CN1844177A - Polypropylene block copolymer and its preparation process and use - Google Patents
Polypropylene block copolymer and its preparation process and use Download PDFInfo
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- CN1844177A CN1844177A CN 200510063210 CN200510063210A CN1844177A CN 1844177 A CN1844177 A CN 1844177A CN 200510063210 CN200510063210 CN 200510063210 CN 200510063210 A CN200510063210 A CN 200510063210A CN 1844177 A CN1844177 A CN 1844177A
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Abstract
This invention is the preparation method and application of polypropylene block copolymer. Polypropylene block copolymer's structure is depicted as followings. m is integer between 100-100000,and n is integer between 10-5000. R1 is H or methyl; R2 is phenyl group, p-tolunitrile, -OCOCH3,-CONH2,-CN or -COOR, R is acroleic acid. Polypropylene block copolymer reported here is characteristic with flexible molecule weight and narrow range. It also has a high fusion temperature and high crystallinity. By scaning with electron scanning microscope, we could find this block copolymer could get into polypropylene and other polymers mixtures. It could change their blending consistency, is an efficient blending consistency agent.
Description
Technical field
The present invention relates to polypropylene block copolymer and preparation method thereof and application.
Background technology
Although polyolefine has higher performance and good processibility is widely used, but because polyolefine lacks reactive group, cause its cementability, relatively poor, thereby greatly limited the further application of polyolefine material with other material comixing compatibility and dyeability.Segmented copolymer and graftomer are effective compatilizers, can improve interfacial interaction (Teyssie, P., Fayt, R.and Jerome, R.Makromol.Chem.Macromol.Symp.1988,16,41 of polyolefine and other polymer materials; Favis, B.D., Can.J.Chem.Eng., 1991,69,619).
The synthesis of polyolefins segmented copolymer mainly contains two kinds of methods at present: a kind of is under Ziegler-Natta catalyst or metallocene catalyst catalysis, and two kinds of monomers carry out copolymerization (Soga K, Yanagihara H.Macromolecules, 1989,22,2875; Permitted optics, Lin Shangan, polymer journal, 1996,4 (4): 416; Permitted optics, Lin Shangan, the polymer journal, 1996,5 (5): 583), but this method is not suitable for polar monomer, and the molecular weight of polymkeric substance can not be regulated and control easily, and the product purification difficult.Second method is to utilize activity polymerizating technology, and this method can accurately be controlled the molecular weight distribution of chain length and polymkeric substance, method (the B.Lu and T.C.Chung that utilizes the polycoordination reaction to combine with active free radical polymerization as Chung etc., Macromolecules, 1999,32,2525; T.C.Chung, H.L.Lu, Polymer, 1997,38,1495), the method that combines with active anionic polymerization of polycoordination reaction prepared polypropylene block copolymer, but these method conditional request harshnesses are reacted wayward.
Summary of the invention
The objective of the invention is a kind of polypropylene block copolymer and preparation method thereof.
Polypropylene block copolymer provided by the present invention has structure shown in the formula I,
(formula I)
Wherein, m is the integer between 100～100000; N is the integer between 10～5000; R
1Be H or methyl; R
2Be phenyl, p-methylphenyl ,-OCOCH
3,-CONH
2,-CN or-COOR, R is an alkyl.
The narrow molecular weight distribution of polypropylene block copolymer of the present invention is 2-5.R is common to be methyl, ethyl, the tertiary butyl etc.
The preparation method of polypropylene block copolymer of the present invention comprises the steps:
1) the preparation end contains cinnamic polypropylene: to containing vinylbenzene, successively feed H in the organic solution of alkylaluminoxane and metallocene catalyst
2And propylene, carry out polyreaction, obtain structural formula and contain cinnamic polypropylene suc as formula the end of II;
2) preparation polypropylene-base atom transfer radical polymerization initiator: the gained end is contained cinnamic polypropylene suspension in organic solvent, add halogenated succinimide imide and thermolysis type radical initiator to aaerosol solution then, under 30～100 ℃, react, obtain the polypropylene-base atom transfer radical polymerization initiator of structural formula such as formula III;
(formula III)
M is 100～100 in the formula III, and the integer between 000, x are fluorine, chlorine, bromine or iodine;
3) the polypropylene-base atom transfer radical polymerization initiator with gained is suspended in toluene or the methyl-phenoxide, adds cuprous halide, multiple tooth nitrogenous compound and reaction monomers, in 70～150 ℃ of reactions down, obtains described polypropylene block copolymer; Described reaction monomers is vinylbenzene, p-methylstyrene, vinyl-acetic ester, third rare acid amides, Methacrylamide, vinyl cyanide, acrylate or the methacrylic ester.
Wherein, the described metallocene catalyst of step 1) is selected from one or more in the metallocene catalyst with following general formula:
(1)Me
2Si[(2-R
1，4-R
2)Ind]
2ZrCl
2
R
1=Me, R
2=i-Pr or
R
1=Et, R
2=i-Pr or
R
1=Me, R
2=benzo or
R
1=Me, R
2=1-naphthyl or
R
1=H, R
2=benzo or
R
1＝Me，R
2＝Phenyl；
(2) Me
2Si[(2-R
1) THInd]
2ZrCl
2(TH represents tetrahydrochysene, promptly on the indenyl one the ring hydrogenation and form)
R
1=Me, or Et;
(3)Me
2Si[2-R
1，5-R
2]
2ZrCl
2
R
1=Me, R
2=H or
R
1=Et, R
2=H or
R
1＝Me，R
2＝i-Pr；
(4)Me
2Si[(2-Me，4-R)(C
5H
2)]
2ZrCl
2
R=tert-Bu or
R＝i-Pr；
(5)C
2H
4(η
5-5，6-X
2Ind)
2ZrCl
2
X=4,7-Me
2, Me, H or OMe;
(6)C
2H
4(3-R)C
5H
3]
2ZrCl
2
R=Me, i-Pr or tert-Bu;
(7)Me
2Si(C
5H
5-nR
n)(C
5H
5-nR’
n)ZrCl
2
R
n=2,3,5-Me
3, R
n'=2,4,5-Me
3Or
R
n=2,4-Me
2, R
n'=3,5-Me
2Or
R
n=3-(tert-Bu), R
n'=4-(tert-Bu) or
R
n=3-Me, R
n'=4-Me or
R
n=2,4-Me
2, R
n'=3-Me, 4-Me or
R
n=3,4-Me
2, R
n'=3-Me or
R
n=3-(tert-Bu), R
n'=3-Me, 4-Me or
R
n=2,3,5-Me
3, R
n'=H or
R
n=2,4-Me
2, R
n'=H or
R
n=3-(tert-Bu), R
n'=H or
R
n＝3-Me，R
n’＝H；
(8)(Me
2Si)
2[(3，4-Me
2C
5H)]
2ZrCl
2
(9)C
2H
4(Ind)
2ZrCl
2
(10)C
2H
4(3-MeInd)
2ZrCl
2
(11)Me
2C(Ind)
2ZrCl
2
(12)Me
2Si(Ind)
2ZrCl
2
(13)Ph
2Si(Ind)
2ZrCl
2
(14)(Me)(Ph)Si(2-MeInd)
2ZrCl
2
(15)Me
2C(Ind)(C
5H
4)ZrCl
2
(16)Me
2C(Ind)(C
5H
3Me)ZrCl
2
(17)Me
2Si(2-Me-5-phenyl-Ind)
2ZrCl
2
Wherein, Me is a methyl, and Et is an ethyl, and i-Pr is a sec.-propyl, and tert-Bu is the tertiary butyl, and Ph or Phenyl are phenyl, and benzo is the benzo base, and naphthyl is a naphthyl, and Ind is an indenyl.
The solvent of step 1) organic solution can be selected from one or more in benzene,toluene,xylene, pentane, hexane and the heptane usually, is preferably toluene; Described alkylaluminoxane is methylaluminoxane, ethyl aikyiaiurnirsoxan beta or isobutyl aluminium alkoxide, is preferably methylaluminoxane.Be added with described vinylbenzene 0.1-10ml in the described organic solution of step 1) in every 100ml organic solvent, described alkylaluminoxane 0.001-100mmol, described metallocene catalyst 0.001-100 μ mol; The mol ratio of alkylaluminoxane and metallocene catalyst is 100: 1-100000: 1, be preferably 300: 1-10000: 1.
When carrying out the step 1) polyreaction, H
2Pressure is 0.01-0.3MPa, and vinylbenzene pressure is 0.1-1MPa; Described polymeric reaction temperature is 0-100 ℃, and the reaction times is 5-60 minute.
Step 2) described organic solvent is selected from one or more in tetracol phenixin, chloroform, toluene, dimethylbenzene, pentane, hexane and the heptane, is preferably tetracol phenixin; Described thermolysis type radical initiator is the special butyl ester of Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile), dibenzoyl peroxide, dilauroyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, di-isopropyl peroxydicarbonate or peroxidation phenylformic acid, is preferably Diisopropyl azodicarboxylate.Described suspension concentration is 1-60g/100ml; Halogenated succinimide imide add-on is 0.1-20g described in the described organic solvent of every 100ml, and described thermolysis type radical initiator add-on is 0.01-1g.
The described cuprous halide of step 3) is cuprous chloride, cuprous bromide or cuprous iodide, is preferably cuprous chloride; Described multiple tooth nitrogenous compound is 2,2 '-two pyridines, and 6,2 '-two pyridines, pyridine imine or pentamethyl-two vinylidene triamines are preferably pentamethyl-two vinylidene triamines.The toluene of described polypropylene-base atom transfer radical polymerization initiator or methyl-phenoxide aaerosol solution concentration are 1.0-20.0g/100ml; The cuprous halide add-on is 0.01-0.1g described in every 100ml toluene or the methyl-phenoxide, and described multiple tooth nitrogenous compound add-on is 0.02-0.1ml, and described reaction monomers add-on is 20-40g.
Another object of the present invention provides the purposes of polypropylene block copolymer of the present invention.
The inventor confirms that by experiment polypropylene block copolymer of the present invention can improve the comixing compatibility of polypropylene and other polymkeric substance, can be used as blending compatilizer and uses.
The present invention is under the condition that hydrogen exists, with vinylbenzene is chain-transfer agent, after the catalyst system catalyzing propone of forming with metallocene catalyst and alkylaluminoxane promotor carries out polyreaction, can obtain the polypropylene that end contains styrol structural unit, obtain containing polyacrylic macromole evocating agent by halogenating reaction then, under relatively mild condition, this initiator can cause atom transition free radical polymerization reaction, can be connected with other reaction monomers, make polypropylene block copolymer.Propylene segmental molecular weight in the polypropylene-base segmented copolymer of the present invention can be controlled by hydrogen, and propylene segmental taxis can be determined by selecting suitable metallocene catalyst; The quantity of another structural unit can be regulated and control by adding reaction conditionss such as monomeric concentration and reaction times in the atom transfer radical polymerization in the segmented copolymer, the gained polypropylene block copolymer has characteristics such as molecular weight adjustable height, narrow molecular weight distribution, can also keep premium propertiess such as the original high-melting-point of polypropylene, high-crystallinity.Pass through sem observation, the segmented copolymer of gained of the present invention joins in the blend of polypropylene and other polymkeric substance (as polystyrene, polymethacrylate), can obviously change their comixing compatibility, be the blending compatilizer of very effective polypropylene and other polymkeric substance.
Description of drawings
Fig. 1 is that the polypropylene block polystyrene copolymer of embodiment 1 preparation is typical
1The H-NMR spectrogram;
Fig. 2 be polypropylene and polystyrene blend (3: 1) after brittle failure, the shape appearance figure of the scanning electronic microscope of section;
Fig. 3 be add 1% embodiment, 1 preparation in polypropylene and the polystyrene blend (3: 1) polypropylene block polystyrene copolymer after brittle failure, the shape appearance figure of the scanning electronic microscope of section;
Fig. 4 be polypropylene and polymethylmethacrylate blend (3: 1) after brittle failure, the shape appearance figure of the scanning electronic microscope of section;
Fig. 5 be add 1% embodiment, 4 preparations in polypropylene and the polymethylmethacrylate blend (3: 1) polypropylene block polymethyl methacrylate copolymer after brittle failure, the shape appearance figure of the scanning electronic microscope of section.
Embodiment
One, the preparation end is the unitary polypropylene of styrene monomer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, 2ml vinylbenzene, 2.5mmol methylaluminoxane (MAO), 2.5 μ mol dimethyl-silicon abutment two (2-methyl-4-naphthyl-indenyl) zirconium dichlorides, feed 0.1MPa hydrogen earlier, feed the certain pressure propylene gas again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 35 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the terminal unitary polypropylene of styrene monomer that is.
Two, preparation polypropylene-base atom transfer radical polymerization initiator
In the 250ml there-necked flask, adding gained end contains the polypropylene 2.0g of styrol structural unit, the 100ml tetracol phenixin, 0.48g bromo-succinimide and 0.1g Diisopropyl azodicarboxylate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
Three, preparation polypropylene block polystyrene copolymer
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, 100ml methyl-phenoxide, cuprous chloride 0.03g, pentamethyl-two vinylidene triamine 0.05ml, 35g vinylbenzene, keeping temperature of reaction is 125 ℃, reacts after 30 minutes, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polystyrene copolymer.The molecular weight distribution of this multipolymer is 2.64, weight-average molecular weight be 264100g/mol (m=3110 wherein, n=1282), its
1H-NMR (deuterium is a solvent for tetrachloroethane) shows that the products therefrom structure is correct as shown in Figure 1.
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, 0.1ml vinylbenzene, 0.01mmol methylaluminoxane (MAO), 0.3 μ mol dimethyl-silicon abutment two (2-methyl-4-naphthyl-indenyl) zirconium dichloride, feed the hydrogen of 0.1MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction is at 35 ℃ of lasting 30min.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 3.0g of styrol structural unit, the 100ml tetracol phenixin, 1.0g bromo-succinimide and 0.14g Diisopropyl azodicarboxylate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 2.0g, 100ml methyl-phenoxide, cuprous chloride 0.02g, pentamethyl-two vinylidene triamine 0.02ml, the 20g p-methylstyrene, keeping temperature of reaction is 125 ℃, reacts after 1 hour, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying, it is poly-to the methylated polystyrene multipolymer to obtain the polypropylene block.
The molecular weight distribution of this multipolymer is 3.25, weight-average molecular weight be 378209g/mol (m=6546 wherein, n=867).
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds the 100ml hexane, 10ml vinylbenzene, 50mmol methylaluminoxane (MAO), the dimethyl-silicon abutment two of 50 μ mol (2-methyl-4-naphthyl-indenyl) zirconium dichloride, feed 0.1MPa hydrogen earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 10 minutes at 35 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 6.0g of styrol structural unit, 100ml toluene, 4.0g chlorosuccinimide and 0.6g di-tert-butyl peroxide, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 8.0g, 100ml toluene, cuprous bromide 0.05g, 2,2 '-two pyridine 0.1ml, vinyl-acetic ester 40g, keeping temperature of reaction is 70 ℃, react after 2 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polyvinyl acetate ester copolymer.The molecular weight distribution of this multipolymer is 3.54, weight-average molecular weight be 261896g/mol (m=2916 wherein, n=1620).
Embodiment 4, preparation polypropylene block polymethyl methacrylate copolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml dimethylbenzene, the vinylbenzene of 2ml, 2.5mmol methylaluminoxane (MAO), the dimethyl-silicon abutment two of 2.5 μ mol (2-methyl-4-naphthyl-indenyl) zirconium dichloride, feed 0.05MPa hydrogen earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 35 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 10.0g of styrol structural unit, the 100ml hexane, 7.0g bromo-succinimide and 0.8g Diisopropyl azodicarboxylate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, the 100ml methyl-phenoxide, cuprous iodide 0.07g, 6,2 '-two pyridine 0.02ml add methyl methacrylate 30g, keeping temperature of reaction is 100 ℃, react after 5 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polymethyl methacrylate copolymer.The molecular weight distribution of this multipolymer is 3.05, weight-average molecular weight be 465510g/mol (m=3461 wherein, n=3596).
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml dimethylbenzene, 0.1ml vinylbenzene, 5mmol methylaluminoxane (MAO), the dimethyl-silicon abutment two of 2.5 μ mol (2-methyl-4-naphthyl-indenyl) zirconium dichloride, feed 0.01MPa hydrogen earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 35 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 15.0g of styrol structural unit, the 100ml hexane, 8.0g bromo-succinimide and 1g Diisopropyl azodicarboxylate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 25.0g, the 100ml methyl-phenoxide, cuprous bromide 0.09g, 2,2 '-two pyridine 0.03ml add Jia Jibingxisuanyizhi 40g, keeping temperature of reaction is 100 ℃, react after 7 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polyethyl methacrylate multipolymer.The molecular weight distribution of this multipolymer is 3.85, weight-average molecular weight be 869410g/mol (m=10231 wherein, n=4268).
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml dimethylbenzene, the vinylbenzene of 1ml, 1.5mmol isobutyl aluminium alkoxide (MAO), the dimethyl-silicon abutment two of 2.5 μ mol (2-methyl-4-phenyl-indenyl) zirconium dichloride, feed 0.07MPa hydrogen earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 40 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 30.0g of styrol structural unit, 100ml, 15.0g bromo-succinimide and 1.0g Diisopropyl azodicarboxylate, 60 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 25.0g, 100ml methyl-phenoxide, cuprous iodide 0.07g, pentamethyl-two vinylidene triamine 0.05ml, add methacrylic tert-butyl acrylate 40g, keeping temperature of reaction is 100 ℃, reacts after 8 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polymethyl tert-butyl acrylate multipolymer.The molecular weight distribution of this multipolymer is 3.78, weight-average molecular weight be 753184g/mol (m=2460 wherein, n=4960).
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml benzene, 0.1ml vinylbenzene, 2.5mmol methylaluminoxane (MAO), 2.5 μ mol dimethyl-silicon abutment two (2-methyl-4-naphthyl-indenyl) zirconium dichlorides, feed 0.015MPa hydrogen earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 35 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains styrol structural unit and gets polypropylene copolymer 2.0g, the 100ml tetracol phenixin, 0.48g iodo succimide and 0.1g Diisopropyl azodicarboxylate, 30 ℃ the reaction 20 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add 10.0g gained polypropylene-base atom transfer radical polymerization initiator, 100ml methyl-phenoxide, cuprous chloride 0.1g, pyridine imine 0.05ml, the 40g acrylamide, keeping temperature of reaction is 120 ℃, reacts after 10 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polypropylene amide copolymer.The molecular weight distribution of multipolymer is 3.85, weight-average molecular weight be 485015g/mol (m=5342 wherein, n=4571).
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, 2ml vinylbenzene, 2.5mmol ethyl aikyiaiurnirsoxan beta (EAO), 2.5 μ mol dimethyl-silicon abutment two (2-methyl-4-naphthyl-indenyl) zirconium dichlorides, feed the hydrogen of 0.05MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 35 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 60g of styrol structural unit, the 100ml tetracol phenixin, bromo-succinimide 20g and 0.07g dibenzoyl peroxide, 90 ℃ answer 6 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, 100ml methyl-phenoxide, cuprous chloride 0.08g, pentamethyl-two vinylidene triamine 0.05ml, the 30g Methacrylamide, keeping temperature of reaction is 125 ℃, reacts after 8 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block PMAm multipolymer.The molecular weight distribution of multipolymer is 3.93, weight-average molecular weight be 652061g/mol (m=6450 wherein, n=5367).
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, 2ml vinylbenzene, 2.5mmol methylaluminoxane (MAO), 2.5 μ mol ethyl abutments, two indenyl zirconium dichlorides, feed the hydrogen of 0.05MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 60 minutes at 0 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 1.5g of styrol structural unit, the 100ml tetracol phenixin, bromo-succinimide 0.6g and 0.14g dilauroyl peroxide, 90 ℃ the reaction 8 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, 100ml methyl-phenoxide, cuprous chloride 0.1g, pentamethyl-two vinylidene triamine 0.05ml, the 40g methyl acrylate, keeping temperature of reaction is 125 ℃, reacts after 5 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polypropylene acid methyl terpolymer.The molecular weight distribution of multipolymer is 4.01, weight-average molecular weight be 322730g/mol (m=560 wherein, n=3478).
Embodiment 10, preparation polypropylene block polypropylene acetoacetic ester multipolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, the vinylbenzene of 2ml, the methylaluminoxane of 2.5mmol (MAO), the ethyl abutment two indenyl zirconium dichlorides of 2.5 μ mol, feed the hydrogen of 0.1MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 1MPa, and polyreaction continues 30 minutes at 10 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 1.5g of styrol structural unit, 100ml dimethylbenzene, bromo-succinimide 0.6g and 0.14g dicumyl peroxide, 90 ℃ the reaction 8 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 15.0g, 100ml methyl-phenoxide, cuprous chloride 0.08g, pentamethyl-two vinylidene triamine 0.05ml, the 20g ethyl propenoate, keeping temperature of reaction is 125 ℃, reacts after 0.5 hour, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polypropylene acetoacetic ester multipolymer.The molecular weight distribution of multipolymer is 3.45, weight-average molecular weight be 48404g/mol (m=850 wherein, n=126).
Embodiment 11, preparation polypropylene block polypropylene tert-butyl acrylate multipolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, the vinylbenzene of 4ml, the methylaluminoxane of 5mmol (MAO), the ethyl abutment two indenyl zirconium dichlorides of 2.5 μ mol, feed the hydrogen of 0.5MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 1MPa, and polyreaction continues 30 minutes at 10 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 2.0g of styrol structural unit, 100ml dimethylbenzene, bromo-succinimide 0.8g and 0.16g Diisopropyl azodicarboxylate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 10.0g, 100ml methyl-phenoxide, cuprous chloride 0.05g, pentamethyl-two vinylidene triamine 0.05ml, the 20g tert-butyl acrylate, keeping temperature of reaction is 125 ℃, reacts after 1 hour, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polypropylene tert-butyl acrylate multipolymer.The molecular weight distribution of multipolymer is 2.98, weight-average molecular weight be 380858g/mol (m=197 wherein, n=2910).
Embodiment 12, preparation polypropylene block polypropylene lonitrile copolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, the vinylbenzene of 2ml, 2.5mmol ethyl aikyiaiurnirsoxan beta (EAO), the ethyl abutment two indenyl zirconium dichlorides of 2.5 μ mol, feed the hydrogen of 0.1MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 40 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 15.0g of styrol structural unit, the 100ml heptane, bromo-succinimide 6g and 0.48g dicumyl peroxide, 90 ℃ the reaction 8 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 15.0g, 100ml methyl-phenoxide, cuprous chloride 0.08g, pentamethyl-two vinylidene triamine 0.05ml, the 30g vinyl cyanide, keeping temperature of reaction is 125 ℃, reacts after 5 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polypropylene lonitrile copolymer.The molecular weight distribution of multipolymer is 3.32, weight-average molecular weight be 326166g/mol (m=1946 wherein, n=4610).
Embodiment 13, preparation polypropylene block polystyrene copolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, 2ml vinylbenzene, 2.5mmol isobutyl aluminium alkoxide, 2.5 μ mol ethyl abutments, two indenyl zirconium dichlorides, feed the hydrogen of 0.1MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 15 minutes at 50 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 2.0g of styrol structural unit, the 100ml chloroform, 0.48g bromo-succinimide and 0.1g di-isopropyl peroxydicarbonate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, 100ml methyl-phenoxide, cuprous chloride 0.03g, pentamethyl-two vinylidene triamine 0.05ml, 35g vinylbenzene, keeping temperature of reaction is 125 ℃, reacts after 30 minutes, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polystyrene copolymer.The molecular weight distribution of multipolymer is 3.81, weight-average molecular weight be 502612g/mol (m=4890 wherein, n=2857).
Embodiment 14, preparation polypropylene block methylmethacrylate copolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, the vinylbenzene of 2ml, 5.0mmol methylaluminoxane (MAO), 2.5 μ mol ethyl abutments, two indenyl zirconium dichlorides, feed the hydrogen of 0.1MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 0.7MPa, and polyreaction continues 30 minutes at 50 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings.
In the 250ml there-necked flask, adding gained end contains the polypropylene 2.0g of styrol structural unit, the 100ml chloroform, 0.48g bromo-succinimide and 0.1g di-isopropyl peroxydicarbonate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, 100ml methyl-phenoxide, cuprous chloride 0.07g, pentamethyl-two vinylidene triamine 0.02ml, add methyl methacrylate 30g, keeping temperature of reaction is 100 ℃, reacts after 5 hours, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polymethyl methacrylate copolymer.The molecular weight distribution of multipolymer is 3.43, weight-average molecular weight be 466221g/mol (m=560 wherein, n=4973).
Embodiment 15, preparation polypropylene block polystyrene copolymer
In being housed, churned mechanically stainless steel cauldron carries out polyreaction.Use nitrogen pump drainage three times earlier, use twice of propylene gas pump drainage again, order adds 100ml toluene, the vinylbenzene of 2ml, 10.0mmol methylaluminoxane (MAO), 2.5 μ mol ethyl abutments, two indenyl zirconium dichlorides, feed the hydrogen of 0.1MPa earlier, feed the propylene gas of certain pressure again, the pressure that finally keeps propylene is 1MPa, and polyreaction continues 30 minutes at 40 ℃.Discharging then, with acidic alcohol precipitation, filter white solid, use the tetrahydrofuran (THF) washed twice then after, 60 ℃ of following vacuum-dryings, obtain the polypropylene that end contains styrol structural unit.
In the 250ml there-necked flask, adding gained end contains the polypropylene 2.0g of styrol structural unit, the 100ml chloroform, 0.48g bromo-succinimide and 0.1g di-isopropyl peroxydicarbonate, 90 ℃ the reaction 5 hours after, with the reaction product acetone precipitation, filter white solid, with acetone thorough washing final vacuum drying, obtain the polypropylene-base atom transfer radical polymerization initiator.
In the 250ml there-necked flask, add gained polypropylene-base atom transfer radical polymerization initiator 20.0g, 100ml methyl-phenoxide, cuprous chloride 0.03g, pentamethyl-two vinylidene triamine 0.05ml, 35g vinylbenzene, keeping temperature of reaction is 125 ℃, reacts after 30 minutes, with excessive 10% acidic alcohol precipitation, filter white solid, water and ethanol thorough washing final vacuum drying obtain polypropylene block polystyrene copolymer.The molecular weight distribution of multipolymer is 3.16, weight-average molecular weight be 507984g/mol (m=380 wherein, n=4730).
The blend test of embodiment 16, polypropylene block copolymer
With polypropylene and polystyrene blend in 3: 1 by weight, with blend brittle failure according to a conventional method, the shape appearance figure of the scanning electronic microscope of section as shown in Figure 2; In addition, add the embodiment 1 preparation-obtained polypropylene block polystyrene copolymer of 1% weight in above-mentioned blend, the shape appearance figure of the scanning electronic microscope of its section as shown in Figure 3.As seen from the figure, show the adding of polypropylene block polystyrene copolymer, can obviously improve polypropylene and the polystyrene blend situation that is separated.
With polypropylene and polymethylmethacrylate blend in 3: 1 by weight, with blend brittle failure according to a conventional method, the shape appearance figure of the scanning electronic microscope of section as shown in Figure 4; In addition, add the embodiment 4 preparation-obtained polypropylene block polymethyl methacrylate copolymer of 1% weight in above-mentioned blend, the shape appearance figure of the scanning electronic microscope of its section as shown in Figure 5.As seen from the figure, show the adding of polypropylene block polymethyl methacrylate copolymer, can obviously improve polypropylene and the polymethylmethacrylate blend situation that is separated.
By above-mentioned two experiment confirms, polypropylene block copolymer of the present invention can obviously improve the comixing compatibility of polypropylene and other polymkeric substance, and the compatilizer that can be used as polypropylene and other polymer materials blend uses.
Claims (13)
1, a kind of polypropylene block copolymer has structure shown in the formula I,
Wherein, m is the integer between the 100-100000; N is the integer between the 10-5000; R
1Be H or methyl; R
2Be phenyl, p-methylphenyl ,-OCOCH
3,-CONH
2,-CN or-COOR, R is an alkyl.
2, polypropylene block copolymer according to claim 1 is characterized in that: described R is methyl, ethyl or the tertiary butyl.
3, polypropylene block copolymer according to claim 1 and 2 is characterized in that: the molecular weight distribution of described polypropylene block copolymer is 2-5.
4, the preparation method of the described polypropylene block copolymer of claim 1 comprises the steps:
1) the preparation end contains cinnamic polypropylene: to containing vinylbenzene, successively feed H in the organic solution of alkylaluminoxane and metallocene catalyst
2And propylene, carry out polyreaction, obtain structural formula and contain cinnamic polypropylene suc as formula the end of II;
2) preparation polypropylene-base atom transfer radical polymerization initiator: the gained end is contained cinnamic polypropylene suspension in organic solvent, add halogenated succinimide imide and thermolysis type radical initiator to aaerosol solution then, under 30～100 ℃, react, obtain the polypropylene-base atom transfer radical polymerization initiator of structural formula such as formula III;
(formula III)
M is 100～100 in the formula III, and the integer between 000, x are fluorine, chlorine, bromine or iodine;
3) the polypropylene-base atom transfer radical polymerization initiator with gained is suspended in toluene or the methyl-phenoxide, adds cuprous halide, multiple tooth nitrogenous compound and reaction monomers, in 70～150 ℃ of reactions down, obtains described polypropylene block copolymer; Described reaction monomers is vinylbenzene, p-methylstyrene, vinyl-acetic ester, third rare acid amides, Methacrylamide, vinyl cyanide, acrylate or the methacrylic ester.
5, preparation method according to claim 4 is characterized in that: the described metallocene catalyst of step 1) is selected from one or more in the metallocene catalyst with following general formula:
(1)Me
2Si[(2-R
1，4-R
2)Ind]
2ZrCl
2
R
1=Me, R
2=i-Pr or
R
1=Et, R
2=i-Pr or
R
1=Me, R
2=benzo or
R
1=Me, R
2=1-naphthyl or
R
1=H, R
2=benzo or
R
1＝Me，R
2＝Phenyl；
(2)Me
2Si[(2-R
1)THInd]
2ZrCl
2
R
1=Me, or Et;
(3)Me
2Si[2-R
1，5-R
2]
2ZrCl
2
R
1=Me, R
2=H or
R
1=Et, R
2=H or
R
1＝Me，R
2＝i-Pr；
(4)Me
2Si[(2-Me，4-R)(C
5H
2)]
2ZrCl
2
R=tert-Bu or
R＝i-Pr；
(5)C
2H
4(η
5-5，6-X
2Ind)
2ZrCl
2
X=4,7-Me
2, Me, H or OMe;
(6)C
2H
4(3-R)C
5H
3]
2ZrCl
2
R=Me, i-Pr or tert-Bu;
(7)Me
2Si(C
5H
5-nR
n)(C
5H
5-nR’
n)ZrCl
2
R
n=2,3,5-Me
3, R
n'=2,4,5-Me
3Or
R
n=2,4-Me
2, R
n'=3,5-Me
2Or
R
n=3-(tert-Bu), R
n'=4-(tert-Bu) or
R
n=3-Me, R
n'=4-Me or
R
n=2,4-Me
2, R
n'=3-Me, 4-Me or
R
n=3,4-Me
2, R
n'=3-Me or
R
n=3-(tert-Bu), R
n'=3-Me, 4-Me or
R
n=2,3,5-Me
3, R
n'=H or
R
n=2,4-Me
2, R
n'=H or
R
n=3-(tert-Bu), R
n'=H or
R
n＝3-Me，R
n’＝H；
(8)(Me
2Si)
2[(3，4-Me
2C
5H)]
2ZrCl
2
(9)C
2H
4(Ind)
2ZrCl
2
(10)C
2H
4(3-MeInd)
2ZrCl
2
(11)Me
2C(Ind)
2ZrCl
2
(12)Me
2Si(Ind)
2ZrCl
2
(13)Ph
2Si(Ind)
2ZrCl
2
(14)(Me)(Ph)Si(2-MeInd)
2ZrCl
2
(15)Me
2C(Ind)(C
5H
4)ZrCl
2
(16)Me
2C(Ind)(C
5H
3Me)ZrCl
2
(17)Me
2Si(2-Me-5-phenyl-Ind)
2ZrCl
2
Wherein, Me is a methyl, and Et is an ethyl, and i-Pr is a sec.-propyl, and tert-Bu is the tertiary butyl, and Ph or Phenyl are phenyl, and benzo is the benzo base, and naphthyl is a naphthyl, and Ind is an indenyl.
6, preparation method according to claim 4 is characterized in that: the solvent of the described organic solution of step 1) is selected from one or more in benzene,toluene,xylene, pentane, hexane and the heptane, is preferably toluene; Described alkylaluminoxane is methylaluminoxane, ethyl aikyiaiurnirsoxan beta or isobutyl aluminium alkoxide, is preferably methylaluminoxane.
7, preparation method according to claim 4, it is characterized in that: be added with described vinylbenzene 0.1-10ml in the described organic solution of step 1) in every 100ml organic solvent, described alkylaluminoxane 0.001-100mmol, described metallocene catalyst 0.001-100 μ mol; The mol ratio of described alkylaluminoxane and described metallocene catalyst is 100: 1-100000: 1, be preferably 300: 1-10000: 1.
8, preparation method according to claim 4 is characterized in that: the described H of step 1)
2Pressure is 0.01-0.3MPa, and vinylbenzene pressure is 0.1-1MPa; Described polymeric reaction temperature is 0-100 ℃, and the reaction times is 1-60 minute.
9, according to the arbitrary described preparation method of claim 4-8, it is characterized in that: step 2) described organic solvent is selected from one or more in tetracol phenixin, chloroform, toluene, dimethylbenzene, pentane, hexane and the heptane, is preferably tetracol phenixin; Described thermolysis type radical initiator is the special butyl ester of Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile), dibenzoyl peroxide, dilauroyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, di-isopropyl peroxydicarbonate or peroxidation phenylformic acid, is preferably Diisopropyl azodicarboxylate.
10, preparation method according to claim 9 is characterized in that: step 2) described aaerosol solution concentration is 1-60g/100ml; Halogenated succinimide imide add-on is 0.1-20g described in the described organic solvent of every 100ml, and described thermolysis type radical initiator add-on is 0.01-1g.
11, according to the described preparation method of claim 4-8, it is characterized in that: the described cuprous halide of step 3) is cuprous chloride, cuprous bromide or cuprous iodide, is preferably cuprous chloride; Described multiple tooth nitrogenous compound is 2,2 '-two pyridines, and 6,2 '-two pyridines, pyridine imine or pentamethyl-two vinylidene triamines are preferably pentamethyl-two vinylidene triamines.
12, preparation method according to claim 11 is characterized in that: the toluene of the described polypropylene-base atom transfer radical polymerization initiator of step 3) or methyl-phenoxide aaerosol solution concentration are 1.0-20.0g/100ml; The cuprous halide add-on is 0.01-0.1g described in every 100ml toluene or the methyl-phenoxide, and described multiple tooth nitrogenous compound add-on is 0.02-0.1ml, and described reaction monomers add-on is 20-40g.
13, the blending compatilizer that is main component with the arbitrary described polypropylene block copolymer of claim 1-3.
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|---|---|---|---|
| CNB2005100632106A CN100532415C (en) | 2005-04-06 | 2005-04-06 | Polypropylene block copolymer and its preparation process and use |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101348535B (en) * | 2007-07-17 | 2012-11-28 | 广州金发科技股份有限公司 | Macromole nucleating agent for polypropylene |
| CN104245834A (en) * | 2011-12-14 | 2014-12-24 | 陶氏环球技术有限责任公司 | Functionalized block composite and crystalline block composite compositions |
| CN115703908A (en) * | 2021-08-17 | 2023-02-17 | 中国石油天然气股份有限公司 | Polypropylene composition and preparation method and application thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1227927B (en) * | 1988-11-25 | 1991-05-14 | Enichem Elastomers | LINEAR COPOLYMERS WITH ALTERNATE BLOCKS. |
| CN1056625C (en) * | 1997-01-10 | 2000-09-20 | 中国石油化工总公司 | Styrene-propene block copolymer and preparing process thereof |
-
2005
- 2005-04-06 CN CNB2005100632106A patent/CN100532415C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101348535B (en) * | 2007-07-17 | 2012-11-28 | 广州金发科技股份有限公司 | Macromole nucleating agent for polypropylene |
| CN104245834A (en) * | 2011-12-14 | 2014-12-24 | 陶氏环球技术有限责任公司 | Functionalized block composite and crystalline block composite compositions |
| CN104245834B (en) * | 2011-12-14 | 2017-10-13 | 陶氏环球技术有限责任公司 | The block composite and crystalline blocks composite of functionalization |
| CN115703908A (en) * | 2021-08-17 | 2023-02-17 | 中国石油天然气股份有限公司 | Polypropylene composition and preparation method and application thereof |
| CN115703908B (en) * | 2021-08-17 | 2023-12-22 | 中国石油天然气股份有限公司 | Polypropylene composition and preparation method and application thereof |
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