JPH0372643B2 - - Google Patents

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Publication number
JPH0372643B2
JPH0372643B2 JP57139936A JP13993682A JPH0372643B2 JP H0372643 B2 JPH0372643 B2 JP H0372643B2 JP 57139936 A JP57139936 A JP 57139936A JP 13993682 A JP13993682 A JP 13993682A JP H0372643 B2 JPH0372643 B2 JP H0372643B2
Authority
JP
Japan
Prior art keywords
solid catalyst
catalyst component
solid
titanium
mmol
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
JP57139936A
Other languages
Japanese (ja)
Other versions
JPS5930805A (en
Inventor
Takefumi Yano
Tokuji Inoe
Shigeru Igai
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.)
Ube Corp
Original Assignee
Ube Industries 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP13993682A priority Critical patent/JPS5930805A/en
Publication of JPS5930805A publication Critical patent/JPS5930805A/en
Publication of JPH0372643B2 publication Critical patent/JPH0372643B2/ja
Granted legal-status Critical Current

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  • Catalysts (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)

Description

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

本発明は、α−オレフイン重合用固体触媒成分
の貯蔵法に関する。 マグネシウム、チタン、ハロゲン及び電子供与
体を必須構成々分とするα−オレフイン重合用固
体触媒成分は、光に対して敏感である。特に、該
固体触媒成分が粉末状であるときには、光が当た
ることによつてその触媒性能が著しく低下する。
このことは、上記固体触媒成分にのみ認められる
特異な現象である。事実、現在工業的に広く採用
されている三塩化チタンを主成分とする固体触媒
成分は、光にさらされても長期にわたつてその触
媒性能を保持する。 本発明は、マグネシウム、チタン、ハロゲン及
び電子供与体を必須構成々分とするα−オレフイ
ン重合用固体触媒成分の貯蔵法を提供するもので
あり、その要旨は、不活性ガス雰囲気下に光を遮
断した状態で該固体触媒成分を貯蔵することにあ
る。 本発明におけるα−オレフイン重合用固体触媒
成分は、マグネシウム、チタン、ハロゲン及び電
子供与体を必須構成々分とするものである。 該固体触媒成分は、たとえば、本出願人の出願
に係る特開昭56−45909号公報、同56−55405号公
報、同56−76411号公報、同56−163102号公報、
同57−18706号公報、同57−25306号公報、同57−
25307号公報、同57−83510号公報、特願昭56−
26102号明細書などに記載の方法、あるいは、ハ
ロゲン化マグネシウム、ハロゲン化チタン、及び
エステル、エーテル、アミンなどの電子供与体を
共粉砕する方法などによつて調製することができ
る。これらの固体触媒成分は有機アルミニウム化
合物と組合せて、エチレン、プロピレン、ブテン
−1、ヘキセン−1、オクテン−1の重合触媒と
して使用される。 不活性ガスの具体例としては、窒素、アルゴ
ン、ヘリウムなどが挙げられる。 本発明においては、上記固体触媒成分を、光を
遮断した状態、たとえば、光を実質的に透過しな
いガラス容器、プラスチツク容器、陶容器、金属
容器中で保存する。ガラス容器あるいはプラスチ
ツク容器を使用する場合は、外壁を黒いシール材
で被覆するか、容器自体を実質的に光不透過の色
彩にする必要がある。 固体触媒成分は、ヘプタン、ヘキサン、トルエ
ン、ベンゼン、シクロヘキサンなどの不活性有機
溶媒、ミネラルオイル、ワリセンなどの高粘度物
質に懸濁させた状態で貯蔵してもよく、乾燥粉末
の状態で貯蔵してもよい。 つぎに実施例および比較例を示す。以下におい
て、重合活性は、固体触媒成分1g当り、重合時
間1時間当りのポリプロピレンの収量(g)であ
り、H.I.は、重合反応で生成するポリプロピレン
を沸騰n−ヘプタンで24時間抽出処理して得られ
る固体ポリマーの処理前のポリマーに対する重量
%である。 実施例1〜5及び比較例1〜4 (1) 固体触媒成分の調製: 無水塩化アルミニウム15ミリモルをトルエン40
mlに添加し、ついでメチルトリエトキシシラン15
ミリモルを添加し、撹拌下に、25℃で0.5時間反
応させた後、60℃に昇温して1時間反応させた。 反応生成混合物を−5℃に冷却した後、撹拌下
にn−ブチルマグネシウムクロライド27ミリモル
を含むジイソアミルエーテル18mlを0.5時間で反
応生成混合物に滴下した。反応系の温度は、−5
℃に保つた。滴下終了後30℃に昇温し1時間反応
を続けた。析出した固体を別し、トルエンで洗
浄した。 得られた固体4.90gをトルエン25mlに懸濁さ
せ、この懸濁液に四塩化チタン150ミリモルを添
加した後、90℃に昇温し撹拌下に1時間固体と四
塩化チタンとを接触させた。同温度でチタン含有
固体を別し、n−ヘプタンついでトルエンで洗
浄した。 チタン含有固体4.10gをトルエン25mlに懸濁さ
せ、この懸濁液に安息香酸エチル6.5ミリモルを
添加し、撹拌しながら90℃に1時間保つた。エス
テル処理固体を同温度で別し、n−ヘプタンつ
いでトルエンで洗浄した。 エステル処理固体をトルエン25mlに懸濁させ、
この懸濁液に四塩化チタン150ミリモルを添加し、
撹拌下に90℃で1時間エステル処理固体と四塩化
チタンとを接触させた。得られた固体触媒成分を
同温度で別し、n−ヘプタンで洗浄した。 固体触媒成分のチタン含有率は2.7重量%であ
つた。 (2) 固体触媒成分の貯蔵: 上記固体触媒成分を褐色のナスフラスコに取
り、真空下(1mmHg)に室温で4時間乾燥した。
次いで窒素を流通させて不活性ガス雰囲気下とし
たドライボツクス中で透明なガラスチユーブに所
定量の固体触媒成分を分取し、チユーブを溶封し
てアンプルとした。このガラスアンプルの内4本
はアルミニウムホイルで被覆し、残りの4本はそ
のままで、室内で所定日数貯蔵した。 (3) 重 合: 撹拌機付の内容積1のオートクレーブ内に固
体触媒成分(固体触媒成分として8.4mg)を封入
したガラスアンプルを取り付けた後、オートクレ
ーブ内の空気を窒素で置換した。 p−トリル酸メチル0.12ミリモルを含むn−ヘ
プタン溶液6.6ml、ついでトリエチルアルミニウ
ム0.47ミリモルを含むn−ヘプタン溶液1.7mlを
オートクレーブに仕込んだ。 この後液体プロピレン600mlをオートクレーブ
に導入し、オートクレーブを振とうした。 オートクレーブ内容物を65℃に昇温した後、撹
拌を開始して上記ガラスアンプルを破砕し、65℃
で1時間プロピレンを重合させた。 重合反応終了後、未反応のプロピレンを放出
し、ガラス破片を取り除き、生成ポリプロピレン
を50℃で20時間減圧乾燥した。 重合結果を第1表に示す。
The present invention relates to a method for storing solid catalyst components for α-olefin polymerization. The solid catalyst component for α-olefin polymerization, which has magnesium, titanium, halogen, and an electron donor as essential constituents, is sensitive to light. In particular, when the solid catalyst component is in powder form, its catalytic performance is significantly reduced by exposure to light.
This is a unique phenomenon observed only in the above-mentioned solid catalyst component. In fact, solid catalyst components based on titanium trichloride, which are currently widely used industrially, retain their catalytic performance over long periods of time even when exposed to light. The present invention provides a method for storing a solid catalyst component for α-olefin polymerization containing magnesium, titanium, halogen, and an electron donor as essential components, and the gist thereof is to irradiate light in an inert gas atmosphere. The purpose is to store the solid catalyst component in a blocked state. The solid catalyst component for α-olefin polymerization in the present invention contains magnesium, titanium, halogen, and an electron donor as essential components. The solid catalyst component is disclosed in, for example, JP-A-56-45909, JP-A-56-55405, JP-A-56-76411, JP-A-56-163102, filed by the present applicant.
No. 57-18706, No. 57-25306, No. 57-
Publication No. 25307, Publication No. 57-83510, Patent Application 1983-
It can be prepared by the method described in the specification of No. 26102, or by a method of co-pulverizing magnesium halide, titanium halide, and an electron donor such as ester, ether, or amine. These solid catalyst components are used in combination with organoaluminum compounds as polymerization catalysts for ethylene, propylene, butene-1, hexene-1, and octene-1. Specific examples of the inert gas include nitrogen, argon, helium, and the like. In the present invention, the solid catalyst component is stored in a light-blocked state, for example, in a glass container, plastic container, ceramic container, or metal container that does not substantially transmit light. If a glass or plastic container is used, it is necessary to cover the outer wall with a black sealant or to paint the container itself in a color that is substantially opaque to light. The solid catalyst component may be stored suspended in an inert organic solvent such as heptane, hexane, toluene, benzene, cyclohexane, or a highly viscous substance such as mineral oil or warisene, or may be stored as a dry powder. It's okay. Next, Examples and Comparative Examples will be shown. In the following, polymerization activity is the yield (g) of polypropylene per 1 g of solid catalyst component per 1 hour of polymerization time, and HI is the yield (g) of polypropylene obtained by extracting polypropylene produced in the polymerization reaction with boiling n-heptane for 24 hours. % by weight of the solid polymer treated relative to the untreated polymer. Examples 1 to 5 and Comparative Examples 1 to 4 (1) Preparation of solid catalyst component: 15 mmol of anhydrous aluminum chloride was added to 40 mmol of toluene.
ml and then methyltriethoxysilane 15
After adding 1 mmol of the mixture and reacting at 25° C. for 0.5 hour with stirring, the temperature was raised to 60° C. and the reaction was continued for 1 hour. After the reaction mixture was cooled to -5° C., 18 ml of diisoamyl ether containing 27 mmol of n-butylmagnesium chloride was added dropwise to the reaction mixture over 0.5 hours while stirring. The temperature of the reaction system is -5
It was kept at ℃. After the dropwise addition was completed, the temperature was raised to 30°C and the reaction was continued for 1 hour. The precipitated solid was separated and washed with toluene. 4.90 g of the obtained solid was suspended in 25 ml of toluene, and 150 mmol of titanium tetrachloride was added to this suspension. The temperature was raised to 90°C and the solid and titanium tetrachloride were brought into contact for 1 hour with stirring. . At the same temperature, the titanium-containing solid was separated and washed with n-heptane and then toluene. 4.10 g of the titanium-containing solid was suspended in 25 ml of toluene, and 6.5 mmol of ethyl benzoate was added to this suspension, which was kept at 90° C. for 1 hour with stirring. The ester treated solid was separated at the same temperature and washed with n-heptane and then toluene. Suspend the ester-treated solid in 25 ml of toluene,
Add 150 mmol of titanium tetrachloride to this suspension,
The ester-treated solid was brought into contact with titanium tetrachloride for 1 hour at 90°C with stirring. The obtained solid catalyst component was separated at the same temperature and washed with n-heptane. The titanium content of the solid catalyst component was 2.7% by weight. (2) Storage of solid catalyst component: The solid catalyst component was placed in a brown eggplant flask and dried under vacuum (1 mmHg) at room temperature for 4 hours.
Next, a predetermined amount of the solid catalyst component was collected into a transparent glass tube in a dry box under an inert gas atmosphere by flowing nitrogen, and the tube was sealed to form an ampoule. Four of the glass ampoules were covered with aluminum foil, and the remaining four were stored indoors for a predetermined number of days. (3) Polymerization: A glass ampoule containing a solid catalyst component (8.4 mg as solid catalyst component) was placed in an autoclave with an internal volume of 1 and equipped with a stirrer, and then the air in the autoclave was replaced with nitrogen. 6.6 ml of an n-heptane solution containing 0.12 mmol of methyl p-tolylate and then 1.7 ml of an n-heptane solution containing 0.47 mmol of triethylaluminum were charged into the autoclave. After this, 600 ml of liquid propylene was introduced into the autoclave and the autoclave was shaken. After raising the temperature of the contents of the autoclave to 65℃, stirring was started to crush the glass ampoule, and the temperature was increased to 65℃.
Propylene was polymerized for 1 hour. After the polymerization reaction was completed, unreacted propylene was released, glass fragments were removed, and the resulting polypropylene was dried under reduced pressure at 50°C for 20 hours. The polymerization results are shown in Table 1.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 マグネシウム、チタン、ハロゲン及び電子供
与体を必須構成々分とするα−オレフイン重合用
固体触媒成分を、不活性ガス雰囲気下に光を遮断
した状態で貯蔵することを特徴とするα−オレフ
イン重合用固体触媒成分の貯蔵法。
1 α-olefin polymerization characterized in that a solid catalyst component for α-olefin polymerization containing magnesium, titanium, halogen, and an electron donor as essential constituents is stored in an inert gas atmosphere in a state where light is blocked. Storage method of solid catalyst components for use.
JP13993682A 1982-08-13 1982-08-13 Method for storing catalytic component for polymerizing alpha-olefin Granted JPS5930805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13993682A JPS5930805A (en) 1982-08-13 1982-08-13 Method for storing catalytic component for polymerizing alpha-olefin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13993682A JPS5930805A (en) 1982-08-13 1982-08-13 Method for storing catalytic component for polymerizing alpha-olefin

Publications (2)

Publication Number Publication Date
JPS5930805A JPS5930805A (en) 1984-02-18
JPH0372643B2 true JPH0372643B2 (en) 1991-11-19

Family

ID=15257113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13993682A Granted JPS5930805A (en) 1982-08-13 1982-08-13 Method for storing catalytic component for polymerizing alpha-olefin

Country Status (1)

Country Link
JP (1) JPS5930805A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61188401A (en) * 1985-02-15 1986-08-22 Mitsui Toatsu Chem Inc Storage of transition metal catalyst slurry

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5317683A (en) * 1976-08-02 1978-02-17 Mitsui Toatsu Chem Inc Polymerization of alpha-olefin
JPS5470385A (en) * 1977-11-15 1979-06-06 Mitsubishi Chem Ind Ltd Production of olefin polymer
JPS54142192A (en) * 1978-03-31 1979-11-06 Union Carbide Corp Polymerization catalyst*its manufacture and use in ethylene single polymerization
JPS55135105A (en) * 1979-04-10 1980-10-21 Mitsui Petrochem Ind Ltd Titanium catalyst component for olefin polymerization
JPS5645909A (en) * 1979-09-21 1981-04-25 Ube Ind Ltd Polymerization of alpha-olefin
JPS56136806A (en) * 1980-03-29 1981-10-26 Mitsui Petrochem Ind Ltd Storage of solid titanium catalyst component containing highly active magnesium
JPS56136805A (en) * 1980-03-29 1981-10-26 Mitsui Petrochem Ind Ltd Titanium catalyst component for olefin polymerization

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5317683A (en) * 1976-08-02 1978-02-17 Mitsui Toatsu Chem Inc Polymerization of alpha-olefin
JPS5470385A (en) * 1977-11-15 1979-06-06 Mitsubishi Chem Ind Ltd Production of olefin polymer
JPS54142192A (en) * 1978-03-31 1979-11-06 Union Carbide Corp Polymerization catalyst*its manufacture and use in ethylene single polymerization
JPS55135105A (en) * 1979-04-10 1980-10-21 Mitsui Petrochem Ind Ltd Titanium catalyst component for olefin polymerization
JPS5645909A (en) * 1979-09-21 1981-04-25 Ube Ind Ltd Polymerization of alpha-olefin
JPS56136806A (en) * 1980-03-29 1981-10-26 Mitsui Petrochem Ind Ltd Storage of solid titanium catalyst component containing highly active magnesium
JPS56136805A (en) * 1980-03-29 1981-10-26 Mitsui Petrochem Ind Ltd Titanium catalyst component for olefin polymerization

Also Published As

Publication number Publication date
JPS5930805A (en) 1984-02-18

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