JPS5930805A - Method for storing catalytic component for polymerizing alpha-olefin - Google Patents
Method for storing catalytic component for polymerizing alpha-olefinInfo
- Publication number
- JPS5930805A JPS5930805A JP13993682A JP13993682A JPS5930805A JP S5930805 A JPS5930805 A JP S5930805A JP 13993682 A JP13993682 A JP 13993682A JP 13993682 A JP13993682 A JP 13993682A JP S5930805 A JPS5930805 A JP S5930805A
- Authority
- JP
- Japan
- Prior art keywords
- solid catalyst
- catalytic component
- titanium
- catalyst component
- olefin
- 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.)
- Granted
Links
Landscapes
- Catalysts (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、α−オレフィン重合用固体触媒成分の貯蔵法
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for storing solid catalyst components for alpha-olefin polymerization.
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4分とするα−オレフィ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ってその触媒性能
が著しく低下する。The solid catalyst component for α-olefin polymerization has four essential components: magnesium, titanium, halogen, and an electron donor.
Sensitive to light. In particular, when the solid catalyst component is in powder form, its catalytic performance is significantly reduced by exposure to light.
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
れても長期にわたってその触媒性能を保持する。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.
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4分とするα−オレフィン重合用固体触
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。The present invention provides a method for storing a solid catalyst component for α-olefin polymerization, which essentially consists of magnesium, titanium, halogen, and an electron donor. The purpose is to store the solid catalyst component in a blocked state.
本発明におけるα−オレフィン重合用固体触媒成分は、
マグネシウム、チタン、ノ・ロゲン及び電子供与体を必
須構成4分とするものである。The solid catalyst component for α-olefin polymerization in the present invention is
The four essential components are magnesium, titanium, nitrogen, and an electron donor.
該固体触媒成分は、たとえば2本出願人の出願に係る特
開昭56−45909号公報、同56−554’ 05
号公報、同56−76411号公報。The solid catalyst component is described, for example, in Japanese Patent Application Laid-open Nos. 56-45909 and 56-554'05 filed by the same applicant.
No. 56-76411.
同56−76411号公報、同57−18706号公報
、同57−8510号公報、同57−25307号公報
、同57−83510号公報。No. 56-76411, No. 57-18706, No. 57-8510, No. 57-25307, No. 57-83510.
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7ウム、ノ・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っ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。It can be prepared by the method described in Japanese Patent Application No. 56-26102, or by the method of co-pulverizing magnesium halide, titanium halide, and an electron donor such as ester, ether, or amine. Can be done. These solid catalyst components are combined with organoaluminum compounds to produce ethylene, propylene, butene-1, hexene-1
Used as a polymerization catalyst for +octene-1.
不活性ガスの具体例としては、窒素、アルゴン。Specific examples of inert gases include nitrogen and argon.
ヘリウムなどが挙げられる。Examples include helium.
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、
プラスチック容器、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ッ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。In the present invention, the solid catalyst component is stored in a light-blocking state, for example, in a glass container that does not substantially transmit light.
Store in plastic, ceramic, or metal containers. When using glass or plastic containers,
Either the outer wall must be coated with a black sealant, or the container itself must be painted in a color that is substantially opaque to light.
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、ワセリ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。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 petrolatum, or as a dry powder. You can.
つぎに実施例および比較例を示す。以下において9重合
活性は、固体触媒成分17当り2重合時間1時間当りの
ポリプロピレンの収量(fI)であり、 H,1,は
1重合反応で生成するポリプロピレンを沸騰n−へブタ
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。Next, Examples and Comparative Examples will be shown. 9 In the following, polymerization activity is the yield (fI) of polypropylene per hour of polymerization time per solid catalyst component 17, and H,1, is the amount of polypropylene produced in one polymerization reaction extracted with boiling n-hbutane for 24 hours. It is the weight percent of the solid polymer obtained by treatment relative to the polymer before treatment.
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40m1
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、攪拌下に、25°Cで0.5時間反応させ
た後、60°Cに昇温しで1時間反応させた。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 ml of toluene.
Then, 15 mmol of methyltriethoxysilane was added, and the mixture was reacted at 25°C for 0.5 hour while stirring, and then the temperature was raised to 60°C, and the reaction was continued for 1 hour.
反応生成混合物を一5°Cに冷却した後、攪拌下に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18m1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。After the reaction product mixture was cooled to -5°C, it was heated to n-
18 ml of diisoamyl ether containing 27 mmol of butylmagnesium chloride were added dropwise to the reaction mixture over a period of 0.5 hours. What is the temperature of the reaction system?
−5゛Cに保った。滴下終了後30°Cに昇温し1時間
反応を続けた。析出した固体をf別し、トルエンで洗浄
した。It was kept at -5°C. 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.
得られた固体4.9 Orをトルエン25m1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°Cに昇温し攪拌下に1時間面体と四塩化チ
タンとを接触させた。同温度でチタン含有固体をP別し
、n−へブタンついでトルエンで洗浄した。The obtained solid 4.9 Or was suspended in 25 ml of toluene, 150 mmol of titanium tetrachloride was added to this suspension, the temperature was raised to 90°C, and the hedron and titanium tetrachloride were mixed for 1 hour with stirring. brought into contact. At the same temperature, the titanium-containing solid was separated with P and washed with n-hebutane and then toluene.
チタン含有固体4.10 rをトルエン25tnlに懸
濁させ、この懸濁液に安息香酸エチル6.5 ミIJモ
ルを添加し、攪拌しながら90°Cに1時間保った。4.10 r of the titanium-containing solid were suspended in 25 tnl of toluene, 6.5 mmoles of ethyl benzoate were added to this suspension and kept at 90°C for 1 hour with stirring.
エステル処理固体を同温度でr別し、n−へブタンつい
でトルエンで洗浄した。The ester-treated solid was separated at the same temperature and washed with n-hebutane and then toluene.
エステル処理固体をトルエン25m1に懸濁させ。The ester treated solid was suspended in 25 ml of toluene.
この懸濁液に四塩化チタン150 ミIJモルを添加し
、攪拌下に90°C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F別し、n−へブタンで洗浄した。To this suspension was added 150 mmoles of titanium tetrachloride, and the ester-treated solid was brought into contact with the titanium tetrachloride at 90° C. for 1 hour with stirring. The obtained solid catalyst component was subjected to F separation at the same temperature and washed with n-hebutane.
固体触媒成分のチタン含有率は2.7重量係であった。The titanium content of the solid catalyst component was 2.7% by weight.
(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
(1,nr)に室温で4時間乾燥した。(2) Storage of solid catalyst component: The solid catalyst component was taken into a brown eggplant flask and dried under vacuum (1, nr) at room temperature for 4 hours.
次いでドライボックス中で透明なガラスチューブに所定
量の固体触媒成分を分取し、チーープを溶封してアンプ
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。Next, a predetermined amount of the solid catalyst component was taken out into a transparent glass tube in a dry box, and the cheap was melt-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)重 合:
攪拌機付の内容積1t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8.47ng)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。(3) Polymerization: A glass ampoule containing a solid catalyst component (8.47 ng as a solid catalyst component) was placed in an autoclave with an internal volume of 1 ton equipped with a stirrer, and then the air in the autoclave was replaced with nitrogen.
p−)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−へブタン溶液1.7m
lをオートクレーブに仕込んだ。p-) 6.6 ml of n-heptane solution containing 0.12 mmol of methyl lylate + then 1.7 ml of n-heptane solution containing 0.47 mmol of triethylaluminum
1 was placed in an autoclave.
この後液体プロピレン600rttl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。After this, 600 rttl of liquid propylene was introduced into the autoclave and the autoclave was shaken.
オートクレーブ内容物を65°Cに昇温した後。After heating the autoclave contents to 65°C.
攪拌を開始して上記ガラスアンプルを破砕し。Start stirring and crush the glass ampoule.
65°Cで1時間プロピレンを重合させた。Propylene was polymerized for 1 hour at 65°C.
重合反応終了後、未反応のプロピレンを放出し。After the polymerization reaction is complete, unreacted propylene is released.
ガラス破片を取り除き、生成ポリプロピレンを50’C
で20時間減圧乾燥した。Remove the glass fragments and heat the resulting polypropylene to 50'C.
It was dried under reduced pressure for 20 hours.
重合結果を第1表に示す。The polymerization results are shown in Table 1.
第 1 表Chapter 1 Table
Claims (1)
須構成4分とするα−オレフィ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−オレフィン重合用固体触媒成分の貯
蔵法。α-olefin polymerization characterized by storing a solid catalyst component for α-olefin polymerization, which has four essential components of magnesium, titanium, halogen, and an electron donor, in an inert gas atmosphere and in a state where light is blocked. Storage method for solid catalyst components.
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 true JPS5930805A (en) | 1984-02-18 |
JPH0372643B2 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) |
Cited By (1)
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)
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 |
-
1982
- 1982-08-13 JP JP13993682A patent/JPS5930805A/en active Granted
Patent Citations (7)
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 |
Cited By (2)
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 |
JPH0580489B2 (en) * | 1985-02-15 | 1993-11-09 | Mitsui Toatsu Chemicals |
Also Published As
Publication number | Publication date |
---|---|
JPH0372643B2 (en) | 1991-11-19 |
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