resin composition

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