CN103694385A - Propylene polymerization catalytic component and catalyst thereof - Google Patents

Propylene polymerization catalytic component and catalyst thereof Download PDF

Info

Publication number
CN103694385A
CN103694385A CN201210366655.1A CN201210366655A CN103694385A CN 103694385 A CN103694385 A CN 103694385A CN 201210366655 A CN201210366655 A CN 201210366655A CN 103694385 A CN103694385 A CN 103694385A
Authority
CN
China
Prior art keywords
hydrazides
phenyl
ethylphenyl
butyl
aminomethyl phenyl
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
Application number
CN201210366655.1A
Other languages
Chinese (zh)
Other versions
CN103694385B (en
Inventor
刘强
朱博超
李振宇
贾军纪
李振昊
杨世元
金鼎铭
王霞
黄安平
邓守军
宋赛楠
谢克锋
王丹丹
王海
刘小燕
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.)
China Petroleum and Natural Gas Co Ltd
Original Assignee
China Petroleum and Natural Gas 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 China Petroleum and Natural Gas Co Ltd filed Critical China Petroleum and Natural Gas Co Ltd
Priority to CN201210366655.1A priority Critical patent/CN103694385B/en
Publication of CN103694385A publication Critical patent/CN103694385A/en
Application granted granted Critical
Publication of CN103694385B publication Critical patent/CN103694385B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses a propylene polymerization catalytic component and a catalyst thereof. The propylene polymerization catalytic component is mainly composed of a spherical magnesium halide alcohol compound, titanium halide and an internal electron donor compound, wherein the internal electron donor compound is a mixture of diphenyl amide represented by the formula (I) and diester represented by the formula (II), and the molar ratio of diphenyl amide to diester is 0.5:1 to 2.2:1; according to the weight percentage, the catalytic component contains 10-25% of magnesium, 1-10% of titanium, 40-60% of halogen and 1-30% of an internal donor. The propylene polymerization catalyst is composed of the catalytic component, an alkyl aluminum compound and an organosilicon compound; and when being used in propylene (co) polymerization, the catalyst has higher catalytic activity, good hydrogen response, and allows a polymer to maintain high stereospecificity and broad molecular weight distribution.

Description

Propylene polymerization catalyst component and catalyzer thereof
Technical field
The present invention relates to a kind of propylene polymerization catalyst component and catalyzer thereof, be specifically related to propylene polymerization catalyst component and catalyzer thereof containing solid titanium.
Background technology
Polypropylene is a kind of important polyolefin products.Most of alkene, particularly propylene (being total to) polymerization is caused by take the Ziegler-Natta catalyst that magnesium, titanium, halogen and electron donor be component, and the polymerisate taxis obtaining is good.In catalyst component, internal electron donor is very important component, very large on the impact of catalyst performance.
Existing bibliographical information multiple internal electron donor, if monoesters class, diester class, two ethers, diones, succinate compound and alkoxide etc. are containing the compound of carbonyl, CN85100997A has adopted diisobutyl phthalate; CN1473809, CN1376722, CN1298887, CN1268957, CN1143651, CN1141303, CN1141285, CN1066723, EP0728770, EP0728724, EP0361493, US5095153, US5068213, US4978648 etc. have adopted 1,3-diether compound, the substituting group that the substituting group that in this compound, on carbon atom, spatial volume is large and symmetry are higher is conducive to the raising of catalytic activity and polymkeric substance degree of isotacticity; CN101628951A has adopted succinic diamide compounds; CN1681853, CN1398270, CN1313869, US0050014631, WO00/63261, WO2004024785 etc. have adopted succinate compounds, the catalyzer of preparing with this compound is during for propylene polymerization, catalyst activity obviously increases, and gained polypropylene molecule amount distributes and obviously widens.
Summary of the invention
A kind of propylene polymerization catalyst component and catalyzer thereof have been the object of this invention is to provide.
Propylene polymerization catalyst component of the present invention, mainly by spherical magnesium halide alcohol polymer, halogenated titanium, internal electron donor compound, formed, it is characterized in that internal electron donor compound is the mixture of two phenyl amides of formula I and the diester of formula II, both mol ratios are 0.5:1~2.2:1
Figure BDA00002202744000021
Substituent R in formula I 1, R 2, R 3, R 4, R 5, R 6, R 7, R 8, R 9, R 10, R 11, R 12identical or different, be selected from H, halogen atom, C 1~C 20straight or branched alkyl, C 3~C 20cycloalkyl, C 6~C 20aryl or C 7~C 20aralkyl;
Substituent R in formula II 13, R 14, R 15, R 16, R 17, R 18identical or different, be selected from H, C 1~C 20straight or branched alkyl;
By weight percentage, catalyst component comprises 10~25% magnesium, 1~10% titanium, 40~60% halogens and 1~30% internal electron donor.
The synthetic of described general formula compound (I) can adopt known method, and main process is: by p-methylbenzoic acid or derivatives thereof and excessive dehydrated alcohol reflux 1~25 hour under acidic conditions, preferably 2~20 hours; Excessive ethanol is removed in distillation, obtains crude product and adds excessive hydrazine hydrate or derivatives thereof to it, stirring and refluxing 1~25 hour, preferably 2~20 hours, filtration, washing, dry, recrystallization; Again by solids and Benzoyl chloride or derivatives thereof reflux 1~15 hour in anhydrous pyridine solution, preferably 2~10 hours, through cooling, filter, washing, dry, recrystallization obtains.
The example of suitable general formula compound (I) includes but not limited to:
Two-(2 '-aminomethyl phenyl) hydrazides, two-(3 '-aminomethyl phenyl)-hydrazides, two-(4 '-aminomethyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-aminomethyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-aminomethyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-ethylphenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-ethylphenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-ethylphenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, two-(2 '-ethylphenyl)-hydrazides, two-(3 '-ethylphenyl)-hydrazides, two-(4 '-ethylphenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides or 1-(4 '-ethylphenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides.
Formula II compound is selected from wherein a kind of of diisobutyl phthalate, diethyl phthalate or n-butyl phthalate, and can be directly commercially available.
Magnesium halide alcohol adduct in catalyst component meets formula M g (OR') mx (2-m)nROH, in formula, R' is C 1~C 20alkyl, aralkyl or aryl; X is halogen; M is the integer of 0≤m<2; N is decimal or the integer of 0<n<6; R is C 1~C 20alkyl, aralkyl or aryl.
Magnesium halide in magnesium halide alcohol adduct is selected from a kind of in magnesium dichloride, dibrominated magnesium, chloro magnesium methylate or chloro magnesium ethylate, preferably magnesium dichloride; Alcohol in magnesium halide alcohol adduct is selected from a kind of in methyl alcohol, ethanol, n-propyl alcohol, Virahol, propyl carbinol or isopropylcarbinol, preferred alcohol.
The preparation of magnesium halide alcohol adduct adopts magnesium halide and alcohol to heat altogether after melting, and high pressure ejection or high-speed stirring are solidified into microballoon and obtain in heat-eliminating medium, and concrete steps are referring to the associated description in CN1091748A.
Halogenated titanium general formula in catalyst component is Ti (OR) px (4-p), in formula, R is C 1~C 20alkyl, aryl or aralkyl; X is halogen; P is the integer of 0≤p < 4.Specifically be selected from wherein a kind of of purity titanium tetraethoxide, four titanium butoxide, chloro tri-alkoxy titanium, dichloro dialkoxy titanium, trichlorine titan-alkoxide, titanium tetrachloride or titanium tetrabromide, preferably titanium tetrachloride.
In addition, the invention provides a kind of preparation method of described catalyst component, process comprises: (1) joins spherical magnesium halide alcohol polymer-50~20 ℃, preferably, in the halogenated titanium of-30~0 ℃, reacts 1~4 hour, and the mol ratio of magnesium and titanium is 1:5~1:50; (2) be warming up to 30~80 ℃, add the mixture of two phenyl amides and diester, mol ratio is 0.5:1~2.2:1, preferred 1:1, and the mol ratio of magnesium and internal electron donor mixture is 2:1~15:1; (3) be warming up to again 100~150 ℃, react 1~4 hour; (4) add the titanium compound with step (1) same amount after filtering, in 110~130 ℃ of reactions 1~4 hour, more after filtration, washing, obtains after dry again.
Above-mentioned catalyst component also needs to add alkylaluminium cpd promotor and external electron donor to form catalyzer for propylene polymerization.Alkylaluminium cpd is selected from the mixture of trialkylaluminium, trialkylaluminium and aluminum alkyl halide or alkyl aluminum hydride, or alkylaluminoxane.
External electron donor can be selected silicoorganic compound, as: trimethylammonium methoxy silane, trimethylethoxysilane, dimethyldimethoxysil,ne, dimethyldiethoxysilane, dimethoxydiphenylsilane, phenylbenzene diethoxy silane, phenyl triethoxysilane, phenyltrimethoxysila,e, vinyltrimethoxy silane, Cyclohexyl Methyl Dimethoxysilane, methyl-t-butyldimethoxysilane, diisopropyl dimethoxy silane, second, isobutyl dimethoxy silane, di-n-butyl dimethoxy silane, dicyclopentyl dimethoxyl silane or two (cyclobutylmethyl) dimethoxy silane, preferred Cyclohexyl Methyl Dimethoxysilane, dimethoxydiphenylsilane, diisopropyl dimethoxy silane, second, isobutyl dimethoxy silane, di-n-butyl dimethoxy silane, dicyclopentyl dimethoxyl silane or two (cyclobutylmethyl) dimethoxy silane.
With titanium: aluminium: the molar ratio computing between external donor compound, the amount ratio in catalyzer between each component is 1:1~2000:1~50; Be preferably 1:1~500:1~20.
Catalyst component of the present invention, for the equal polymerization of propylene and the copolymerization of propylene and other alkene, can access the polymkeric substance that isotactic index is very high.Meanwhile, do not get rid of yet and be applicable to produce polyethylene and ethene and alpha-olefin as the copolymerization of propylene, 1-butylene, 1-amylene, 4-methyl-1-pentene, 1-hexene or 1-octene.
During for propylene polymerization, can adopt the whole bag of tricks of the prior art, can in liquid phase or gas phase, carry out, also can under the combination operation of liquid and gas polymerization stage, carry out.Polymerization is carried out at 0~150 ℃ conventionally, and preferably 40~90 ℃, polymerization pressure is 0.01~10MPa.Adopt hydrogen or other compound to control the molecular weight of polymkeric substance.
In catalyst component provided by the invention, two kinds of specific interior electronics of giving are as the efficient component of alkene polypropylene catalyst, during for propylene (being total to) polymerization, catalyzer has higher catalytic activity, and hydrogen response is good, and polymkeric substance keeps high tacticity and wide molecular weight distribution.
Embodiment
Embodiment given below is for the present invention rather than limitation of the present invention are described better.
Testing method
1, polymericular weight and molecular weight distribution MWD: adopt gel permeation chromatography method, with Alliance-GPCV2000, take orthodichlorobenzene and at 135 ℃, measure as solvent.
2, polymkeric substance degree of isotacticity: adopt heptane extraction process to measure (heptane boiling extracting 8 hours), i.e. 1 gram of dry polymer samples, be placed in extractor and use the extracting of boiling heptane after 8 hours, the polymer weight (g) that residuum is dried to constant weight gained is degree of isotacticity with 1 ratio.
3, the mensuration of melt index: measure according to μ PXRZ-400C.
4, the mensuration of titanium percentage composition: according to spectrophotometry.
5, the mensuration of internal electron donor percentage composition: according to the AutosystemXL of PE company gas chromatograph for determination.
Embodiment
One, two phenyl amide compounds is synthetic
Only, with the example that synthesizes of 1-(4 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, concrete method is as follows:
(1) synthesizing toluyl hydrazine
Figure BDA00002202744000061
10g p-methylbenzoic acid is dissolved in to 200mL dehydrated alcohol completely, and by 5mL H 2sO 4slowly drop in reaction flask stirring and refluxing 20h.Excessive ethanol is removed in distillation, obtains crude product ethyl p-methyl benzoate.In crude product, add excessive hydrazine hydrate (20mL), stirring and refluxing 15h at 80 ℃.Product is filtered, washing, dry, then use recrystallizing methanol, obtain white solid 9.15g, yield 84%.
(2) 1-(4 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides is synthetic
At 0 ℃, 13.2g is dissolved in 100mL anhydrous pyridine solution, at N toluyl hydrazine 2the lower 4-tert.-butylbenzene formyl chloride 17.3g that drips of protection, drips and finishes rear temperature rising reflux 5h.After reaction finishes, be cooled to room temperature, mixture is slowly poured in 200mL frozen water, occur a large amount of white precipitates.Filter water repetitive scrubbing several, vacuum-drying.Crude product, through recrystallizing methanol, obtains white solid 22.45g, and yield is 78%, m.p.237-238 ℃ of .IR (KBr pellet, cm-1): 3218 (N-H), 2961 (Alkyl-CH), 1635 (C=O), 1540 (C-N), 1499,1277,1114,843,749.
Two, the preparation of catalyzer
Embodiment 1-33
Under anhydrous and oxygen-free condition, by 100mlTiCl 4be added in 500ml round-bottomed flask, be cooled to-20 ℃, add 10gMgCl 22.8CH 3cH 2oH ball type carrier, constant temperature 1h.With 2h, be slowly warming up to 60 ℃, add respectively the mixture 7.4mmol of corresponding two kinds of internal electron donors in table 1, with 2h, be slowly warming up to 120 ℃, constant temperature 2h at 120 ℃.Pump filtrate, again add 100mlTiCl 4, constant temperature 2h at 120 ℃.Pump filtrate, at 50 ℃, each 60ml anhydrous hexane solid ingredient of using, washs 3 times, at normal temperatures, washs 3 times, obtains solid catalyst after vacuum-drying.
Comparative example 1-5
By the method for above-described embodiment, prepare spherical catalyst component, internal electron donor is replaced with to two-(2 '-aminomethyl phenyl) hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-aminomethyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, phthalic acid two isobutyl fat, the positive fourth fat of phthalic acid two.
Three, propylene polymerization experiment
The catalyzer of above-described embodiment 1-33 and comparative example 1-5 is carried out respectively to propylene polymerization.First, after the stainless steel autoclave of 5L fully being replaced with high pure nitrogen, add AlEt 32.5mmol, external electron donor Cyclohexylmethyldimethoxysilane (CHMMS) 0.1mmol, then add ingredient of solid catalyst 10mg and the 1.2L hydrogen of above-described embodiment 1-33 and comparative example 1-5, and pass into liquid propene 2.3L, be warming up to 70 ℃, reaction 1h.Cooling, pressure release, obtains PP powder.Polymerization result is listed in table 1.
Table 1 propylene polymerization result
Figure BDA00002202744000081
Figure BDA00002202744000091
Figure BDA00002202744000101
Four, vinyl polymerization experiment
Volume is the stainless steel autoclave of 10L, after high pure nitrogen is fully replaced, starts stirring, under nitrogen protection progressively to the catalyst solid constituent and the 5.0mmol promotor AlEt that add 2L hexane, 20mg embodiment 1 gained in still 3be warming up to after 75 ℃, in still, supplement appropriate high-purity hydrogen, making hydrogen partial pressure in still is 0.3Mpa, and in 5 minutes backward stills, make-up ethylene gas makes its dividing potential drop reach 0.75Mpa, the dividing potential drop that maintains ethylene gas is constant, make system temperature keep 80 ℃, after 3 hours, cooling discharge, polymkeric substance, except desolventizing, is obtained to polyethylene 560g after being fully dried.
Five, ethene and copolymerization of propylene experiment
Volume is the stainless steel autoclave of 10L, after high pure nitrogen is fully replaced, starts stirring, under nitrogen protection progressively to the catalyst solid constituent and the 5.0mmol promotor AlEt that add 2L hexane, 20mg embodiment 1 gained in still 3pass into liquid propene 2.5L, be warming up to after 75 ℃, in still, supplement appropriate high-purity hydrogen, making hydrogen partial pressure in still is 0.3Mpa, in 5 minutes backward stills, make-up ethylene gas makes its dividing potential drop reach 0.75Mpa, and the dividing potential drop that maintains ethylene gas is constant, makes system temperature keep 80 ℃, after 3 hours, cooling discharge, except desolventizing, obtains polymer powders 846g after being fully dried by polymkeric substance.

Claims (11)

1. propylene polymerization catalyst component, mainly by spherical magnesium halide alcohol polymer, halogenated titanium, internal electron donor compound, formed, it is characterized in that internal electron donor compound is the mixture of two phenyl amides of formula (I) and the diester of formula II, both mol ratios are 0.5:1~2.2:1
Figure FDA00002202743900011
Substituent R in formula (I) 1, R 2, R 3, R 4, R 5, R 6, R 7, R 8, R 9, R 10, R 11, R 12identical or different, be selected from H, halogen atom, C 1~C 20straight or branched alkyl, C 3~C 20cycloalkyl, C 6~C 20aryl or C 7~C 20aralkyl;
Substituent R in formula II 13, R 14, R 15, R 16, R 17, R 18identical or different, be selected from H, C 1~C 20straight or branched alkyl;
By weight percentage, catalyst component comprises 10~25% magnesium, 1~10% titanium, 40~60% halogens and 1~30% internal electron donor.
2. catalyst component according to claim 1, is characterized in that formula (I) compound is selected from two-(2 '-aminomethyl phenyl) hydrazides, two-(3 '-aminomethyl phenyl)-hydrazides, two-(4 '-aminomethyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-aminomethyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-aminomethyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-ethylphenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-ethylphenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-ethylphenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-aminomethyl phenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, two-(2 '-ethylphenyl)-hydrazides, two-(3 '-ethylphenyl)-hydrazides, two-(4 '-ethylphenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-ethylphenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-ethylphenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-propyl group phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-propyl group phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-propyl group phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-isopropyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-isopropyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-isopropyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-butyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-butyl phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-butyl phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-isobutyl phenenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-isobutyl phenenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(4 '-isobutyl phenenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(2 '-ethylphenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides, 1-(3 '-ethylphenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(2 '-tert-butyl-phenyl)-hydrazides, 1-(4 '-ethylphenyl)-2-(3 '-tert-butyl-phenyl)-hydrazides or 1-(4 '-ethylphenyl)-2-(4 '-tert-butyl-phenyl)-hydrazides.
3. catalyst component according to claim 1, is characterized in that formula (II) compound is selected from wherein a kind of of diisobutyl phthalate, diethyl phthalate or n-butyl phthalate.
4. catalyst component according to claim 1, is characterized in that described magnesium halide alcohol adduct meets formula M g (OR') mx (2-m)nROH, in formula, R' is C 1~C 20alkyl, aralkyl or aryl; X is halogen; M is the integer of 0≤m<2; N is decimal or the integer of 0<n<6; R is C 1~C 20alkyl, aralkyl or aryl.
5. catalyst component according to claim 4, is characterized in that magnesium halide in described magnesium halide alcohol adduct is selected from a kind of in magnesium dichloride, dibrominated magnesium, chloro magnesium methylate or chloro magnesium ethylate; Alcohol in magnesium halide alcohol adduct is selected from a kind of in methyl alcohol, ethanol, n-propyl alcohol, Virahol, propyl carbinol or isopropylcarbinol.
6. catalyst component according to claim 1, is characterized in that described halogenated titanium general formula is Ti (OR) px (4-p), in formula, R is C 1~C 20alkyl, aryl or aralkyl; X is halogen; P is the integer of 0≤p < 4.
7. catalyst component according to claim 6, is characterized in that described halogenated titanium is selected from wherein a kind of of purity titanium tetraethoxide, four titanium butoxide, chloro tri-alkoxy titanium, dichloro dialkoxy titanium, trichlorine titan-alkoxide, titanium tetrachloride or titanium tetrabromide.
8. a catalyst for polymerization of propylene that comprises catalyst component described in claim 1, is characterized in that catalyzer forms to comprise:
1) catalyst component claimed in claim 1;
2) alkylaluminium cpd;
3) silicoorganic compound,
With titanium: aluminium: the molar ratio computing between external donor compound, the amount ratio in catalyzer between each component is 1:1~2000:1~50.
9. catalyst for polymerization of propylene according to claim 8, is characterized in that alkylaluminium cpd is selected from the mixture of trialkylaluminium, trialkylaluminium and aluminum alkyl halide or alkyl aluminum hydride, or alkylaluminoxane.
10. catalyst for polymerization of propylene according to claim 8, is characterized in that silicoorganic compound are selected from Cyclohexyl Methyl Dimethoxysilane, dimethoxydiphenylsilane, diisopropyl dimethoxy silane, second, isobutyl dimethoxy silane, di-n-butyl dimethoxy silane, dicyclopentyl dimethoxyl silane or two (cyclobutylmethyl) dimethoxy silane.
11. catalyst for polymerization of propylene according to claim 8, is characterized in that in catalyzer, the amount ratio between each component is 1:1~500:1~20.
CN201210366655.1A 2012-09-28 2012-09-28 Propylene polymerization catalytic component and catalyzer thereof Active CN103694385B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210366655.1A CN103694385B (en) 2012-09-28 2012-09-28 Propylene polymerization catalytic component and catalyzer thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210366655.1A CN103694385B (en) 2012-09-28 2012-09-28 Propylene polymerization catalytic component and catalyzer thereof

Publications (2)

Publication Number Publication Date
CN103694385A true CN103694385A (en) 2014-04-02
CN103694385B CN103694385B (en) 2016-03-09

Family

ID=50356064

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210366655.1A Active CN103694385B (en) 2012-09-28 2012-09-28 Propylene polymerization catalytic component and catalyzer thereof

Country Status (1)

Country Link
CN (1) CN103694385B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105985464A (en) * 2015-03-05 2016-10-05 中国石油天然气股份有限公司 Olefin polymerization solid catalyst component and catalyst thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4985461A (en) * 1985-10-21 1991-01-15 Rohm And Haas Company Insecticidal N'-substituted-N,N'-diacylhydrazines
EP0639559A1 (en) * 1993-08-19 1995-02-22 Rohm And Haas Company Preparation of 1,2-diacyl-2-(t-alkyl)hydrazines
CN1435411A (en) * 2002-02-01 2003-08-13 珠海真绿色技术有限公司 Process for preparing N.N'-diacyl-N'-t-butyl hydrazine
CN1486994A (en) * 2003-09-04 2004-04-07 中国石油化工股份有限公司 Ethylene polymerization catalyst system and its prepn and use
CN101824107A (en) * 2009-03-04 2010-09-08 中国石油天然气股份有限公司 Solid main catalyst for olefin polymerization

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4985461A (en) * 1985-10-21 1991-01-15 Rohm And Haas Company Insecticidal N'-substituted-N,N'-diacylhydrazines
EP0639559A1 (en) * 1993-08-19 1995-02-22 Rohm And Haas Company Preparation of 1,2-diacyl-2-(t-alkyl)hydrazines
CN1435411A (en) * 2002-02-01 2003-08-13 珠海真绿色技术有限公司 Process for preparing N.N'-diacyl-N'-t-butyl hydrazine
CN1486994A (en) * 2003-09-04 2004-04-07 中国石油化工股份有限公司 Ethylene polymerization catalyst system and its prepn and use
CN101824107A (en) * 2009-03-04 2010-09-08 中国石油天然气股份有限公司 Solid main catalyst for olefin polymerization

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
温笑菁 等: "丙烯等规聚合Ziegler-Natta催化剂体系中给电子体化合物的研究进展", 《高分子通报》, no. 6, 15 June 2010 (2010-06-15) *
肖士镜 等: "《烯烃配位聚合催化剂及聚烯烃》", 31 December 2002, article "TiCl4/给电子体的相互作用,内给电子体的作用", pages: 22 - 72 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105985464A (en) * 2015-03-05 2016-10-05 中国石油天然气股份有限公司 Olefin polymerization solid catalyst component and catalyst thereof
CN105985464B (en) * 2015-03-05 2018-04-03 中国石油天然气股份有限公司 Olefin polymerization solid catalyst component and its catalyst

Also Published As

Publication number Publication date
CN103694385B (en) 2016-03-09

Similar Documents

Publication Publication Date Title
US9321857B2 (en) Carrier for olefin polymerization catalyst, preparation method and application thereof
EP2562189B9 (en) Catalyst component for olefin polymerization reaction and catalyst comprising same
CN101824106B (en) Catalytic component for olefin polymerization and catalyst thereof
EP3533776B1 (en) Magnesium alkoxide particle and application thereof
EP4038108A1 (en) Process for polymerization of polypropylene using ziegler-natta procatalyst with novel 1,3-diether internal electron donors
CN103772557A (en) Preparation method for high isotactic polybutene-1
CN101628951B (en) Olefin polymerization solid catalytic component and catalyst thereof
CN105492469A (en) Catalyst components for the polymerization of olefins
CN101747455B (en) Load type olefin polymerization main catalyst and preparation method thereof
CN101423571A (en) Catalyst component for olefin polymerization and catalyst thereof
CN105985464B (en) Olefin polymerization solid catalyst component and its catalyst
CN101824108B (en) Ziegler-Natta catalyst
CN103694385B (en) Propylene polymerization catalytic component and catalyzer thereof
CN101423570B (en) Spherical catalyst component for olefin polymerization and catalyst thereof
EP2644627B1 (en) Catalyst for polymerization of olefins comprising thienyl-substituted silanes
CN103539874B (en) Olefin polymerization solid titanium catalyst and preparation method thereof
CN101423572B (en) Catalyst component for olefin polymerization and catalyst thereof
CN102268109B (en) Solid titanium catalyst for olefin polymerization
CN101671409B (en) Olefin polymerization solid catalyst
CN102268110B (en) Olefine polymerization catalyst component
CN101831016B (en) Olefin polymerization catalytic component and catalyst thereof
CN101671408B (en) Propylene polymerization solid catalyst composition
CN101824105B (en) Solid titanium catalytic component and catalyst
CN103145893A (en) Preparation method of ultra-high-molecular-weight polyethylene catalyst
CN101735354B (en) Method for preparing beta-crystal form polypropylene resin by in-situ polymerization

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant