Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0561302B2 - - Google Patents
[go: Go Back, main page]

JPH0561302B2 - - Google Patents

Info

Publication number
JPH0561302B2
JPH0561302B2 JP63089882A JP8988288A JPH0561302B2 JP H0561302 B2 JPH0561302 B2 JP H0561302B2 JP 63089882 A JP63089882 A JP 63089882A JP 8988288 A JP8988288 A JP 8988288A JP H0561302 B2 JPH0561302 B2 JP H0561302B2
Authority
JP
Japan
Prior art keywords
weight
parts
powder
synthetic resin
resin 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 - Lifetime
Application number
JP63089882A
Other languages
Japanese (ja)
Other versions
JPS6426663A (en
Inventor
Atsushi Kawakatsu
Ryuichi Takagi
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP63089882A priority Critical patent/JPS6426663A/en
Publication of JPS6426663A publication Critical patent/JPS6426663A/en
Publication of JPH0561302B2 publication Critical patent/JPH0561302B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は合成樹脂の粉末の粉体特性改良方法に
関する。さらに詳しくは、本発明はゴムを幹ポリ
マーとするグラフト共重合体ラテツクスの凝固後
に微粉体を添加し、優れた粉体特性を有する合成
樹脂の粉末をうるための合成樹脂の粉末の粉体特
性改良方法に関する。 [従来の技術] 従来より合成樹脂の粉末の粉体特性を改良する
方法は種々検討されている。たとえば、共重合体
ラテツクスを気相凝固する方法(特開昭57−
59929号公報参照)、直接噴霧乾燥する方法や特定
の溶媒に球形分散した後、凝固する方法などが知
られている。 [発明が解決しようとする課題] しかしながら、前記のような従来から知られて
いる方法では、粉体特性を改良する効果が不充分
であり、近年の粉末の自動計量および輸送方式の
大型化に対応することができる流動性や耐ブロツ
キング性を有する粉末がえられないという欠点が
ある。 そこで本発明者らは、粉体特性の改良が粉末の
自動計量および輸送方式の大型化に不可欠である
と考え、鋭意研究を重ねた結果、本発明を完成す
るに至つた。 [課題を解決するための手段] すなわち、本発明はゴムを幹ポリマーとするグ
ラフト共重合体を凝固し、該共重合体100重量部
に対して平均粒径が10μm以下のSi,Mg,Al,
Ca,Ba,ZnおよびTiよりなる群から選ばれた金
属の1種または2種以上の酸化物、塩化物、炭酸
塩および硫酸塩の少なくとも1種の微粉体0.001
〜10重量部を添加することを特徴とする合成樹脂
の粉末の粉体特性改良方法に関する。 [実施例] 本発明に用いられるグラフト共重合体は、幹ポ
リマーとなるゴムをまず通常の乳化重合で製造
し、つぎにえられた共重合体ラテツクスに該共重
合体ラテツクスと共重合しうる単量体を通常の乳
化重合でグラフト共重合させることによつてえら
れる。 幹ポリマーとして用いられるゴムを形成する単
量体としては、たとえば、ブタジエン、イソプレ
ン、クロロプレンなどのジエン系単量体および/
またはブチルアクリレート、オクチルアクリレー
トなどのアクリル酸アルキルエステル系単量体が
用いられる。なお、前記アクリル酸アルキルエス
テル系単量体の炭素数4〜11、なかんづく5〜7
であることが好ましい。さらに、前記単量体を共
重合可能な単量体と共重合させてもよい。かかる
共重合可能な単量体としては、たとえば、メチル
メタクリレート、エチルメタクリレートなどのア
ルキルメタクリレート、アクリロニトリル、メタ
クリロニトリルなどのビニルシアン、スチレン、
α−メチルスチレンなどの芳香族ビニル、塩化ビ
ニル、臭化ビニルなどのハロゲン化ビニルなどが
あげられる。さらに架橋剤としてジビニルベンゼ
ン、モノエチレングリコールジメタクリレート、
ポリエチレングリコールジメタクリレートなどを
用いることができるが、本発明はかかる具体例の
みに限定されるものではない。 とくに好ましいゴムは、全量100重量部に対し
てブタジエン20〜80重量部、スチレン0〜50重量
部、ブタジエンまたはスチレンと共重合可能な単
量体0〜20重量部および架橋剤0〜5重量部を乳
化重合することによりえられる。 つぎに前記ゴムを幹ポリマーとしてグラフト共
重合させて共重合体をうるときに用いられる単量
体としては、前記ゴムと共重合可能なメチルアク
リレート、エチルアクリレート、ブチルアクリレ
ート、オクチルアクリレートなどのアルキルアク
リレート;メチルメタクリレート、エチルメタク
リレートなどのアクリルメタクリレート;アクリ
ロニトリル、メタクリロニトリルなどのビニルシ
アン;スチレン、α−メチルスチレンなどの芳香
族ビニル;塩化ビニル、臭化ビニルなどのハロゲ
ン化ビニルやジビニルベンゼン、モノエチレング
リコールジメタクリレート、ポリエチレングリコ
ールジメタクリレートなどの架橋剤などがあげら
れる。 本発明に用いられる微粉体としてはSi,Mg,
Al,Ca,Ba,ZnおよびTiよりなる群から選ば
れた金属の1種または2種以上の酸化物、塩化
物、炭酸塩および硫酸塩の単独またはそれらの混
合物があげられ、その具体例としては、たとえば
SiO2,MgO,MgCO3,Al2O3,Al2(CO33
CaO,CaCO3,TiO2,タルク,クレー,けいそ
う土,メタケイ酸カルシウムなどがあげられる。
なお、これらの化合物は天然物であつても合成物
であつてもよい。 前記微粉体の平均粒径は、10μm以下であり、
小さければ小さいほど粉末の粉体特性を改良する
効果が大きいので好ましい。平均粒径が10μmを
こえるばあい、粉体特性の改善効果が小さい。 また、前記微粉体は凝固されたゴムを幹ポリマ
ーとする共重合体100重量部に対して0.001〜10重
量部添加される。微粉体の添加量が0.001重量部
未満のばあい、粉体特性の改善効果が小さく、ま
た10重量部をこえるばあい、その合成樹脂の本来
の物性が低下する。 前記グラフト共重合によつてえられた共重合体
の組成は、共重合体全量100重量部に対してゴム
成分5〜80重量部およびグラフト成分20〜95重量
部からなり、グラフト部における単量体の比率は
グラフト部の全量100重量部に対してメチルメタ
クリレート30〜70重量部、スチレン30〜70重量
部、その他の共重合可能な単量体0〜20重量部お
よび架橋剤0〜5重量部であることが好ましい。 本発明において前記グラフト共重合体を凝固す
る際の凝固剤としては硫酸、塩酸、リン酸、硝酸
などの無機酸類、酢酸などの有機酸類、ナトリウ
ム、カリウムなどのいわゆるアルカリ金属のハロ
ゲン化物、無機酸とのアルカリ金属塩あるいは有
機酸とのアルカリ金属塩などが用いられる。これ
らは単独または2種以上併用することができる。
前記のような凝固剤を0.05〜10重量部、好ましく
は0.1〜5重量部を共重合体ラテツクス100重量部
に添加し、凝固操作を行なう。 グラフト共重合体を凝固した後に、平均粒径が
10μm以下の前記微粉体は、凝固された共重合体
100重量部に対して0.001〜10重量部の割合で添加
される。前記微粉体の添加は凝固後、熱処理後、
脱水後、乾燥後のいずれのときに行なつてもよい
が、脱水後または乾燥後の粉体に添加するのがも
つとも効果があるので好ましい。 以下、本発明の合成樹脂の粉末の粉体特性改良
方法を実施例にもとづき説明するが、本発明はこ
れらの実施例のみに限定されるものではない。 実施例 1 水200重量部、オレイン酸ソーダ1.5重量部、硫
酸第一鉄0.002重量部、エチレンジアミン四酢酸
二ナトリウム塩0.005重量部、リン酸三カリウム
0.2重量部、ホルムアルデヒドスルフオキシル酸
ソーダ0.2重量部、ブタジエン75重量部、スチレ
ン25重量部、ジビニルベンゼン1.0重量部および
ジイソプロピルベンゼンハイドロパーオキサイド
0.1重量部を内容積5の撹拌機付き重合容器に
仕込み、反応温度50℃で5時間重合させた。えら
れたゴムの重合転化率は98%であつた。つぎにえ
られた前記ゴム180重量部(固形分60重量部)、水
90重量部、硫酸第一鉄0.002重量部、エチレンジ
アミン四酢酸二ナトリウム塩0.004重量部、ホル
ムアルデヒドスルフオキシル酸ソーダ0.1重量部、
スチレン20重量部、メチルメタクリレート20重量
部を内容積5の撹拌機付き重合容器に仕込み、
反応温度60℃で3時間重合させた。えられた共重
合体の重合転化率は99%であつた。 えられた共重合体ラテツクス3(グラフト共
重合体100重量部)に10%塩酸300mlを加え凝固さ
せた後、脱水乾燥を行ない合成樹脂の粉末をえ
た。 えられた合成樹脂粉末100重量部に酸化チタン
(日本アエロジル(株)製、品番:チタニウムオキサ
イドP25、平均粒径:0.03μm)の微粉体を0.5重
量部添加し、粉体特性が改良された合成樹脂の粉
末をえた。 えられた合成樹脂の粉末の粉体特性として流動
性指数、崩壊性および剪断荷重を下記の方法にし
たがつて調べた。その結果を第1表に示す。 (流動性指数) ケミカル・エンジニアリング(Chemical
Engineering)、1965年1月18日刊163〜168頁に
記載の方法により安息角、圧縮度、スパチエラ
角、均一度(または凝集度)の4つの測定値をえ
られた合成樹脂の粉末について求め、それらの値
より換算表にしたがつて点数をつけ、こられの点
数の和で表わされる指数によつて評価した。なお
測定値が大きいものほど流動性がよい。 (崩壊性) えられた合成樹脂の粉末に一定の荷重(5Kg/
cm2)をかけてブロツク(形状:円柱状、寸法:5
cmφ×3cm)を製造し、該ブロツクに一定の振動
(振動数:60Hz)を100秒間与えて崩壊させ、崩壊
された粉末のうち18メツシユパスの粉末の重量を
もとのブロツクの全重量に対する百分率で表わし
た。その百分率の数値を崩壊性(単位:%)とい
い、数値が大きいものほどブロツキングしにくい
ことを示す。 (剪断荷重) パウダーベツドテスター(三協電業(株)製、
PTO型)にえられた合成樹脂の粉末を充填し、
一定荷重(20Kg/cm2)をかけ、一面剪断試験を行
なつた。そのときの最大剪断荷重(単位:Kg)を
樹脂のブロツキング指標として表わした。すなわ
ち、数値が大きいほどブロツキングしやすいこと
を示す。 実施例 2 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として酸化チタンを用いるかわりに炭
酸カルシウム(白石カルシウム(株)製、商品名:白
艶華CCR、平均粒径:0.08μm)0.5重量部を用い
たほかは実施例1と同様にして粉体特性が改良さ
れた合成樹脂の粉末をえた。えられた合成樹脂の
粉末の粉体特性として流動性指数、崩壊性および
剪断荷重を実施例1と同様にして測定した。その
結果を第1表に示す。 実施例 3 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として酸化チタンを用いるかわりに酸
化ケイ素(日本アエロジル(株)製、商品名:アエロ
ジル#2、平均粒径:0.01μm)0.5重量部を用い
たほかは実施例1と同様にして粉体特性が改良さ
れた合成樹脂の粉末をえた。えられた合成樹脂の
粉末の粉体特性として流動性指数、崩壊性および
剪断荷重を実施例1と同様にして測定した。その
結果を第1表に示す。 実施例 4 実施例1でえられた合成樹脂の粉末100重量部
に微粉体として酸化チランを用いるかわりに酸化
アルミニウム(日本アエロジル(株)製、商品名:ア
ルミニウムオキサドC、平均粒径:0.02μm)0.5
重量部を用いたほかは実施例1と同様にして粉体
特性が改良された合成樹脂の粉末をえた。えられ
た合成樹脂の粉末の粉体特性として流動性指数、
崩壊性および剪断荷重を実施例1と同様にして測
定した。その結果を第1表に示す。 実施例 5 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として酸化チタンを用いるかわりに塩
化バリウム(和光純薬(株)製を分離したもの、平均
粒径:0.5μm)0.001重量部を用いたほかは実施
例1と同様にして粉体特性が改良された合成樹脂
の粉末をえた。えられた合成樹脂の粉末の粉体特
性として流動性指数、崩壊性および剪断荷重を実
施例1と同様にして測定した。その結果を第1表
に示す。 実施例 6 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として酸化チタンを用いるかわりに塩
化亜鉛(和光純薬(株)製)を分級したもの(平均粒
径:1μm)10重量部を用いたほかは実施例1と
同様にして粉体特性が改良された合成樹脂の粉末
をえた。えられた合成樹脂の粉末の粉体特性とし
て流動性指数、崩壊性および剪断荷重を実施例1
と同様にして測定した。その結果を第1表に示
す。 実施例 7 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として平均粒径が0.03μmの酸化チタ
ンを用いるかわりに平均粒径が10μmの混合物
[混合物全体100重量部に対して塩化バリウム(和
光純薬(株)製)を分級したもの(平均粒径:10μ
m)0.25重量部と塩化亜鉛(和光純薬(株)製)を分
級したもの(平均粒径:10μm)0.25重量部から
なる]0.5重量部を用いたほかは実施例1と同様
にして粉体特性が改良された合成樹脂の粉末をえ
た。えられた合成樹脂の粉末の粉体特性として流
動性指数、崩壊性および剪断荷重を実施例1と同
様にして測定した。その結果を第1表に示す。 比較例 1 実施例1でえられた合成樹脂の粉末そのものの
粉体特性として流動性指数、崩壊性および剪断荷
重を実施例1と同様にして測定した。その結果を
第1表に示す。 比較例 2 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として酸化チタンを用いるかわりに炭
酸カルシウム(白石カルシウム(株)製、商品名:白
艶華CCR、平均粒径:0.08μm)0.005重量部を用
いたほかは実施例1と同様にして合成の樹脂粉末
をえた。 えられた合成樹脂の粉末の粉体特性として流動
性指数、崩壊性および剪断荷重を実施例1と同様
にして測定した。その結果を第1表に示す。 比較例 3 実施例1でえられた合成樹脂の粉末100重量部
に、微粉体として平均粒径が0.03μmの酸化チタ
ンを用いるかわりに平均粒径が15μmの混合物
[混合物全体100重量部に対して塩化バリウム(和
光純薬(株)製)を分級したもの(平均粒径:15μ
m)0.25重量部と塩化亜鉛(和光純薬(株)製)を分
級したもの(平均粒径:15μm)0.25重量部から
なる]0.5重量部を用いたほかは実施例1と同様
にして合成樹脂の粉末をえた。 えられた合成樹脂の粉末の粉体特性として流動
性指数、崩壊性および剪断荷重を実施例1と同様
にして測定した。その結果を第1表に示す。
[Industrial Field of Application] The present invention relates to a method for improving powder properties of synthetic resin powder. More specifically, the present invention involves adding fine powder after coagulation of a graft copolymer latex having rubber as a backbone polymer to obtain a synthetic resin powder having excellent powder characteristics. Regarding improvement methods. [Prior Art] Various methods for improving the powder properties of synthetic resin powder have been studied. For example, a method for coagulating copolymer latex in a vapor phase (Japanese Patent Application Laid-open No. 1983-
59929), a method of direct spray drying, and a method of coagulating after spherical dispersion in a specific solvent are known. [Problems to be Solved by the Invention] However, the conventionally known methods as described above are insufficiently effective in improving powder properties, and the recent increase in the size of automatic powder weighing and transportation methods The drawback is that powders with flowability and anti-blocking properties cannot be obtained. Therefore, the present inventors believed that improvement of powder properties is essential for automatic powder metering and larger transportation methods, and as a result of extensive research, they have completed the present invention. [Means for Solving the Problem] That is, the present invention coagulates a graft copolymer having rubber as a backbone polymer, and adds Si, Mg, and Al having an average particle size of 10 μm or less to 100 parts by weight of the copolymer. ,
At least one fine powder of one or more oxides, chlorides, carbonates and sulfates of metals selected from the group consisting of Ca, Ba, Zn and Ti 0.001
The present invention relates to a method for improving powder properties of synthetic resin powder, which comprises adding up to 10 parts by weight. [Example] The graft copolymer used in the present invention can be prepared by first producing a rubber serving as a backbone polymer by ordinary emulsion polymerization, and then copolymerizing the obtained copolymer latex with the copolymer latex. It can be obtained by graft copolymerizing monomers using conventional emulsion polymerization. Examples of rubber-forming monomers used as the backbone polymer include diene monomers such as butadiene, isoprene, and chloroprene;
Alternatively, acrylic acid alkyl ester monomers such as butyl acrylate and octyl acrylate are used. In addition, the carbon number of the acrylic acid alkyl ester monomer is 4 to 11, especially 5 to 7.
It is preferable that Furthermore, the monomer may be copolymerized with a copolymerizable monomer. Examples of such copolymerizable monomers include alkyl methacrylates such as methyl methacrylate and ethyl methacrylate, vinyl cyanogens such as acrylonitrile and methacrylonitrile, styrene,
Examples include aromatic vinyl such as α-methylstyrene, and halogenated vinyl such as vinyl chloride and vinyl bromide. Furthermore, divinylbenzene, monoethylene glycol dimethacrylate,
Although polyethylene glycol dimethacrylate and the like can be used, the present invention is not limited to such specific examples. Particularly preferred rubbers contain 20 to 80 parts by weight of butadiene, 0 to 50 parts by weight of styrene, 0 to 20 parts by weight of a monomer copolymerizable with butadiene or styrene, and 0 to 5 parts by weight of a crosslinking agent, based on 100 parts by weight of the total amount. obtained by emulsion polymerization. Next, monomers used when graft copolymerizing the rubber as a backbone polymer to obtain a copolymer include alkyl acrylates such as methyl acrylate, ethyl acrylate, butyl acrylate, and octyl acrylate, which are copolymerizable with the rubber. ; Acrylic methacrylates such as methyl methacrylate and ethyl methacrylate; Vinyl cyanide such as acrylonitrile and methacrylonitrile; Aromatic vinyls such as styrene and α-methylstyrene; Vinyl halides such as vinyl chloride and vinyl bromide, divinylbenzene, and monoethylene Examples include crosslinking agents such as glycol dimethacrylate and polyethylene glycol dimethacrylate. The fine powder used in the present invention includes Si, Mg,
Specific examples include oxides, chlorides, carbonates, and sulfates of one or more metals selected from the group consisting of Al, Ca, Ba, Zn, and Ti. For example,
SiO 2 , MgO, MgCO 3 , Al 2 O 3 , Al 2 (CO 3 ) 3 ,
Examples include CaO, CaCO 3 , TiO 2 , talc, clay, diatomaceous earth, and calcium metasilicate.
Note that these compounds may be natural products or synthetic products. The average particle size of the fine powder is 10 μm or less,
The smaller the particle size, the greater the effect of improving the powder characteristics of the powder, so it is preferable. When the average particle size exceeds 10 μm, the effect of improving powder properties is small. Further, the fine powder is added in an amount of 0.001 to 10 parts by weight per 100 parts by weight of a copolymer having coagulated rubber as a backbone polymer. If the amount of fine powder added is less than 0.001 part by weight, the effect of improving powder properties is small, and if it exceeds 10 parts by weight, the original physical properties of the synthetic resin will deteriorate. The composition of the copolymer obtained by the graft copolymerization is 5 to 80 parts by weight of the rubber component and 20 to 95 parts by weight of the graft component based on 100 parts by weight of the total amount of the copolymer, and the monomer content in the graft part is The proportions are 30 to 70 parts by weight of methyl methacrylate, 30 to 70 parts by weight of styrene, 0 to 20 parts by weight of other copolymerizable monomers, and 0 to 5 parts by weight of crosslinking agent, based on 100 parts by weight of the total amount of the graft part. Preferably. In the present invention, coagulants used in coagulating the graft copolymer include inorganic acids such as sulfuric acid, hydrochloric acid, phosphoric acid, and nitric acid, organic acids such as acetic acid, so-called alkali metal halides such as sodium and potassium, and inorganic acids. Alkali metal salts with organic acids or alkali metal salts with organic acids are used. These can be used alone or in combination of two or more.
0.05 to 10 parts by weight, preferably 0.1 to 5 parts by weight of the coagulant as described above is added to 100 parts by weight of the copolymer latex, and a coagulation operation is carried out. After coagulating the graft copolymer, the average particle size
The fine powder of 10 μm or less is a solidified copolymer.
It is added in a proportion of 0.001 to 10 parts by weight per 100 parts by weight. The fine powder is added after solidification, after heat treatment,
Although it may be carried out either after dehydration or drying, it is preferable to add it to the powder after dehydration or drying, as it is more effective. Hereinafter, the method for improving the powder properties of synthetic resin powder according to the present invention will be explained based on Examples, but the present invention is not limited to these Examples. Example 1 200 parts by weight of water, 1.5 parts by weight of sodium oleate, 0.002 parts by weight of ferrous sulfate, 0.005 parts by weight of ethylenediaminetetraacetic acid disodium salt, tripotassium phosphate
0.2 parts by weight, 0.2 parts by weight of sodium formaldehyde sulfoxylate, 75 parts by weight of butadiene, 25 parts by weight of styrene, 1.0 parts by weight of divinylbenzene, and diisopropylbenzene hydroperoxide.
0.1 part by weight was charged into a polymerization vessel with an internal volume of 5 and equipped with a stirrer, and polymerization was carried out at a reaction temperature of 50°C for 5 hours. The polymerization conversion rate of the obtained rubber was 98%. Next, 180 parts by weight of the obtained rubber (solid content 60 parts by weight), water
90 parts by weight, 0.002 parts by weight of ferrous sulfate, 0.004 parts by weight of ethylenediaminetetraacetic acid disodium salt, 0.1 parts by weight of sodium formaldehyde sulfoxylate,
20 parts by weight of styrene and 20 parts by weight of methyl methacrylate were placed in a polymerization vessel with an internal volume of 5 and equipped with a stirrer.
Polymerization was carried out at a reaction temperature of 60°C for 3 hours. The polymerization conversion rate of the obtained copolymer was 99%. 300 ml of 10% hydrochloric acid was added to the obtained copolymer latex 3 (100 parts by weight of the graft copolymer) to coagulate it, followed by dehydration and drying to obtain a synthetic resin powder. The powder properties were improved by adding 0.5 parts by weight of fine powder of titanium oxide (manufactured by Nippon Aerosil Co., Ltd., product number: Titanium Oxide P25, average particle size: 0.03 μm) to 100 parts by weight of the resulting synthetic resin powder. Obtained synthetic resin powder. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were investigated according to the following methods. The results are shown in Table 1. (Fluidity Index) Chemical Engineering
Engineering), January 18, 1965, Daily Edition, pp. 163-168, the four measured values of angle of repose, degree of compaction, angle of spatierla, and degree of uniformity (or degree of agglomeration) were obtained for the obtained synthetic resin powder, Scores were assigned based on these values according to a conversion table, and evaluation was made using an index expressed as the sum of these scores. Note that the larger the measured value, the better the fluidity. (Disintegrability) A certain load (5 kg/
cm 2 ) and block (shape: cylindrical, dimensions: 5
cmφ x 3cm), the block is subjected to constant vibration (frequency: 60Hz) for 100 seconds to disintegrate it, and the weight of the powder of 18 mesh passes among the disintegrated powder is calculated as a percentage of the total weight of the original block. It was expressed as The percentage value is called disintegrability (unit: %), and the larger the value, the more difficult it is to block. (Shear load) Powder bed tester (manufactured by Sankyo Dengyo Co., Ltd.)
PTO type) is filled with synthetic resin powder,
A one-sided shear test was conducted under a constant load (20 Kg/cm 2 ). The maximum shearing load (unit: Kg) at that time was expressed as a blocking index of the resin. That is, the larger the value, the easier it is to block. Example 2 Calcium carbonate (manufactured by Shiraishi Calcium Co., Ltd., trade name: Shiroenka CCR, average particle size: 0.08 μm) was added to 100 parts by weight of the synthetic resin powder obtained in Example 1, instead of using titanium oxide as a fine powder. ) A synthetic resin powder with improved powder properties was obtained in the same manner as in Example 1, except that 0.5 part by weight was used. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1. Example 3 Silicon oxide (manufactured by Nippon Aerosil Co., Ltd., trade name: Aerosil #2, average particle size: 0.01) was added to 100 parts by weight of the synthetic resin powder obtained in Example 1 instead of using titanium oxide as a fine powder. A synthetic resin powder with improved powder properties was obtained in the same manner as in Example 1, except that 0.5 parts by weight (μm) was used. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1. Example 4 Instead of using tyrane oxide as a fine powder in 100 parts by weight of the synthetic resin powder obtained in Example 1, aluminum oxide (manufactured by Nippon Aerosil Co., Ltd., trade name: Aluminum Oxide C, average particle size: 0.02) μm) 0.5
A synthetic resin powder with improved powder properties was obtained in the same manner as in Example 1 except that parts by weight were used. The powder properties of the obtained synthetic resin powder include the fluidity index,
The collapsibility and shear load were measured in the same manner as in Example 1. The results are shown in Table 1. Example 5 To 100 parts by weight of the synthetic resin powder obtained in Example 1, instead of using titanium oxide as a fine powder, barium chloride (separated product manufactured by Wako Pure Chemical Industries, Ltd., average particle size: 0.5 μm) was added. A synthetic resin powder with improved powder properties was obtained in the same manner as in Example 1 except that 0.001 part by weight was used. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1. Example 6 100 parts by weight of the synthetic resin powder obtained in Example 1 was classified with zinc chloride (manufactured by Wako Pure Chemical Industries, Ltd.) instead of using titanium oxide as a fine powder (average particle size: 1 μm). A synthetic resin powder with improved powder properties was obtained in the same manner as in Example 1 except that 10 parts by weight was used. Example 1: Fluidity index, disintegration, and shear load were measured as powder properties of the obtained synthetic resin powder.
It was measured in the same manner. The results are shown in Table 1. Example 7 Instead of using titanium oxide with an average particle size of 0.03 μm as a fine powder to 100 parts by weight of the synthetic resin powder obtained in Example 1, a mixture with an average particle size of 10 μm [based on 100 parts by weight of the entire mixture] Barium chloride (manufactured by Wako Pure Chemical Industries, Ltd.) was classified using
m) 0.25 parts by weight and 0.25 parts by weight of classified zinc chloride (manufactured by Wako Pure Chemical Industries, Ltd.) (average particle size: 10 μm)] Powder was prepared in the same manner as in Example 1, except that 0.5 parts by weight were used. A synthetic resin powder with improved physical properties was obtained. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1. Comparative Example 1 The powder properties of the synthetic resin powder itself obtained in Example 1, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1. Comparative Example 2 In 100 parts by weight of the synthetic resin powder obtained in Example 1, instead of using titanium oxide as a fine powder, calcium carbonate (manufactured by Shiraishi Calcium Co., Ltd., product name: Shiroenka CCR, average particle size: 0.08 μm) ) A synthetic resin powder was obtained in the same manner as in Example 1 except that 0.005 part by weight was used. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1. Comparative Example 3 Instead of using titanium oxide with an average particle size of 0.03 μm as a fine powder in 100 parts by weight of the synthetic resin powder obtained in Example 1, a mixture with an average particle size of 15 μm [based on 100 parts by weight of the entire mixture] Barium chloride (manufactured by Wako Pure Chemical Industries, Ltd.) was classified using
m) 0.25 parts by weight and 0.25 parts by weight of classified zinc chloride (manufactured by Wako Pure Chemical Industries, Ltd.) (average particle size: 15 μm)] Synthesized in the same manner as in Example 1 except that 0.5 parts by weight were used. I got resin powder. The powder characteristics of the obtained synthetic resin powder, such as fluidity index, disintegration, and shear load, were measured in the same manner as in Example 1. The results are shown in Table 1.

【表】 [発明の効果] 本発明によれば、合成樹脂の粉末の流動性およ
び耐ブロツキング性を従来より知られている方法
を用いたばあいに比べていちじるしく向上させる
ことができる。したがつて合成樹脂の粉末の貯蔵
中のブロツキング現象や輸送ラインの詰りをなく
すことができるだけではなく、粉末の自動計量お
よび輸送の大型化を可能にすることができる。
[Table] [Effects of the Invention] According to the present invention, the fluidity and blocking resistance of synthetic resin powder can be significantly improved compared to when conventionally known methods are used. Therefore, it is possible not only to eliminate blocking phenomena and clogging of transportation lines during storage of synthetic resin powder, but also to enable automatic weighing and transportation of powders on a larger scale.

Claims (1)

【特許請求の範囲】[Claims] 1 ゴムを幹ポリマーとするグラフト共重合体ラ
テツクスを凝固し、該共重合体100重量部に対し
て平均粒径が10μm以下のSi,Mg,Al,Ca,
Ba,ZnおよびTiよりなる群から選ばれた金属の
1種または2種以上の酸化物、塩化物、炭酸塩お
よび硫酸塩の少なくとも1種の微粉体0.001〜10
重量部を添加することを特徴とする合成樹脂の粉
末の粉体特性改良方法。
1. Coagulate a graft copolymer latex with rubber as the backbone polymer, and add Si, Mg, Al, Ca,
Fine powder of at least one oxide, chloride, carbonate and sulfate of one or more metals selected from the group consisting of Ba, Zn and Ti 0.001 to 10
A method for improving powder characteristics of a synthetic resin powder, characterized by adding parts by weight.
JP63089882A 1987-04-13 1988-04-12 Method for improving powder characteristic of synthetic polymer powder Granted JPS6426663A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63089882A JPS6426663A (en) 1987-04-13 1988-04-12 Method for improving powder characteristic of synthetic polymer powder

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP9007587 1987-04-13
JP63089882A JPS6426663A (en) 1987-04-13 1988-04-12 Method for improving powder characteristic of synthetic polymer powder

Publications (2)

Publication Number Publication Date
JPS6426663A JPS6426663A (en) 1989-01-27
JPH0561302B2 true JPH0561302B2 (en) 1993-09-06

Family

ID=13988403

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63089882A Granted JPS6426663A (en) 1987-04-13 1988-04-12 Method for improving powder characteristic of synthetic polymer powder

Country Status (1)

Country Link
JP (1) JPS6426663A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4961078B2 (en) * 2001-03-15 2012-06-27 三菱レイヨン株式会社 Graft copolymer mixed powder and method for improving powder properties of graft copolymer
JP2007302861A (en) * 2006-04-14 2007-11-22 Hitachi Chem Co Ltd Method for producing polymer powder

Also Published As

Publication number Publication date
JPS6426663A (en) 1989-01-27

Similar Documents

Publication Publication Date Title
JP5185534B2 (en) Method for producing coagulated latex particles
EP0611788B1 (en) Method for producing powdery and granular polymers
JP3260486B2 (en) Method for producing synthetic resin powder with improved blocking resistance
JPS6347745B2 (en)
JP2873107B2 (en) Method for producing rubber-containing graft copolymer particles
WO2001096468A1 (en) Resin composition improved in powder characteristics and process for the production thereof
JPH0561302B2 (en)
JP2003119396A (en) Thermoplastic resin composition with excellent impact resistance
JP2000273258A (en) Improved impact resistance resin for vinyl chloride resin with improved powder properties
US4460749A (en) Rubber powders
JPH0655833B2 (en) Method for improving powder properties of synthetic resin powder
US20060122327A1 (en) Process for preparing enlarged latex particles
JP3347869B2 (en) Method for producing graft copolymer powder
JPH06256415A (en) Method for producing powdery polymer
JP3163195B2 (en) Method for producing powdery granular polymer
JPH10279640A (en) Method for recovering rubber-containing polymer
JPS6037807B2 (en) Manufacturing method of terpolymer-polyblend
JPS6342924B2 (en)
EP0287930B1 (en) Process for improving properties of synthetic resin powder
JP2002309056A (en) Impact modifier for acrylic resin, method for producing the same, acrylic resin composition, and method for modifying impact resistance of acrylic resin
JPH06157923A (en) Production of thermoplastic polymer powder
JP2515013B2 (en) Vinyl chloride resin composition
JPH1087934A (en) Vinyl chloride resin composition
JPH0568485B2 (en)
JPS6322207B2 (en)