JPH0745543B2 - Process for producing olefin polymer - Google Patents
Process for producing olefin polymerInfo
- Publication number
- JPH0745543B2 JPH0745543B2 JP19243187A JP19243187A JPH0745543B2 JP H0745543 B2 JPH0745543 B2 JP H0745543B2 JP 19243187 A JP19243187 A JP 19243187A JP 19243187 A JP19243187 A JP 19243187A JP H0745543 B2 JPH0745543 B2 JP H0745543B2
- Authority
- JP
- Japan
- Prior art keywords
- titanium
- carbon atoms
- group
- component
- compound
- 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
Links
- 238000000034 method Methods 0.000 title claims description 26
- 229920000098 polyolefin Polymers 0.000 title claims description 5
- 239000010936 titanium Substances 0.000 claims description 56
- 229910052719 titanium Inorganic materials 0.000 claims description 44
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 34
- 150000001875 compounds Chemical class 0.000 claims description 32
- 239000011777 magnesium Substances 0.000 claims description 22
- 239000007787 solid Substances 0.000 claims description 20
- 125000004432 carbon atom Chemical group C* 0.000 claims description 17
- -1 organic acid ester Chemical class 0.000 claims description 17
- 125000000217 alkyl group Chemical group 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 239000003446 ligand Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 150000001336 alkenes Chemical class 0.000 claims description 8
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 8
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 8
- 125000003118 aryl group Chemical group 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 4
- 150000002148 esters Chemical class 0.000 claims description 4
- 125000003454 indenyl group Chemical group C1(C=CC2=CC=CC=C12)* 0.000 claims description 4
- 239000012265 solid product Substances 0.000 claims description 4
- 150000004678 hydrides Chemical class 0.000 claims description 3
- 229930195733 hydrocarbon Natural products 0.000 claims description 3
- 230000000379 polymerizing effect Effects 0.000 claims description 3
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- 125000001931 aliphatic group Chemical group 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 229920006395 saturated elastomer Polymers 0.000 claims description 2
- 229910052710 silicon Inorganic materials 0.000 claims description 2
- 239000010703 silicon Substances 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 150000005846 sugar alcohols Polymers 0.000 claims description 2
- 229910052720 vanadium Inorganic materials 0.000 claims description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 21
- 238000006116 polymerization reaction Methods 0.000 description 20
- 229920000642 polymer Polymers 0.000 description 19
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 18
- 239000003054 catalyst Substances 0.000 description 16
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 11
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 7
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 7
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 7
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 7
- 239000000203 mixture Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- XWJBRBSPAODJER-UHFFFAOYSA-N 1,7-octadiene Chemical compound C=CCCCCC=C XWJBRBSPAODJER-UHFFFAOYSA-N 0.000 description 2
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 2
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Natural products C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 description 2
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- HGCIXCUEYOPUTN-UHFFFAOYSA-N cyclohexene Chemical compound C1CCC=CC1 HGCIXCUEYOPUTN-UHFFFAOYSA-N 0.000 description 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000011949 solid catalyst Substances 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- CLNYHERYALISIR-FNORWQNLSA-N (3e)-nona-1,3-diene Chemical compound CCCCC\C=C\C=C CLNYHERYALISIR-FNORWQNLSA-N 0.000 description 1
- PRBHEGAFLDMLAL-GQCTYLIASA-N (4e)-hexa-1,4-diene Chemical compound C\C=C\CC=C PRBHEGAFLDMLAL-GQCTYLIASA-N 0.000 description 1
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- LVZWSLJZHVFIQJ-UHFFFAOYSA-N Cyclopropane Chemical compound C1CC1 LVZWSLJZHVFIQJ-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 238000012661 block copolymerization Methods 0.000 description 1
- WJTCGQSWYFHTAC-UHFFFAOYSA-N cyclooctane Chemical compound C1CCCCCCC1 WJTCGQSWYFHTAC-UHFFFAOYSA-N 0.000 description 1
- 239000004914 cyclooctane Substances 0.000 description 1
- NLDGJRWPPOSWLC-UHFFFAOYSA-N deca-1,9-diene Chemical compound C=CCCCCCCC=C NLDGJRWPPOSWLC-UHFFFAOYSA-N 0.000 description 1
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 238000012685 gas phase polymerization Methods 0.000 description 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- JFNLZVQOOSMTJK-KNVOCYPGSA-N norbornene Chemical compound C1[C@@H]2CC[C@H]1C=C2 JFNLZVQOOSMTJK-KNVOCYPGSA-N 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- QYZLKGVUSQXAMU-UHFFFAOYSA-N penta-1,4-diene Chemical compound C=CCC=C QYZLKGVUSQXAMU-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000037048 polymerization activity Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- 150000003609 titanium compounds Chemical class 0.000 description 1
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、オレフィン重合体の製造方法に関する。さら
に詳しくは、Mg化合物に担持されたチタン系固体成分お
よびブリッジ型配位子を有するチタニウムジアルキル化
合物からなる触媒を用いて、高位体規制性のポリオレフ
ィンを製造する方法に関する。TECHNICAL FIELD The present invention relates to a method for producing an olefin polymer. More specifically, it relates to a method for producing a high-order-regulating polyolefin by using a catalyst composed of a titanium-based solid component supported on an Mg compound and a titanium dialkyl compound having a bridge-type ligand.
Mg化合物に担持されたチタン系固体成分は、有機アルミ
ニウム化合物と組み合わせて、オレフィン重合用の触媒
に使うことができるが、生成するポリマーは立体規則性
が低いことが知られている。このような触媒系で、立体
規則性を改善するため種々の電子供与体を重合時に添加
する方法が公知になっている(John Boor,Jr.,“Ziegle
r−Natta Catalysts and Polymerizations",Academic P
ress)。The titanium-based solid component supported on the Mg compound can be used as a catalyst for olefin polymerization in combination with an organoaluminum compound, but it is known that the polymer produced has low stereoregularity. In such a catalyst system, a method of adding various electron donors at the time of polymerization to improve stereoregularity has been known (John Boor, Jr., “Ziegle.
r−Natta Catalysts and Polymerizations ", Academic P
ress).
この従来のMg化合物に担持されたチタン系固体触媒で、
高立体規制性のポリマーを得るためには有機アルミニウ
ム化合物の他に第3成分として電子供与体を添加しなけ
ればならず、しかも立体規則性を高めるために電子供与
体の添加量を増加させると、重合活性が低下するという
問題点があった。With this titanium-based solid catalyst supported on this conventional Mg compound,
In order to obtain a highly stereoregulatory polymer, an electron donor must be added as a third component in addition to the organoaluminum compound, and if the addition amount of the electron donor is increased to increase the stereoregularity. However, there is a problem that the polymerization activity is lowered.
また、Mg化合物に担持されたチタン系固体触媒と(Men
−Cp)2TiMe2(n=0,1)化合物とを成分する触媒でオ
レフィンを重合する方法が公知になっている(Makromo
l.Chem.,Rapid Commun.7巻,719頁(1986))。なお、こ
の論文には、ブリッジ型の配位子を有するチタン化合物
を使用する記載はまったくない。In addition, the titanium-based solid catalyst supported on the Mg compound and (Me n
A method of polymerizing an olefin with a catalyst containing a —Cp) 2 TiMe 2 (n = 0,1) compound has been known (Makromo
l. Chem., Rapid Commun. 7, p. 719 (1986)). It should be noted that there is no description in this paper of using a titanium compound having a bridge-type ligand.
本発明者らは、上記の問題点を解決すべく研究を重ねた
結果、Mg化合物に担持されたチタン系固体成分と、ブリ
ッジ型配位子を有するチタニウムジアルキル化合物とか
らなる触媒が、2成分系であるにもかかわらず高立体規
則性の重合体を製造しうることを見いだし、本発明に到
達した。As a result of repeated studies to solve the above problems, the present inventors have found that a catalyst composed of a titanium-based solid component supported on an Mg compound and a titanium dialkyl compound having a bridge-type ligand has two components. It was found that a polymer having a high stereoregularity can be produced even though it is a system, and the present invention has been accomplished.
〔問題点を解決するための手段〕 すなわち本発明は、 (A)下記の段階I〜IIIの反応を経て製造されたMg化
合物に担持されたチタン系固体成分、及び I.無水マグネシウムジハライド、一般式Ti(OR1)4
で表わされるオルトチタン酸エステルおよび/または一
般式R2O−Ti(OR3)(OR4)mO−R5で表わされるポ
リチタン酸エステルからなる(ここでR1、R2、R3、R4お
よびR5は炭素数1〜20のアルキル基、アリール基または
炭素数3〜20のシクロアルキル基であり、mは2〜20の
数である)、および炭素数1ないし20の飽和若しくは
不飽和の1価若しくは多価アルコールを不活性炭化水
素溶剤中で混合して溶解させて(成分A)を得、 II.該(成分A)に、炭素2ないし24の脂肪族若しくは
芳香族のモノ若しくはポリカルボン酸エステル(以下有
機酸エステルという)、一般式AlXnR8 3-n(ここで、
XはClまたはBr、R8は炭素数3〜20のシクロアルキル
基、nは0〜3の数である)で表わされるハロゲン化ア
ルミニウム、および一般式SiXlR▲6 4-l若しくはSiXp
(OR7)4-p(ここで、XはClまたはBr、R6およびR7はそ
れぞれ炭素数1〜20のアルキル基、アリール基または炭
素数3〜20のシクロアルキル基、lまたはpは1〜4の
数である)で表わされるハロゲン化ケイ素からなる
(成分B)を混合反応させて固体(以下固体生成物
(I)という)を析出させ、 III.該固体生成物(I)に、一般式TiXq(OR9)4-q(こ
こで、XはClまたはBr、R9は炭素数1〜20のアルキル
基、アリール基または炭素数3〜20のシクロアルキル基
であり、qは1〜4の数である)で表わされ、ハロゲン
化チタンおよび/または一般式VOXs(OR10)3-s若し
くはVXt(OR11)4-tで表わされるハロゲン化バナジル若
しくはハロゲン化バナジウムからなる(成分C)を反
応させて固体(以下固体生成物(II)という)を収得す
る反応。[Means for Solving the Problems] That is, the present invention provides (A) a titanium-based solid component supported on an Mg compound produced through the following reactions of steps I to III, and I. anhydrous magnesium dihalide, General formula Ti (OR 1 ) 4
In ortho titanate represented and / or the general formula R 2 O-Ti (OR 3 ) (OR 4) m consists polytitanic acid ester represented by OR 5 (wherein R 1, R 2, R 3 , R 4 and R 5 are an alkyl group having 1 to 20 carbon atoms, an aryl group or a cycloalkyl group having 3 to 20 carbon atoms, m is a number of 2 to 20), and a saturated group having 1 to 20 carbon atoms or An unsaturated monohydric or polyhydric alcohol is mixed and dissolved in an inert hydrocarbon solvent to obtain (Component A), and II. (Component A) contains an aliphatic or aromatic carbon atom having 2 to 24 carbon atoms. Mono- or polycarboxylic acid ester (hereinafter referred to as organic acid ester), a general formula AlX n R 8 3-n (where,
X is Cl or Br, R 8 is a cycloalkyl group having a carbon number of 3 to 20, n is a number of 0 to 3), and an aluminum halide represented by the general formula SiX 1 R ▲ 6 4-l or SiX p
(OR 7 ) 4-p (wherein X is Cl or Br, R 6 and R 7 are each an alkyl group having 1 to 20 carbon atoms, an aryl group or a cycloalkyl group having 3 to 20 carbon atoms, and 1 or p is (Component B) composed of a silicon halide represented by the formula (1 to 4) is mixed and reacted to precipitate a solid (hereinafter referred to as a solid product (I)), and III. , The general formula TiX q (OR 9 ) 4-q (wherein X is Cl or Br, R 9 is an alkyl group having 1 to 20 carbon atoms, an aryl group or a cycloalkyl group having 3 to 20 carbon atoms, and q Is a number of 1 to 4) and is a titanium halide and / or a vanadyl halide or a halogenated compound represented by the general formula VOX s (OR 10 ) 3-s or VX t (OR 11 ) 4-t . A reaction for obtaining a solid (hereinafter referred to as a solid product (II)) by reacting (component C) composed of vanadium.
(B)インデニル基及びその部分水素化物から選ばれた
2個の基が低級アルキル基を介して結合したブリッジ型
化合物を2座配位子として有するチタニウムジアルキル
化合物、 を成分とする触媒を用いてオレフィンを重合することを
特徴とするオレフィン重合体の製造方法に係わるもので
ある。(B) A titanium dialkyl compound having as a bidentate ligand a bridge-type compound in which two groups selected from an indenyl group and a partial hydride thereof are bonded via a lower alkyl group. The present invention relates to a method for producing an olefin polymer, which comprises polymerizing an olefin.
本発明の方法において使用される触媒構成成分のMg化合
物に担持されたチタン系固体成分(A)の製造法には、 MgCl2を使用する方法、 Mg(OR)2を使用する方法、 RMgClを使用する方法、 RMgR′を使用する方法、 金属Mgをを使用する方法、 (ただしR,R′=アルキル基)等がある。The method for producing the titanium-based solid component (A) supported on the Mg compound as the catalyst component used in the method of the present invention is a method using MgCl 2 , a method using Mg (OR) 2 , and RMgCl. There are a method of using, a method of using RMgR ′, a method of using metal Mg, and the like (where R and R ′ are alkyl groups).
いずれの方法で製造されたMg化合物担持型チタン系固体
成分も使用可能であるが、より具体的には、特願昭59−
208775号(特開昭61−85408号)に示された製造方法を
挙げることができる。An Mg compound-supported titanium-based solid component produced by any method can be used, but more specifically, Japanese Patent Application No. 59-
The manufacturing method shown in 208775 (Japanese Patent Laid-Open No. 61-85408) can be mentioned.
本発明の方法において使用されるもう一つの触媒構成成
分のチタニウムジアルキル化合物(B)は、ブリッジ型
化合物を2座配位子として有するチタニウムジアルキル
化合である。ブリッジ型配位子としては、エチレンビス
(インデニル)基、エチレンビス(4,5,6,7−テトラヒ
ドロ−1−インデニル)基、1,3−プロパンジニルビス
(インデニル)基、および1,3−プロパンジニルビス
(4,5,6,7−テトラヒドロ−1−インイデニル)基等を
挙げることができる。上記のチタニウムジアルキル化合
物は、ブリッジ型配位子を有する公知のチタニウムジハ
ライド化合物(Journal of Organometallic Chem.,232
巻,233頁(1982)、および322巻、65頁(1987))と、
アルキルリチウムを反応させることにより得られる。ま
た、アルキル基として、メチル基、エチル基等を挙げる
ことができる。Another catalyst component, titanium dialkyl compound (B), used in the method of the present invention is a titanium dialkyl compound having a bridge type compound as a bidentate ligand. Examples of the bridge-type ligand include an ethylenebis (indenyl) group, an ethylenebis (4,5,6,7-tetrahydro-1-indenyl) group, a 1,3-propanedinylbis (indenyl) group, and a 1,3 -Propandinylbis (4,5,6,7-tetrahydro-1-inidenyl) group and the like can be mentioned. The above-mentioned titanium dialkyl compound is a known titanium dihalide compound having a bridge type ligand (Journal of Organometallic Chem., 232
Volume, 233 (1982), and 322, 65 (1987),
It is obtained by reacting alkyllithium. Moreover, a methyl group, an ethyl group, etc. can be mentioned as an alkyl group.
本発明の方法で使用することができるチタニウムジアル
キル化合物としては、エチレンビス(インデニル)チタ
ニウムジメチル、エチレンビス(インデニル)チタニウ
ムジエチル、エチレンビス(4,5,6,7−テトラヒドロ−
1−インデニル)チタニウムジメチル、エチレンビス
(4,5,6,7−テトラヒドロ−1−インデニル)チタニウ
ムジエチル、1,3−プロパンジニルビス(インデニル)
チタニウムジメチル、1,3−プロパンジニルビス(イン
デニル)チタニウムジエチル、1,3−プロパンジニルビ
ス(4,5,6,7−テトラヒドロ−1−インデニル)チタニ
ウムジメチル、1,3−プロパンジニルビス(4,5,6,7−テ
トラヒドロ−1−インデニル)チタニウムジエチル等で
あり、好ましくは、エチレンビス(インデニル)チタニ
ウムジメチル、1,3−プロパンジニルビス(インデニ
ル)チタニウムジメチルである。Titanium dialkyl compounds that can be used in the method of the present invention include ethylenebis (indenyl) titanium dimethyl, ethylenebis (indenyl) titanium diethyl, ethylenebis (4,5,6,7-tetrahydro-
1-indenyl) titanium dimethyl, ethylenebis (4,5,6,7-tetrahydro-1-indenyl) titanium diethyl, 1,3-propanedinylbis (indenyl)
Titanium dimethyl, 1,3-propanedinylbis (indenyl) titanium diethyl, 1,3-propanedinylbis (4,5,6,7-tetrahydro-1-indenyl) titanium dimethyl, 1,3-propanedinylbis (4 , 5,6,7-Tetrahydro-1-indenyl) titanium diethyl, etc., preferably ethylenebis (indenyl) titanium dimethyl and 1,3-propanedinylbis (indenyl) titanium dimethyl.
本発明の方法において、重合反応に用いられるオレフィ
ンは、エチレン、プロピレン、1−ブテン、4−メチル
−1−ペンテン、1−ヘキセン、1−オクテン、1−デ
センなどのα−オレフィンであり、これら2種以上の混
合成分を重合に供にすることもできる。また、上記α−
オレフィンを順次用いて、ブロック共重合に供すること
も可能である。さらには、ブタジエン、1,4−ヘキサジ
エン、1,4−ペンタジエン、1,7−オクタジエン、1,8−
ノナジエン、1,9−デカジエンなどのようなジエン類、
またはシクロプロパン、シクロブタン、シクロヘキセ
ン、ノルボルネン、ジシクロペンタジエンなどのような
環状オレフィンとα−オレフィンとの共重合にも有効で
ある。In the method of the present invention, the olefin used in the polymerization reaction is an α-olefin such as ethylene, propylene, 1-butene, 4-methyl-1-pentene, 1-hexene, 1-octene, 1-decene, It is also possible to use two or more kinds of mixed components for the polymerization. Also, the above α-
It is also possible to sequentially use olefins and subject them to block copolymerization. Furthermore, butadiene, 1,4-hexadiene, 1,4-pentadiene, 1,7-octadiene, 1,8-
Dienes such as nonadiene, 1,9-decadiene,
Alternatively, it is also effective for copolymerizing a cyclic olefin such as cyclopropane, cyclobutane, cyclohexene, norbornene, and dicyclopentadiene with an α-olefin.
重合方法としては、懸濁重合もしくは溶液重合のような
液相重合、または気相重合のいずれも可能である。液相
重合の重合溶液としては、ペンタン、ヘキサン、オクタ
ン、デカンなどの脂肪族系炭化水素、シクロペンタン、
シクロヘキサン、シクロオクタンなどの脂環族系炭化水
素、ベンゼン、トルエン、キシレンなどの芳香族系炭化
水素、ガソリン、灯油、軽油などの石油留分などが用い
られる。これらの中では、芳香族系炭化水素が好まし
い。As the polymerization method, either liquid phase polymerization such as suspension polymerization or solution polymerization, or gas phase polymerization can be used. As a polymerization solution for liquid phase polymerization, pentane, hexane, octane, aliphatic hydrocarbons such as decane, cyclopentane,
Alicyclic hydrocarbons such as cyclohexane and cyclooctane, aromatic hydrocarbons such as benzene, toluene and xylene, petroleum fractions such as gasoline, kerosene, and light oil are used. Of these, aromatic hydrocarbons are preferable.
反応系のオレフィン圧は、常圧〜50kg/cm2Gであり、重
合温度は、−50〜230℃、好ましくは、−20〜200℃の範
囲である。The olefin pressure of the reaction system is normal pressure to 50 kg / cm 2 G, and the polymerization temperature is -50 to 230 ° C, preferably -20 to 200 ° C.
本発明の方法では、(A)Mg化合物に担持されたチタン
系固体成分、(B)チタニウムジアルキル化合物の両成
分をそれぞれ重合容器に供給し、オレフィンの供給前に
5分〜3時間、好ましくは、30分〜2時間の範囲で撹拌
するのが適当である。両成分の重合系内における濃度、
モル比については特に制限はないが、好ましくは、
(B)/(A)のTi成分のモル比が、0.1〜100の範囲で
ある。In the method of the present invention, both (A) a titanium-based solid component supported on a Mg compound and (B) a titanium dialkyl compound are fed to a polymerization vessel, respectively, and 5 minutes to 3 hours, preferably 5 minutes to 3 hours before feeding an olefin. It is suitable to stir for 30 minutes to 2 hours. Concentration of both components in the polymerization system,
The molar ratio is not particularly limited, but preferably,
The molar ratio of the Ti component of (B) / (A) is in the range of 0.1 to 100.
本発明で用いるアイソタクチックインデックス(I.I.)
とは、例えば、プロピレン重合体の製造に於て、n−ヘ
キサン(20℃)不溶物としてのアイソタクチックポリプ
ロピレンのポリマーの全生成量100に対する重合割合
で、立体規則性の目安となるものである。Isotactic index (II) used in the present invention
For example, in the production of a propylene polymer, the term "stereoregularity" refers to the ratio of the polymerization of isotactic polypropylene as an insoluble matter in n-hexane (20 ° C) to the total amount of polymer production of 100. is there.
[発明の効果] Mg化合物に担持されたチタン型固体成分と組み合わせる
チタニウムジアルキル化合物として、インデニルおよび
その部分水素化物から選ばれた2個の基が低級アルキル
基を介して結合したブリッジ型化合物を2座配位子とし
て有するチタニウムジアルキル化合物を用いる本発明の
方法によれば、後述の実施例及び比較例から明らかな通
り、2成分系にもかかわらず、従来の触媒系よりも立体
規則性の高い重合体が得られる。[Effects of the Invention] As a titanium dialkyl compound to be combined with a titanium type solid component supported on a Mg compound, a bridge type compound in which two groups selected from indenyl and its partial hydride are bonded via a lower alkyl group is used. According to the method of the present invention using a titanium dialkyl compound having a bidentate ligand, as is clear from the examples and comparative examples described below, the stereoregularity is higher than that of the conventional catalyst system despite the two-component system. A polymer is obtained.
次に、本発明を実施例によって具体的に説明する。 Next, the present invention will be specifically described with reference to examples.
実施例1 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製トルエン500ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.06mmo
l、およびエチレンビス(インデニル)チタニウムジメ
チル0.58mmolを順次添加し、30℃に昇温した。この温度
で1時間撹拌し、次いで、これにプロピレンを全圧が1.
0kg/cm2Gを維持するように連続的に導入し、2.0時間重
合を行った。反応後、メタノールにより触媒成分を分解
し、得られたポリマーを乾燥した。この結果ポリマーが
5.2g得られ、I.I.は97であった。Example 1 500 ml of purified toluene was placed in a sus autoclave having an internal volume of 1.5 L, which had been sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the above-mentioned method (A) was added to 0.06 mmo as a Ti component.
1, and ethylenebis (indenyl) titanium dimethyl (0.58 mmol) were sequentially added, and the temperature was raised to 30 ° C. Stir at this temperature for 1 hour, then add propylene to this at a total pressure of 1.
It was continuously introduced so as to maintain 0 kg / cm 2 G, and polymerization was carried out for 2.0 hours. After the reaction, the catalyst component was decomposed with methanol, and the obtained polymer was dried. As a result, the polymer
5.2 g were obtained, II was 97.
実施例2 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製トルエン500ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.05mmo
l、およびエチレンビス(インデニル)チタニウムジメ
チル0.51mmolを順次添加し、30℃に昇温した。この温度
で1時間撹拌し、次いで、これにプロピレンを全圧が1.
0kg/cm2Gを維持するように連続的に導入し、4.0時間重
合を行った。反応後、メタノールにより触媒成分を分解
し、得られたポリマーを乾燥した。この結果ポリマーが
7.6g得られ、I.I.は96であった。Example 2 500 ml of purified toluene was added to a sus autoclave with an internal volume of 1.5 L that had been sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the above-mentioned method (A) was used as a Ti component in an amount of 0.05 mmo.
1, and ethylenebis (indenyl) titanium dimethyl (0.51 mmol) were sequentially added, and the temperature was raised to 30 ° C. Stir at this temperature for 1 hour, then add propylene to this at a total pressure of 1.
It was continuously introduced so as to maintain 0 kg / cm 2 G, and polymerization was carried out for 4.0 hours. After the reaction, the catalyst component was decomposed with methanol, and the obtained polymer was dried. As a result, the polymer
7.6 g was obtained, II was 96.
実施例3 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製トルエン500ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.06mmo
l、およびエチレンビス(インデニル)チタニウムジメ
チル0.59mmolを順次添加し、50℃に昇温した。この温度
で1時間撹拌し、次いで、これにプロピレンを全圧が7.
0kg/cm2Gを維持するように連続的に導入し、2.0時間重
合を行った。反応後、メタノールにより触媒成分を分解
し、得られたポリマーを乾燥した。この結果ポリマーが
28.8g得られ、I.I.は94であった。Example 3 500 ml of purified toluene was added to a sus autoclave having an internal volume of 1.5 L which had been sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the method of the above (A) was 0.06 mmo as Ti component.
1, and ethylenebis (indenyl) titanium dimethyl (0.59 mmol) were sequentially added, and the temperature was raised to 50 ° C. Stir at this temperature for 1 hour, then add propylene to this at a total pressure of 7.
It was continuously introduced so as to maintain 0 kg / cm 2 G, and polymerization was carried out for 2.0 hours. After the reaction, the catalyst component was decomposed with methanol, and the obtained polymer was dried. As a result, the polymer
28.8 g was obtained and II was 94.
実施例4 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製トルエン500ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.06mmo
l、および1,3−プロパンジニルビス(インデニル)チタ
ニウムジメチル0.59mmolを順次添加し、30℃に昇温し
た。この温度で1時間撹拌し、次いで、これにプロピレ
ンを全圧が1.0kg/cm2Gを維持するように連続的に導入
し、2.0時間重合を行った。反応後、メタノールにより
触媒成分を分解し、得らてたポリマーを乾燥した。この
結果ポリマーが4.0g得られ、I.I.は96であった。Example 4 500 ml of purified toluene was added to a sus autoclave having an internal volume of 1.5 L, which had been sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the above-mentioned method (A) was 0.06 mmo as Ti component.
1, and 1,3-propanedinylbis (indenyl) titanium dimethyl (0.59 mmol) were sequentially added, and the temperature was raised to 30 ° C. The mixture was stirred at this temperature for 1 hour, and then propylene was continuously introduced into this so that the total pressure was maintained at 1.0 kg / cm 2 G, and polymerization was carried out for 2.0 hours. After the reaction, the catalyst component was decomposed with methanol, and the obtained polymer was dried. As a result, 4.0 g of a polymer was obtained, and II was 96.
実施例5 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製トルエン500ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.07mmo
l、および1,3−プロパンジニルビス(インデニル)チタ
ニウムジメチル0.68mmolを順次添加し、30℃に昇温し
た。この温尾で1時間撹拌し、次いで、これにプロピレ
ンを全圧が1.0kg/cm2Gを維持するように連続的に導入
し、4.0時間重合を行った。反応後、メタノールにより
触媒乾燥を分解し、得られたポリマーを乾燥した。この
結果ポリマーが8.2g得られ、I.I.は95であった。Example 5 500 ml of purified toluene in a sus autoclave with an internal volume of 1.5 L that had been sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the method (A) above was 0.07 mmo as Ti component.
1, and 1,3-propanedinylbis (indenyl) titanium dimethyl (0.68 mmol) were sequentially added, and the temperature was raised to 30 ° C. The mixture was stirred for 1 hour with this warm tail, and then propylene was continuously introduced into this so that the total pressure was maintained at 1.0 kg / cm 2 G, and polymerization was carried out for 4.0 hours. After the reaction, the catalyst dried was decomposed with methanol, and the obtained polymer was dried. As a result, 8.2 g of a polymer was obtained, and II was 95.
比較例1 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製ヘキサン700ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.05mmo
l、およびトリエチルアルミニウム0.49mmolを順次添加
し、30℃に昇温した。この温度で1時間撹拌し、次い
で、これにプロピレンを全圧が1.0kg/cm2Gを維持するよ
うに連続的に導入し、2.0時間重合を行った。反応後、
メタノールにより触媒成分を分解し、得られたポリマー
を乾燥した。この結果ポリマーが19.2g得られ、I.I.は7
5であった。Comparative Example 1 700 ml of purified hexane was added to an autoclave made of sus having an internal volume of 1.5 L, which was sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the method (A) was used as a Ti component in an amount of 0.05 mmo.
1, and triethylaluminum 0.49 mmol were sequentially added, and the temperature was raised to 30 ° C. The mixture was stirred at this temperature for 1 hour, and then propylene was continuously introduced into this so that the total pressure was maintained at 1.0 kg / cm 2 G, and polymerization was carried out for 2.0 hours. After the reaction
The catalyst component was decomposed with methanol, and the obtained polymer was dried. As a result, 19.2 g of polymer was obtained, and II was 7
Was 5.
比較例2 充分に窒素置換した内容積1.5Lのsus製オートクレーブ
に精製ヘキサン700ml、前述(A)の方法により調製し
たMg化合物担持型チタン系固体成分をTi成分で0.06mmo
l、およびジエチルアルミニウムクロライド0.60mmolを
順次添加し、30℃に昇温した。この温度で1時間撹拌
し、次いで、これにプロピレンを全圧が1.0kg/cm2Gを維
持するように連続的に導入し、2.0時間重合を行った。
反応後、メタノールにより触媒成分を分解し、得られた
ポリマーを乾燥した。この結果ポリマーが9.2g得られ、
I.I.は60であった。Comparative Example 2 700 ml of purified hexane was added to a sus autoclave with an internal volume of 1.5 L that had been sufficiently replaced with nitrogen, and the Mg compound-supported titanium-based solid component prepared by the above-mentioned method (A) was used as a Ti component at 0.06 mmo.
1 and 0.60 mmol of diethylaluminum chloride were sequentially added, and the temperature was raised to 30 ° C. The mixture was stirred at this temperature for 1 hour, and then propylene was continuously introduced into this so that the total pressure was maintained at 1.0 kg / cm 2 G, and polymerization was carried out for 2.0 hours.
After the reaction, the catalyst component was decomposed with methanol, and the obtained polymer was dried. As a result, 9.2 g of a polymer was obtained,
The II was 60.
第1図は、本発明の方法の工程を説明するフローシート
である。 第2図は、本発明に係るチタン系固体成分の製造工程を
説明するフローシートである。FIG. 1 is a flow sheet illustrating the steps of the method of the present invention. FIG. 2 is a flow sheet for explaining the production process of the titanium-based solid component according to the present invention.
Claims (3)
造されたMg化合物に担持されたチタン系固体成分、及び I.無水マグネシウムジハライド、一般式Ti(OR1)4
で表わされるオルトチタン酸エステルおよび/または一
般式R2O−Ti(OR3)(OR4)mO−R5で表わされるポ
リチタン酸エステルからなる(ここでR1、R2、R3、R4お
よびR5は炭素数1〜20のアルキル基、アリール基または
炭素数3〜20のシクロアルキル基であり、mは2〜20の
数である)、および炭素数1ないし20の飽和若しくは
不飽和の1価若しくは多価アルコールを不活性炭化水
素溶剤中で混合して溶解させて(成分A)を得、 II.該(成分A)に、炭素数2ないし24の脂肪族若しく
は芳香族のモノ若しくはポリカルボン酸エステル(以下
有機酸エステルという)、一般式AlXnR8 3-n(ここ
で、XはClまたはBr、R8は炭素数3〜20のシクロアルキ
ル基、nは0〜3の数である)で表わされるハロゲン化
アルミニウム、および一般式SiXlR▲6 4-l若しくはSiX
p(OR7)4-p(ここで、XはClまたはBr、R6およびR7は
それぞれ炭素数1〜20のアルキル基、アリール基または
炭素数3〜20のシクロアルキル基、lまたはpは1〜4
の数である)で表わされるハロゲン化ケイ素からなる
(成分B)を混合反応させて固体(以下固体生成物
(I)という)を析出させ、 III.該固体生成物(I)に、一般式TiXq(OR9)4-q(こ
こで、XはClまたはBr、R9は炭素数1〜20のアルキル
基、アリール基または炭素数3〜20のシクロアルキル基
であり、qは1〜4の数である)で表わされ、ハロゲン
化チタンおよび/または一般式VOXs(OR10)3-s若し
くはVXt(OR11)4-tで表わされるハロゲン化バナジル若
しくはハロゲン化バナジウムからなる(成分C)を反
応させて固体(以下固体生成物(II)という)を収得す
る反応。 (B)インデニル基及びその部分水素化物から選ばれた
2個の基が低級アルキル基を介して結合したブリッジ型
化合物を2座配位子として有するチタニウムジアルキル
化合物、 を成分とする触媒を用いてオレフィンを重合することを
特徴とするオレフィン重合体の製造方法。1. (A) A titanium-based solid component supported on a Mg compound produced through the following reactions of steps I to III, and I. anhydrous magnesium dihalide, a general formula Ti (OR 1 ) 4
In ortho titanate represented and / or the general formula R 2 O-Ti (OR 3 ) (OR 4) m consists polytitanic acid ester represented by OR 5 (wherein R 1, R 2, R 3 , R 4 and R 5 are an alkyl group having 1 to 20 carbon atoms, an aryl group or a cycloalkyl group having 3 to 20 carbon atoms, m is a number of 2 to 20), and a saturated group having 1 to 20 carbon atoms or An unsaturated monohydric or polyhydric alcohol is mixed and dissolved in an inert hydrocarbon solvent to obtain (Component A). II. The (Component A) contains an aliphatic or aromatic group having 2 to 24 carbon atoms. A mono- or polycarboxylic acid ester (hereinafter referred to as an organic acid ester) of the general formula AlX n R 8 3-n (wherein X is Cl or Br, R 8 is a cycloalkyl group having 3 to 20 carbon atoms, and n is 0). To a number of 3), and an aluminum halide represented by the general formula SiX l R ▲ 6 4-l SiX
p (OR 7 ) 4-p (wherein X is Cl or Br, R 6 and R 7 are each an alkyl group having 1 to 20 carbon atoms, an aryl group or a cycloalkyl group having 3 to 20 carbon atoms, l or p Is 1 to 4
A component (hereinafter referred to as solid product (I)) consisting of a silicon halide represented by the general formula: III. TiX q (OR 9 ) 4-q (wherein X is Cl or Br, R 9 is an alkyl group having 1 to 20 carbon atoms, an aryl group or a cycloalkyl group having 3 to 20 carbon atoms, and q is 1 to 4) and is composed of titanium halide and / or vanadyl halide or vanadium halide represented by the general formula VOX s (OR 10 ) 3-s or VX t (OR 11 ) 4-t. (Component C) is reacted to obtain a solid (hereinafter referred to as a solid product (II)). (B) A titanium dialkyl compound having as a bidentate ligand a bridge-type compound in which two groups selected from an indenyl group and a partial hydride thereof are bonded via a lower alkyl group. A method for producing an olefin polymer, which comprises polymerizing an olefin.
チレンビス(インデニル)チタニウムジメチルである特
許請求の範囲第(1)項記載の方法。2. The method according to claim 1, wherein the titanium dialkyl compound (B) is ethylenebis (indenyl) titanium dimethyl.
3−プロパンジニルビス(インデニル)チタニウムジメ
チルである特許請求の範囲第(1)項記載の方法。3. The (B) titanium dialkyl compound is 1,
The method according to claim 1, which is 3-propanedinylbis (indenyl) titanium dimethyl.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19243187A JPH0745543B2 (en) | 1987-07-31 | 1987-07-31 | Process for producing olefin polymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19243187A JPH0745543B2 (en) | 1987-07-31 | 1987-07-31 | Process for producing olefin polymer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6436606A JPS6436606A (en) | 1989-02-07 |
| JPH0745543B2 true JPH0745543B2 (en) | 1995-05-17 |
Family
ID=16291196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19243187A Expired - Lifetime JPH0745543B2 (en) | 1987-07-31 | 1987-07-31 | Process for producing olefin polymer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0745543B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02206604A (en) * | 1989-02-03 | 1990-08-16 | Showa Denko Kk | Polymerization of olefin |
| ATE300549T1 (en) * | 1998-11-20 | 2005-08-15 | Basell Polyolefine Gmbh | BRIDGED METALLOCENES, PRODUCTION AND USE AS OLEFIN POLYMERIZATION CATALYST |
-
1987
- 1987-07-31 JP JP19243187A patent/JPH0745543B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6436606A (en) | 1989-02-07 |
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