CN106146708B - A kind of cationic polymerization process - Google Patents
A kind of cationic polymerization process Download PDFInfo
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- CN106146708B CN106146708B CN201510195024.1A CN201510195024A CN106146708B CN 106146708 B CN106146708 B CN 106146708B CN 201510195024 A CN201510195024 A CN 201510195024A CN 106146708 B CN106146708 B CN 106146708B
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Abstract
The invention discloses a kind of cationic polymerization process, it is included under solution polymerization condition, conjugated diene shown in monoolefine shown in formula IV and Formula V is contacted with each component in initiator system in polymer solvent, the initiator system contains the compound for being capable of providing proton, lewis acid and activator, the activator is selected from compound shown in compound and Formulas I 2 shown in Formulas I 1, and the lewis acid of 10~90 moles of % is lewis acid shown in Formula II.With the simple H of use+/ lewis acid initiator system is compared, and this method efficiency of initiation significantly improves, and can obtain higher polymer yield with higher rate of polymerization;By adjusting the content and type of activator in initiator system, the polymer with different molecular weight can be obtained under different polymerizing conditions;It can also implement to polymerize at higher temperatures, reduce the energy expenditure in polymerization process.
Description
Technical field
The present invention relates to a kind of cationic polymerization process.
Background technology
Butyl rubber is produced by the slurry polymerization process of diluent of monochloro methane currently, worldwide generally using,
Its reason essentially consists in:The production efficiency of slurry polymerization process is high, and the molecular weight of product is high, processing performance is good.
Compared with slurry polymerization process, polymerisation in solution rule is in these areas without apparent advantage, especially polymerisation in solution
Molecular weight product that method obtains is low, processing performance is poor, therefore is difficult that the product that is obtained with slurry polymerization process is mutually competing on the market
It strives.But the development space of solution polymerization process is than broader, such as:Solution polymerization process is than slurry polymerization process more meets environmental protection
It asks, and broader to the accommodation of polymerization temperature, especially to realizing that high temperature polymerization aspect has better development prospect.
In addition, prepared by halogenated butyl rubber generally use solwution method, that is, by the butyl rubber being dissolved in alkane and halogen-containingization
It closes object contact and carries out halogenation, when preparing butyl rubber using slurry polymerization process, need in polymerization procedure and halogenation
The solvent for the halogenated alkane that setting is intended in the mixture obtained with alkane displacement slurry polymerization process between reaction step replaces step
Rapid and polymer is redissolved step, and in solution polymerization process, then it is not necessarily to the polymer and is redissolved step, it is clear that polymerisation in solution
Production of the method more suitable for solwution method halogenated butyl rubber.
However, for producing butyl rubber in the solution, main problems faced is that the efficiency of initiation of initiator system is low,
Cause polymerization efficiency poor, it is difficult to obtain the product of high molecular weight.
US3361725 propose aluminum alkyl halide be the effective initiator for preparing butyl rubber in the solution, can compared with
The product of higher molecular weight is obtained at high temperature, but the molar ratio of dialkylaluminum halides in aluminum alkyl halide is required to reach
80% or more, and the molar ratio of monoalkyl dihalide aluminium is then less than 20%, thus the self-initiating of alkyl aluminum is leaned on to act on solution
In prepare butyl rubber in (such as hexane).But in fact, the efficiency of initiation of this initiator system is very low, and polymerization is fast
Rate is very slow, cannot be satisfied the needs of practical application.For this purpose, US6403747 improves this initiator system, i.e., upper
It states in dialkylaluminum halides/monoalkyl dihalide aluminium mixed system and introduces micro water or aikyiaiurnirsoxan beta, keep initiator system active
It improves, so as to prepare the butyl rubber that weight average molecular weight reaches 400,000 or more at -60 DEG C to -80 DEG C.Although
The efficiency of initiation of initiator system and rate of polymerization disclosed in US6403747 are improved to some extent, but in practical operation
It is in journey or unsatisfactory, and the preparation of initiator system is relatively difficult, especially requires very the technology of preparing of aikyiaiurnirsoxan beta
It is high.
Therefore, for the cationic solution polymerization technique of butyl rubber, there is an urgent need for the height that exploitation is adapted to polymerisation in solution
Active initiator system obtains high molecular weight products to improve efficiency of initiation and polymerization efficiency.
Invention content
The purpose of the present invention is to provide a kind of cationic polymerization process, this method prepares monoene using solution polymerization process
It is total to prepare monoolefine-conjugated diene with higher molecular weight with higher polymerization efficiency for hydrocarbon-conjugated diene copolymer
Polymers.
The present invention provides a kind of cationic polymerization process, this method is included under solution polymerization condition, will be at least one
Monoolefine and at least one conjugated diene are contacted with each component in initiator system in polymer solvent,
The initiator system contains at least one compound for being capable of providing proton, at least one lewis acid and at least
A kind of activator, the activator are selected from -2 compound represented of -1 compound represented of Formulas I and Formulas I,
In Formulas I -1 and Formulas I -2, R1、R2、R3、R4、R5、R6、R7And R8Respectively-H ,-X1、-NO2、With in-CN
One kind, X1And X2One kind respectively in halogen group;
The lewis acid of 10~90 moles of % is lewis acid shown in Formula II,
In Formula II, R9And R10Respectively C1~C8Linear or branched alkyl group, X3For one kind in halogen group;
The monoolefine is selected from formula IV compound represented,
In formula IV, R13And R14Respectively C1~C5Linear or branched alkyl group;Or R13For hydrogen, R14For C3~C5Branch
Alkyl;
The conjugated diene is selected from Formula V compound represented,
In Formula V, R15、R16And R17Respectively hydrogen or C1~C5Linear or branched alkyl group.
Method using the present invention prepares monoolefine-conjugated diene copolymer, with the simple H of use+/ lewis acid draws
Hair agent system is compared, and one side efficiency of initiation significantly improves, so as to obtain higher polymerization produce with higher rate of polymerization
Rate;On the other hand it by adjusting the content and type of activator in initiator system, can be obtained under different polymerizing conditions
Polymer with different molecular weight, so as to meet the requirement of different application occasion.In addition, with simple H is used+/
Lewis acid initiator system is compared, and method of the invention can be implemented to polymerize at higher temperatures, so as to be effectively reduced
Energy expenditure in polymerization process.
Specific implementation mode
The present invention provides a kind of cationic polymerization process, this method is included under solution polymerization condition, will be at least one
Monoolefine and at least one conjugated diene are contacted with each component in initiator system in polymer solvent.
In the present invention, "at least one" indicates one or more kinds of.
According to the method for the present invention, the initiator system (being referred to as initiator composition) contains at least one energy
Enough carry protogenic compound, at least one lewis acid and at least one activator.
The activator is selected from -2 compound represented of -1 compound represented of Formulas I and Formulas I,
In Formulas I -1 and Formulas I -2, R1、R2、R3、R4、R5、R6、R7And R8Respectively-H ,-X1、-NO2、With in-CN
One kind, X1And X2Respectively in halogen group one kind (such as:- F ,-Cl ,-Br or-I).
The specific example of the activator can include but is not limited to:Tetrahydrochysene 1,4-benzoquinone, tetrahydrochysene neighbour benzoquinones, three hydrogen pair of a fluorine
Benzoquinones, three hydrogen neighbour benzoquinones of a fluorine, difluoro dihydro 1,4-benzoquinone, difluoro dihydro neighbour benzoquinones, one hydrogen 1,4-benzoquinone of trifluoro, one hydrogen neighbour's benzene of trifluoro
Quinone, tetrafluoro 1,4-benzoquinone, tetrafluoro neighbour benzoquinones, three hydrogen 1,4-benzoquinone of a chlorine, three hydrogen neighbour benzoquinones of a chlorine, dichloro-dihydro 1,4-benzoquinone (including 2,
3- dichloros 1,4-benzoquinone, 2,5- dichloros 1,4-benzoquinone, 2,6- dichloros 1,4-benzoquinone), dichloro-dihydro neighbour benzoquinones (including 3,4- dichloro neighbour's benzene
Quinone, 3,5- dichloro neighbours benzoquinones, 3,6- dichloro neighbours benzoquinones), one hydrogen 1,4-benzoquinone of trichlorine, one hydrogen neighbour benzoquinones of trichlorine, chloranil, four
Chlorine neighbour benzoquinones, three hydrogen 1,4-benzoquinone of monobromo, three hydrogen neighbour benzoquinones of monobromo, dibromo dihydro 1,4-benzoquinone (including 2,3- dibromos 1,4-benzoquinone, 2,5-
Dibromo 1,4-benzoquinone, 2,6- dibromos 1,4-benzoquinone), dibromo dihydro neighbour benzoquinones (including 3,4- dibromo-os benzoquinones, 3,5- dibromo-os benzoquinones,
3,6- dibromo-o benzoquinones), one hydrogen 1,4-benzoquinone of tribromo, one hydrogen neighbour benzoquinones of tribromo, tetrabromo 1,4-benzoquinone, tetrabromo-phthalic quinone, three nitre of a fluorine
Base 1,4-benzoquinone, a fluorine trinitro- neighbour benzoquinones, difluoro dinitro 1,4-benzoquinone (including 2, bis- fluoro- 5,6- dinitros 1,4-benzoquinone of 3-, 2,5-
Two fluoro- 3,6- dinitros 1,4-benzoquinone, 2,6-, bis- fluoro- 3,5- dinitros 1,4-benzoquinone), difluoro dinitro o benzoquinones (including 3,4- bis-
Fluoro- 5,6- dinitro os benzoquinones, 3,5-, bis- fluoro- 4,6- dinitro os benzoquinones, 3,6-, bis- fluoro- 4,5- dinitro os benzoquinones), trifluoro
One nitro 1,4-benzoquinone, one nitro neighbour benzoquinones of trifluoro, a chlorine trinitro- 1,4-benzoquinone, a chlorine trinitro- neighbour benzoquinones, dichloro dinitro pair
Benzoquinones (including 2, bis- chloro- 5,6- dinitros 1,4-benzoquinone of 3-, 2,5-, bis- chloro- 3,6- dinitros 1,4-benzoquinone, 2,6-, bis- chloro- 3,5- bis-
Nitro 1,4-benzoquinone), dichloro dinitro o benzoquinones (including 3, bis- chloro- 5,6- dinitro os benzoquinones of 4-, 3,5-, bis- chloro- 4,6- dinitros
Base neighbour benzoquinones, 3,6-, bis- chloro- 4,5- dinitro os benzoquinones), one nitro 1,4-benzoquinone of trichlorine, one nitro neighbour benzoquinones of trichlorine, monobromo three
Nitro 1,4-benzoquinone, monobromo trinitro- neighbour benzoquinones, dibromo dinitro 1,4-benzoquinone (including 2, bis- bromo- 5,6- dinitros 1,4-benzoquinone of 3-, 2,
Bis- bromo- 3,6- dinitros 1,4-benzoquinone of 5-, 2,6-, bis- bromo- 3,5- dinitros 1,4-benzoquinone), dibromo dinitro o benzoquinones (including 3,4-
Two bromo- 5,6- dinitro os benzoquinones, 3,5-, bis- bromo- 4,6- dinitro os benzoquinones, 3,6-, bis- bromo- 4,5- dinitro os benzoquinones), three
One nitro 1,4-benzoquinone of bromine, one nitro neighbour benzoquinones of tribromo, tetranitro 1,4-benzoquinone, tetranitro neighbour benzoquinones, a fluorine tricyano 1,4-benzoquinone, one
Fluorine tricyano neighbour benzoquinones, difluoro dicyano p-benzoquinone (including 2, bis- fluoro- 5,6- dicyano p-benzoquinones of 3-, 2,5-, bis- fluoro- 3,6- bis-
Cyano 1,4-benzoquinone, 2,6-, bis- fluoro- 3,5- dicyano p-benzoquinones), difluoro dicyano neighbour benzoquinones (including 3, bis- fluoro- 5,6- dicyan of 4-
Base neighbour benzoquinones, 3,5-, bis- fluoro- 4,6- dicyanos neighbour benzoquinones, 3,6-, bis- fluoro- 4,5- dicyanos neighbour benzoquinones), one cyano of trifluoro is to benzene
Quinone, one cyano neighbour benzoquinones of trifluoro, a chlorine tricyano 1,4-benzoquinone, a chlorine tricyano neighbour benzoquinones, dichloro dicyano p-benzoquinone (including 2,
Bis- chloro- 5,6- dicyano p-benzoquinones of 3-, 2,5-, bis- chloro- 3,6- dicyano p-benzoquinones, 2,6-, bis- chloro- 3,5- dicyano p-benzoquinones),
Dichloro dicyano neighbour benzoquinones (including 3, bis- chloro- 5,6- dicyanos neighbour benzoquinones of 4-, 3,5-, bis- chloro- 4,6- dicyanos neighbour benzoquinones, 3,6-
Two chloro- 4,5- dicyanos neighbour benzoquinones), one cyano 1,4-benzoquinone of trichlorine, one cyano neighbour benzoquinones of trichlorine, monobromo tricyano 1,4-benzoquinone, one
Bromine tricyano neighbour benzoquinones, dibromo dicyano p-benzoquinone (including 2, bis- bromo- 5,6- dicyano p-benzoquinones of 3-, 2,5-, bis- bromo- 3,6- bis-
Cyano 1,4-benzoquinone, 2,6-, bis- bromo- 3,5- dicyano p-benzoquinones), dibromo dicyano neighbour benzoquinones (including 3, bis- bromo- 5,6- dicyan of 4-
Base neighbour benzoquinones, 3,5-, bis- bromo- 4,6- dicyanos neighbour benzoquinones, 3,6-, bis- bromo- 4,5- dicyanos neighbour benzoquinones), one cyano of tribromo is to benzene
Quinone, one cyano neighbour benzoquinones of tribromo, one cyano 1,4-benzoquinone of trinitro-, one cyano neighbour benzoquinones of trinitro-, dinitro dicyano p-benzoquinone
(including 2,3- dinitros -5,6- dicyano p-benzoquinone, 2,5- dinitros -3,6- dicyano p-benzoquinone, 2,6- dinitros -3,5-
Dicyano p-benzoquinone), dinitro dicyano neighbour benzoquinones (including 3,4- dinitro -5,6- dicyano neighbours benzoquinones, 3,5- dinitros -
4,6- dicyano neighbour benzoquinones, 3,6- dinitro -4,5- dicyano neighbours benzoquinones), a nitro tricyano 1,4-benzoquinone, a nitro tricyano
Adjacent benzoquinones, four cyano 1,4-benzoquinone, four cyano neighbour benzoquinones, a fluorine front three acid chloride group 1,4-benzoquinone, a fluorine front three acid chloride group neighbour benzoquinones, two
Fluorine dimethyl chloride base 1,4-benzoquinone (including 2, bis- fluoro- 5,6- dimethyl chlorides base 1,4-benzoquinone of 3-, 2,5-, bis- fluoro- 3,6- dimethyl chlorides bases
1,4-benzoquinone, 2,6-, bis- fluoro- 3,5- dimethyl chlorides base 1,4-benzoquinone), difluoro dimethyl chloride base neighbour benzoquinones (including 3,4- bis- fluoro- 5,6-
Dimethyl chloride base neighbour benzoquinones, 3,5-, bis- fluoro- 4,6- dimethyl chlorides base neighbour benzoquinones, 3,6-, bis- fluoro- 4,5- dimethyl chlorides base neighbour's benzene
Quinone), one formyl chloro 1,4-benzoquinone of trifluoro, one formyl chloro neighbour benzoquinones of trifluoro, a chlorine front three acid chloride group 1,4-benzoquinone, three formyl of a chlorine
Chloro neighbour benzoquinones, dichloro dimethyl chloride base 1,4-benzoquinone (including 2, bis- chloro- 5,6- dimethyl chlorides base 1,4-benzoquinone of 3-, 2,5- bis- chloro- 3,
6- dimethyl chloride bases 1,4-benzoquinone, 2,6-, bis- chloro- 3,5- dimethyl chlorides base 1,4-benzoquinone), dichloro dimethyl chloride base neighbour benzoquinones (including 3,
Bis- chloro- 5,6- dimethyl chlorides base neighbour benzoquinones of 4-, 3,5-, bis- chloro- 4,6- dimethyl chlorides base neighbour benzoquinones, 3,6-, bis- chloro- 4,5-, bis- formyls
Chloro neighbour benzoquinones), one formyl chloro 1,4-benzoquinone of trichlorine, one formyl chloro neighbour benzoquinones of trichlorine, monobromo front three acid chloride group 1,4-benzoquinone, one
Bromine front three acid chloride group neighbour benzoquinones, dibromo dimethyl chloride base 1,4-benzoquinone (including 2, bis- bromo- 5,6- dimethyl chlorides base 1,4-benzoquinone of 3-, 2,
Bis- bromo- 3,6- dimethyl chlorides base 1,4-benzoquinone of 5-, 2,6-, bis- bromo- 3,5- dimethyl chlorides base 1,4-benzoquinone), dibromo dimethyl chloride base neighbour's benzene
Quinone (including 3, bis- bromo- 5,6- dimethyl chlorides base neighbour benzoquinones of 4-, 3,5-, bis- bromo- 4,6- dimethyl chlorides base neighbour benzoquinones, 3,6- bis- are bromo-
4,5- dimethyl chloride base neighbour benzoquinones), one formyl chloro 1,4-benzoquinone of tribromo, one formyl chloro neighbour benzoquinones of tribromo, tetramethyl acid chloride group pair
Benzoquinones and tetramethyl acid chloride group neighbour's benzoquinones.
The activator be preferably selected from tetrahydrochysene benzoquinones (including tetrahydrochysene 1,4-benzoquinone and tetrahydrochysene neighbour benzoquinones), tetrachloroquinone (including
Chloranil and monoethyl quinone), four cyano benzoquinones (including four cyano 1,4-benzoquinone and four cyano neighbour benzoquinones) and dichloro dicyan
Base benzoquinones (including dichloro dicyano p-benzoquinone and dichloro dicyano neighbour benzoquinones).
The content of the activator, which is subject to, can obtain satisfactory polymerization effect.Usually, described to be capable of providing
The compound of proton and the molar ratio of the activator can be 1: 0.01~3, preferably 1: 0.1~2.8, more preferably 1:
0.2~2.5, further preferably 1: 0.8~1.5.
Polymerization according to the present invention, the lewis acid contain lewis acid shown in Formula II,
In Formula II, R9And R10Can be identical or different, can be respectively C1~C8Linear or branched alkyl group, preferably C1
~C5Linear or branched alkyl group;Preferably, R9And R10It is identical, is C1~C5Linear or branched alkyl group, more preferably second
Base.
In Formula II, X3For one kind in halogen group, such as-F ,-Cl ,-Br or-I, preferably-Cl.
In the present invention, C1~C8Linear or branched alkyl group include C1~C8Straight chained alkyl and C3~C8Branched alkyl,
Its specific example can include but is not limited to:Methyl, ethyl, n-propyl, isopropyl, normal-butyl, sec-butyl, isobutyl group, tertiary fourth
Base, n-pentyl, 2- methyl butyls, 3- methyl butyls, 2,2- dimethyl propyls, n-hexyl, 2- methyl amyls, 3- methyl amyls,
4- methyl amyls, 2,3- dimethylbutyls, 2,2- dimethylbutyls, 3,3- dimethylbutyls, 2- ethyl-butyls, n-heptyl, 2-
Methylhexyl, 3- methylhexyls, 4- methylhexyls, 5- methylhexyls, 2,2- dimethyl amyl groups, 2,3- dimethyl amyl groups, 2,4-
Dimethyl amyl group, 3,3- dimethyl amyl groups, 3,4- dimethyl amyl groups, 4,4- dimethyl amyl groups, 2- ethylpentyls, 3- ethyls penta
Base, n-octyl, 2- methylheptyls, 3- methylheptyls, 4- methylheptyls, 5- methylheptyls, 6- methylheptyls, 2,2- dimethyl oneself
Base, 2,3- dimethylhexanyls, 2,4- dimethylhexanyls, 2,5- dimethylhexanyls, 3,3- dimethylhexanyls, 3,4- dimethyl oneself
Base, 3,5- dimethylhexanyls, 4,4- dimethylhexanyls, 4,5- dimethylhexanyls, 5,5- dimethylhexanyls, 2- ethylhexyls, 3-
Ethylhexyl, 4- ethylhexyls, 2- n-propyls amyl and 2- isopropyl amyls.
In the present invention, lewis acidic specific example shown in Formula II can include but is not limited to:Dimethylaluminum chloride, two
Ethylmercury chloride aluminium, diη-propyl aluminium chloride, diisopropyl aluminium chloride, di-n-butyl aluminium chloride and diisobutyl aluminum chloride.
Preferably, lewis acid shown in Formula II is diethyl aluminum chloride.
Containing there are two alkyl in lewis acidic molecular structure shown in Formula II, it can play and inhibit cation activity center
Occur chain tra nsfer effect, so as to improve preparation polymer molecular weight.But lewis acidic shown in Formula II contain
It measures excessively high, can reduce polymerization rate, extend polymerization time.Polymerization according to the present invention, with lewis acidic total amount
On the basis of, lewis acidic content shown in Formula II is 10~90 moles of %, in this way can be in polymerization rate and polymer
Preferable balance is obtained between molecular weight.Preferably, lewis acidic shown in Formula II to contain on the basis of lewis acidic total amount
Amount is 20~80 moles of %.It is highly preferred that on the basis of lewis acidic total amount, lewis acidic content shown in Formula II is 30
~70 moles of %.
Initiator system according to the present invention, 10~90 moles of % (preferably rub by 20~80 moles of %, more preferable 30~70
Your %) lewis acid be lewis acid shown in Formula II, remainder lewis acid can be cationic polymerization initiators body
At least one of common lewis acid in system.Such as:Remainder lewis acid can be selected from BCl3、BF3、AlCl3、
TiCl4、SnCl4、ZnCl2, formula III compound represented and R12 3Al,
In formula III, R11For C1~C8Linear or branched alkyl group, preferably C1~C5Linear or branched alkyl group, more preferably
For ethyl, X41And X42It is identical or different, one kind (such as-F ,-Cl ,-Br or-I) respectively in halogen group, preferably-Cl;
R12 3In Al, three R12It is identical or different, can be respectively C1~C8Linear or branched alkyl group, preferably C1~C5
Linear or branched alkyl group.
The specific example of formula III compound represented can include but is not limited to dichloromethyl aluminium, ethyl aluminum dichloride, dichloro
N-propyl aluminium, two chloro isopropyl aluminium, dichloro n-butylaluminum and dichloro aluminium isobutyl.
R12 3The specific example of Al can include but is not limited to:Trimethyl aluminium and triethyl aluminum.
Preferably, remainder lewis acid is formula III compound represented.That is, the lewis acid is preferably Formula II
Shown in lewis acid and formula III compound represented, it is lewis acidic shown in Formula II on the basis of lewis acidic total amount
Content is 10~90 moles of %, preferably 20~80 moles of %, more preferably 30~70 moles of %.
It is highly preferred that the lewis acid is diethyl aluminum chloride and ethyl aluminum dichloride, using lewis acidic total amount as base
The content of standard, diethyl aluminum chloride is 10~90 moles of %, preferably 20~80 moles of %, more preferably 30~70 moles of %.
Polymerization according to the present invention, the lewis acidic content can be that the conventional of cationic polymerization field is used
Amount.Usually, the compound for being capable of providing proton and the lewis acidic molar ratio can be 0.01~1: 1, preferably
It is 0.02~0.5: 1, more preferably 0.04~0.3: 1, further preferably 0.05~0.1: 1.
The compound for being capable of providing proton can be capable of providing proton to be commonly various in cationic polymerization field
Compound.Usually, the compound for being capable of providing proton can be H2O and/or Bronsted acid, specific example can wrap
It includes but is not limited to:H2O、HCl、HF、HBr、H2SO4、H2CO3、H3PO4And HNO3.Preferably, the chemical combination for being capable of providing proton
Object is HCl.
May be used common various methods by the monoolefine and conjugated diene with it is each in the initiator system
Component contacts, and to be polymerize, forms monoolefine-conjugated diene copolymer.
In one embodiment of the invention, each component in the initiator system can be dissolved in solvent,
And be aged obtained mixture, obtain initiator solution;By the initiator solution and described in being dissolved in polymer solvent
Monoolefine and conjugated diene mixing.
The purpose of the ageing is to make lewis acid in initiator system and is capable of providing compound and the work of proton
Agent forms stable complexing and causes activated centre, can carry out under normal conditions.Usually, the ageing can be -100
DEG C to 20 DEG C, preferably -100 DEG C to 0 DEG C, more preferably -100 DEG C to -50 DEG C, further preferred -90 DEG C to -70 DEG C of temperature range
Interior progress.The time of the ageing can be 10 minutes to 10 hours.Preferably, the time of the ageing is 30 minutes or more,
Such as 30 minutes to 5 hours.It is highly preferred that the time of the ageing is 60 minutes or more, such as 60 minutes to 120 minutes.
The solvent can be the various liquids that can dissolve the Bronsted acid, the lewis acid and the activator
Matter.Usually, the solvent can be selected from alkane, halogenated alkane and aromatic hydrocarbons, be preferably selected from C3~C10Alkane, C1~C10Halogen
For alkane and C6~C12Aromatic hydrocarbons.
As solvent, the alkane includes aliphatic alkane and alicyclic alkanes, such as C3~C10Alkane include C3~C10
Aliphatic alkane and C3~C10Alicyclic alkanes.
As solvent, the halogenated alkane includes halogenated aliphatic alkane and halogenated cyclo alkane, such as C1~C10Halogen
Include C for alkane1~C10Halogenated aliphatic alkane and C3~C10Halogenated cyclo alkane.Halogen in the halogenated alkane
Atom can be chlorine, bromine or fluorine, preferably chlorine or fluorine.The halogenated alkane is preferably C1~C4Halogenated aliphatic alkane.
The specific example of the solvent can include but is not limited to:Propane, normal butane, iso-butane, pentane, isopentane,
Neopentane, pentamethylene, n-hexane, 2- methylpentanes, 3- methylpentanes, 2,3- dimethylbutanes, hexamethylene, methyl cyclopentane,
Normal heptane, 2- methyl hexanes, 3- methyl hexanes, 2- ethylpentanes, 3- ethylpentanes, 2,3- dimethyl pentanes, 2,4- dimethyl
Pentane, normal octane, 2- methyl heptanes, 3- methyl heptanes, 4- methyl heptanes, 2,3- dimethylhexanes, 2,4- dimethylhexanes, 2,
5- dimethylhexanes, 3- ethyl hexanes, 2,2,3- trimethylpentanes, 2,3,3- trimethylpentanes, 2,4,4- trimethylpentanes, 2-
Methyl -3- ethylpentanes, n -nonane, 2- methyloctanes, 3- methyloctanes, 4- methyloctanes, 2,3- dimethyl heptanes, 2,4- bis-
Methyl heptane, 3- ethyl heptanes, 4- ethyl heptanes, 2,3,4- trimethyl cyclohexanes, 2,3,5- trimethyl cyclohexanes, 2,4,5- trimethyls
Hexane, 2,2,3- trimethyl cyclohexanes, 2,2,4- trimethyl cyclohexanes, 2,2,5- trimethyl cyclohexanes, 2,3,3- trimethyl cyclohexanes, 2,4,
4- trimethyl cyclohexanes, 2- methyl -3- ethyl hexanes, 2- methyl -4- ethyl hexanes, 3- methyl -3- ethyl hexanes, 3- methyl -4-
Ethyl hexane, 3,3- diethylpentanes, 1- methyl -2- ethyl cyclohexanes, 1- methyl -3- ethyl cyclohexanes, 1- methyl -4- ethyls
Hexamethylene, n-propyl hexamethylene, isopropyl cyclohexane, trimethyl-cyclohexane (include the various isomers of trimethyl-cyclohexane, such as
1,2,3- trimethyl-cyclohexane, 1,2,4- trimethyl-cyclohexanes, 1,2,5- trimethyl-cyclohexanes, 1,3,5- trimethyl-cyclohexanes),
N-decane, 2- methylnonanes, 3- methylnonanes, 4- methylnonanes, 5- methylnonanes, 2,3- dimethyl octane, 2,4- dimethyl
Octane, 3- ethyls octane, 4- ethyls octane, 2,3,4- trimethylheptanes, 2,3,5- trimethylheptanes, 2,3,6- trimethyl heptan
Alkane, 2,4,5- trimethylheptanes, 2,4,6- trimethylheptanes, 2,2,3- trimethylheptanes, 2,2,4- trimethylheptanes, 2,2,5-
Trimethylheptane, 2,2,6- trimethylheptanes, 2,3,3- trimethylheptanes, 2,4,4- trimethylheptanes, 2- methyl -3- ethyl heptan
Alkane, 2- methyl -4- ethyl heptanes, 2- methyl -5- ethyl heptanes, 3- methyl -3- ethyl heptanes, 4- methyl -3- ethyl heptanes, 5-
Methyl -3- ethyl heptanes, 4- methyl -4- ethyl heptanes, 4- propyl heptane, 3,3- diethylhexanes, 3,4- diethylhexanes, 2-
Methyl -3,3- diethylpentane, 1,2- diethyl cyclohexanes, 1,3- diethyl cyclohexanes, Isosorbide-5-Nitrae-diethyl cyclohexane, normal-butyl
Hexamethylene, isobutyl butylcyclohexane, t-butylcyclohexane, tetramethyl-ring hexane (include the various isomers of tetramethyl-ring hexane, such as
1,2,3,4- tetramethyl-ring hexane, 1,2,4,5- tetramethyl-ring hexanes, 1,2,3,5- tetramethyl-ring hexanes), a fluoromethane, difluoro
Methane, fluoroform, carbon tetrafluoride, monochloro methane, dichloromethane, chloroform, carbon tetrachloride, a fluoroethane, Difluoroethane,
Trifluoroethane, tetrafluoroethane, pentafluoroethane, carbon hexa fluoride, monochlorethane, dichloroethanes, trichloroethanes, tetrachloroethanes, pentachloro-
Ethane, carbon hexachloride, a fluoro-propane, difluoropropane, trifluoro propane, tetrafluoropropane, pentafluoropropane, hexafluoropropane, heptafluoro-propane,
Octafluoropropane, a chloropropane, dichloropropane, trichloropropane, four chloropropanes, pentachloropropane, chlordene propane, heptachloropropane, eight chlorine
Propane, a fluorine butane, difluorobutane, trifluorobutane, tetrafluoro butane, 3-pentafluorobutane, hexafluoro butane, seven fluorine butane, octafluorobutane,
Nine fluorine butane, ten fluorine butane, a chlorobutane, dichloroetane, three chlorobutanes, four chlorobutanes, pentachlorobutane, chlordene butane, heptachlor
Butane, telodrine alkane, nine chlorobutanes, ten chlorobutanes, toluene, ethylbenzene and dimethylbenzene (including ortho-xylene, meta-xylene and to two
Toluene).
The concentration of the initiator solution can be conventional selection, be not particularly limited.The dosage of the initiator solution
It can be made appropriate choice according to specific polymerizing condition, polymerization can be caused by being subject to.Those skilled in the art can be
Under the introduction of the prior art, the initiator amount for being adequate to bring about polymerization is determined by the experiment of limited number of time.
Polymerization according to the present invention, the monoolefine can carry out cationic polymerization for commonly used in the art
Monoolefine.Usually, the monoolefine is selected from formula IV compound represented,
In formula IV, R13And R14Respectively C1~C5Linear or branched alkyl group;Or R13For hydrogen, R14For C3~C5Branch
Alkyl.
In the present invention, C1~C5Linear or branched alkyl group include C1~C5Straight chained alkyl and C3~C5Branched alkyl,
Its specific example can include but is not limited to:Methyl, ethyl, n-propyl, isopropyl, normal-butyl, sec-butyl, isobutyl group, tertiary fourth
Base, n-pentyl, isopentyl, tertiary pentyl and neopentyl.
Specifically, the monoolefine can be selected from but not limited to:2- methyl-1-propylenes (that is, isobutene), 2- methyl-1s-
Butylene, 3-methyl-1-butene, 2,3- dimethyl -1- butylene, 2- Methyl-1-pentenes, 3- Methyl-1-pentenes, 4- methyl-1-pentenes
Alkene, 2,3- dimethyl -1- amylenes, 2,4- dimethyl -1- amylenes, 2- methyl-1s-hexene, 2,3- dimethyl -1- hexenes, 2,4- bis-
Methyl-1-hexene, 2,5- dimethyl-1- hexenes and 2,4,4- trimethyl-1- amylenes.
Preferably, the monoolefine is isobutene.
According to the method for the present invention, the conjugated diene refers to the compound containing conjugated double bond in molecular structure.It is excellent
Selection of land, the conjugated diene are selected from Formula V compound represented,
In Formula V, R15、R16And R17It is identical or different, respectively hydrogen or C1~C5Linear or branched alkyl group.
The specific example of the conjugated diene can include but is not limited to butadiene and/or isoprene.It is highly preferred that
The conjugated diene is isoprene.
According to the method for the present invention, the relative usage of the monoolefine and the conjugated diene can be prepared according to final
The concrete application occasion of polymer make appropriate choice.Usually, it is with the total amount of the monoolefine and conjugated diene
The content of benchmark, the monoolefine can be 80~99.5 weight %, preferably 90~98 weight %;The conjugated diene
Content can be 0.5~20 weight %, preferably 2~10 weight %.
Polymerization according to the present invention, the polymer solvent can be enough to make polymerisation under solution state to be various
The solvent of progress, i.e., the described polymer solvent can not only dissolve monoolefine and conjugated diene, and can dissolve the poly- of polymerization formation
Close object.Usually, the polymer solvent can be selected from alkane (can be aliphatic alkane and/or alicyclic alkanes) and alkyl halide
Hydrocarbon is preferably selected from C3~C10Alkane and C1~C10Halogenated alkane.Halogen atom in the halogenated alkane can be chlorine, bromine
Or fluorine, preferably chlorine or fluorine.The halogenated alkane is preferably C1~C4Halogenated alkane.
Polymerization according to the present invention, even if can be imitated with high polymerization if polymerization in low polar polymeric solvent
Rate prepares the polymer of high molecular weight.The low polar polymeric solvent can be for example the alkane, can also be the alkane
With the mixture of the halogenated alkane.When the polymer solvent is the mixture of the alkane and the halogenated alkane, with institute
On the basis of the total amount for stating polymer solvent, the content of the alkane can be 20~99 volume %, preferably 40~99 volume %, more
Preferably 50~90 volume %;The content of the halogenated alkane can be 1~80 volume %, preferably 1~60 volume %, more excellent
It is selected as 10~50 volume %.
The specific example of the polymer solvent can include but is not limited to:Propane, normal butane, iso-butane, pentane, isoamyl
Alkane, neopentane, pentamethylene, n-hexane, 2- methylpentanes, 3- methylpentanes, 2,3- dimethylbutanes, hexamethylene, methyl ring penta
Alkane, normal heptane, 2- methyl hexanes, 3- methyl hexanes, 2- ethylpentanes, 3- ethylpentanes, 2,3- dimethyl pentanes, 2,4- diformazans
Base pentane, normal octane, 2- methyl heptanes, 3- methyl heptanes, 4- methyl heptanes, 2,3- dimethylhexanes, 2,4- dimethylhexanes,
2,5- dimethylhexanes, 3- ethyl hexanes, 2,2,3- trimethylpentanes, 2,3,3- trimethylpentanes, 2,4,4- trimethylpentanes,
2- methyl -3- ethylpentanes, n -nonane, 2- methyloctanes, 3- methyloctanes, 4- methyloctanes, 2,3- dimethyl heptanes, 2,4-
Dimethyl heptane, 3- ethyl heptanes, 4- ethyl heptanes, 2,3,4- trimethyl cyclohexanes, 2,3,5- trimethyl cyclohexanes, 2,4,5- front threes
Base hexane, 2,2,3- trimethyl cyclohexanes, 2,2,4- trimethyl cyclohexanes, 2,2,5- trimethyl cyclohexanes, 2,3,3- trimethyl cyclohexanes, 2,
4,4- trimethyl cyclohexanes, 2- methyl -3- ethyl hexanes, 2- methyl -4- ethyl hexanes, 3- methyl -3- ethyl hexanes, 3- methyl -
4- ethyl hexanes, 3,3- diethylpentanes, 1- methyl -2- ethyl cyclohexanes, 1- methyl -3- ethyl cyclohexanes, 1- methyl -4- second
Butylcyclohexane, n-propyl hexamethylene, isopropyl cyclohexane, trimethyl-cyclohexane (include the various isomers of trimethyl-cyclohexane,
Such as 1,2,3- trimethyl-cyclohexanes, 1,2,4- trimethyl-cyclohexanes, 1,2,5- trimethyl-cyclohexanes, 1,3,5- 3-methyl cyclohexanols
Alkane), n-decane, 2- methylnonanes, 3- methylnonanes, 4- methylnonanes, 5- methylnonanes, 2,3- dimethyl octane, 2,4- bis-
Methyloctane, 3- ethyls octane, 4- ethyls octane, 2,3,4- trimethylheptanes, 2,3,5- trimethylheptanes, 2,3,6- trimethyls
Heptane, 2,4,5- trimethylheptanes, 2,4,6- trimethylheptanes, 2,2,3- trimethylheptanes, 2,2,4- trimethylheptanes, 2,2,
5- trimethylheptanes, 2,2,6- trimethylheptanes, 2,3,3- trimethylheptanes, 2,4,4- trimethylheptanes, 2- methyl -3- ethyls
Heptane, 2- methyl -4- ethyl heptanes, 2- methyl -5- ethyl heptanes, 3- methyl -3- ethyl heptanes, 4- methyl -3- ethyl heptanes,
5- methyl -3- ethyl heptanes, 4- methyl -4- ethyl heptanes, 4- propyl heptane, 3,3- diethylhexanes, 3,4- diethylhexanes,
2- methyl -3,3- diethylpentane, 1,2- diethyl cyclohexanes, 1,3- diethyl cyclohexanes, Isosorbide-5-Nitrae-diethyl cyclohexane, positive fourth
Butylcyclohexane, isobutyl butylcyclohexane, t-butylcyclohexane, tetramethyl-ring hexane (include the various isomers of tetramethyl-ring hexane,
Such as 1,2,3,4- tetramethyl-ring hexanes, 1,2,4,5- tetramethyl-ring hexanes, 1,2,3,5- tetramethyl-ring hexanes), a fluoromethane, two
Fluoromethane, fluoroform, carbon tetrafluoride, monochloro methane, dichloromethane, chloroform, carbon tetrachloride, a fluoroethane, difluoro second
Alkane, trifluoroethane, tetrafluoroethane, pentafluoroethane, carbon hexa fluoride, monochlorethane, dichloroethanes, trichloroethanes, tetrachloroethanes, five
Chloroethanes, carbon hexachloride, a fluoro-propane, difluoropropane, trifluoro propane, tetrafluoropropane, pentafluoropropane, hexafluoropropane, seven fluorine third
Alkane, octafluoropropane, a chloropropane, dichloropropane, trichloropropane, four chloropropanes, pentachloropropane, chlordene propane, heptachloropropane, eight
Chloropropane, a fluorine butane, difluorobutane, trifluorobutane, tetrafluoro butane, 3-pentafluorobutane, hexafluoro butane, seven fluorine butane, octafluoro fourth
Alkane, nine fluorine butane, ten fluorine butane, a chlorobutane, dichloroetane, three chlorobutanes, four chlorobutanes, pentachlorobutane, chlordene butane, seven
Chlorobutane, telodrine alkane, nine chlorobutanes and ten chlorobutanes.
The polymer solvent is preferably selected from pentane, n-hexane, normal heptane, monochloro methane, dichloromethane and monochlorethane.
The dosage of the polymer solvent can be the conventional selection of this field.Usually, the dosage of the polymer solvent makes
It is 2~50 weight %, preferably 5~30 weight %, more preferably 5~20 weight % to obtain total monomer concentration.
Polymerization according to the present invention, the cationic polymerization condition can be the conventional selection of this field.Usually,
Monoolefine and conjugated diene can be at -120 DEG C to 20 DEG C, preferably -100 DEG C extremely with the contact of each component in initiator system
It is carried out within the temperature range of 0 DEG C, more preferably -100 DEG C to -40 DEG C, further preferably -90 DEG C to -60 DEG C.It is according to the present invention poly-
Conjunction method, the duration of the contact can be the conventional selection of this field, can be generally 10~180 minutes, preferably
30~120 minutes.
According to the method for the present invention, in a preferred embodiment, the activator is dichlorocyanobenzoquinone (packet
Include dichloro dicyano p-benzoquinone and dichloro dicyano neighbour benzoquinones), the lewis acid be formula III shown in lewis acid (preferably
For ethyl aluminum dichloride) and Formula II shown in lewis acid (preferably diethyl aluminum chloride), be with the lewis acidic total amount
Benchmark, lewis acidic content shown in formula III are 10~50 moles of %, and lewis acidic content is 50~90 shown in Formula II
Mole %, the polymer solvent contains halogenated alkane and alkane, on the basis of the total amount of the polymer solvent, the halogenated alkane
Content be 10~50 volume %, preferably 20~50 volume %, the content of the alkane is 50~90 volume %, preferably 50
~80 volume %.According to the preferred embodiment, can be prepared with higher polymerization efficiency has higher molecular weight (as divided equally again
Son amount is 3 × 105More than) monoolefine-conjugated diene copolymer.In the preferred embodiment, with the Louis
On the basis of the total amount of acid, lewis acidic content shown in formula III is preferably 10~30 moles of %, lewis acid shown in Formula II
Content be preferably 70~90 moles of %, can prepare in this way with higher molecular weight (such as weight average molecular weight be 5 × 105More than)
Monoolefine-conjugated diene copolymer.According to the preferred embodiment, polymerisation preferably -70 DEG C to -120 DEG C, more
It is preferred that being carried out at a temperature of -80 DEG C to -100 DEG C.In the preferred embodiment, the ratio in initiator system between each component
Example is not particularly limited, and can be previously described ratio, still, the compound for being capable of providing proton and the activator
Molar ratio be preferably 1: 0.5~1.5;The compound for being capable of providing proton is preferably with the lewis acidic molar ratio
0.04~0.1: 1.In the preferred embodiment, remaining reaction condition can be previously described condition.
Polymerization according to the present invention, in another preferred embodiment, the activator is four cyano benzoquinones
(including four cyano 1,4-benzoquinone and four cyano neighbour benzoquinones) and/or dichlorocyanobenzoquinone (including dichloro dicyano p-benzoquinone and two
Chlorine dicyano neighbour benzoquinones), the lewis acid is shown in lewis acid shown in formula III (preferably ethyl aluminum dichloride) and Formula II
Lewis acid (preferably diethyl aluminum chloride), on the basis of the lewis acidic total amount, lewis acid shown in formula III
Content be 30~70 moles of %, lewis acidic content shown in Formula II is 30~70 moles of %, when preparing initiator solution
Digestion time be 30 minutes or more, the polymer solvent be alkane.According to the preferred embodiment, even if in higher temperature
Degree is polymerize (as being not higher than -60 DEG C to -70 DEG C), and can also be prepared with higher polymerization efficiency has higher molecular weight (such as weight
Average molecular weight is 2.5 × 105More than) monoolefine-conjugated diene copolymer.It is highly preferred that the activator is dichloro two
Cyano benzoquinones (including dichloro dicyano p-benzoquinone and dichloro dicyano neighbour benzoquinones), can obtain higher polymerization efficiency in this way.
According to the preferred embodiment, polymerisation carries out at a temperature of -60 DEG C to -120 DEG C, preferably -80 DEG C to -90 DEG C.
In the preferred embodiment, the ratio in initiator system between each component is not particularly limited, and can be previously described
Ratio, still, the compound for being capable of providing proton and the molar ratio of the activator are preferably 1: 0.8~1.5;The energy
It is preferably 0.04~0.1: 1 that protogenic compound, which is enough put forward, with the lewis acidic molar ratio.In the preferred embodiment
In, remaining reaction condition can be previously described condition.
Polymerization according to the present invention can also include adding to gather in the mixture obtained to polymerization after completion of polymerization
Terminator is closed to make polymerisation terminate (such as alcohol).The present invention is not special for the type and dosage of the polymerization terminator
It limits, can be the conventional selection of this field, polymerisation can be terminated by being subject to, and repeats no more herein.
The present invention will be described in detail with reference to embodiments.
In following embodiment and comparative example, polymer yield is measured using weight method,
Polymer yield (%)=(total weight of the monomer of weight/addition of obtained polymer) × 100%.
In following embodiment and comparative example, the molecular weight and molecular weight distributing index of polymer are given birth to using Japanese Shimadzu Corporation
The LC-20A type liquid phase gel permeation chromatographs of production measure, using single aperture chromatographic columnWithFour columns are combined.Mobile phase is tetrahydrofuran, flow velocity 0.7mL/min;A concentration of 2mg/mL of sample solution, sample size are
200μL;Test temperature is 35 DEG C;Using single distribution polystyrene as standard sample.
In following embodiment and comparative example, using the AVANCE400 Nuclear Magnetic Resonance commercially available from Bruker companies of Switzerland, with
CDC13Make solvent, TMS is internal standard, measures the degree of unsaturation of monoolefine-conjugated diene copolymer of preparation (that is, the list prepared
The content of the structural unit formed by isoprene in alkene-conjugated diene copolymer).
Solvent and monomer used in following embodiment and comparative example before use, using method commonly used in the art into
Row is refined, and the preparation of polymerisation and initiator solution carries out in the operating under nitrogen case equipped with low temperature cryostat.
The method that Examples 1 to 31 is used to illustrate the present invention.
Embodiment 1
(1) 0.0662g chloranils are dissolved in 80g and the dichloromethane for containing HCl (a concentration of 0.0036mol/L) is molten
In liquid, obtained solution is cooled to -80 DEG C in advance, the dichloro of a concentration of 0.9mol/L of 2.6mL is then sequentially added into the solution
The n-heptane solution of the hexane solution of aluminium ethide (EADC) and the diethyl aluminum chloride (DEAC) of a concentration of 1.0mol/L of 1mL,
After mixing, obtained mixed liquor is aged to 80min at -80 DEG C, to obtain initiator solution.Wherein, by weight, draw
The content for sending out chloranil in agent solution is 800ppm.
(2) 250mL three-necked flasks are placed in temperature control in -80 DEG C to -85 DEG C of low temperature cryostat, to be burnt successively to three mouthfuls
It is added that 85mL is cooled to -80 DEG C of n-hexane, 15mL is cooled to -80 DEG C of isobutene and 0.5mL is cooled to -20 DEG C different in advance in bottle
Pentadiene is uniformly mixed, obtains monomer solution.Initiator solution prepared by 10mL steps (1), mixing are added into monomer solution
Reaction 30min is stood after uniformly, it is in -80 DEG C to -85 DEG C that control cryostat temperature in initiator solution and reaction process, which is added dropwise,
Within the scope of.The methanol solution that 5mL contains 0.5 weight %NaOH is added into reaction mixture after reaction, to terminate
Polymerisation.Then mixed solution is placed in hot bath and removes solvent, after obtained solid is washed, in vacuum drying oven
In it is dry to constant weight in 60 DEG C, obtain monoolefine-conjugated diene copolymer.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 1.
Embodiment 2
It is polymerize using side same as Example 1, unlike, in step (2), initiator solution and polymerization is added dropwise
In reaction process, by the temperature control of cryostat within the scope of -40 DEG C to -50 DEG C, the dosage of initiator solution is
15mL, polymerization reaction time 50min.The molecular weight of polymer yield and polymer, molecular weight distributing index and unsaturation
Degree, is as a result listed in table 1.
Embodiment 3
It is polymerize using method same as Example 1, unlike, in step (1), the hexane solution of EADC
A concentration of 0.9mol/L, a concentration of 1.0mol/L of the n-heptane solution of dosage 1.9mL, DEAC, dosage 1.7mL.Polymerization
The molecular weight of produce rate and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 4
It is polymerize using method same as Example 3, unlike, in step (2), initiator solution is added dropwise and gathers
It closes in reaction process, by the temperature control of cryostat within the scope of -60 DEG C to -70 DEG C, polymerization reaction time is
40min.The molecular weight of polymer yield and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 5
It is polymerize using method same as Example 1, unlike, in step (1), the hexane solution of EADC
A concentration of 0.9mol/L, a concentration of 1.0mol/L of the n-heptane solution of dosage 1.1mL, DEAC, dosage 2.3mL.Polymerization
The molecular weight of produce rate and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 6
(1) by 0.0602g 2, bis- chloro- 5,6- dicyano p-benzoquinones of 3- be dissolved in 80g and containing HCl it is (a concentration of
In dichloromethane solution 0.0040mol/L), obtained solution is cooled to -85 DEG C in advance, is then sequentially added into the solution
The diethyl of the hexane solution and a concentration of 1.0mol/L of 1.1mL of the ethyl aluminum dichloride (EADC) of a concentration of 0.9mol/L of 2.8mL
Obtained mixed liquor is placed in -85 DEG C of cryostat and is aged after mixing by the n-heptane solution of base aluminium chloride (DEAC)
100min, to obtain initiator solution.Wherein, by weight, 2,3-, bis- chloro- 5,6- dicyano p-benzoquinones in initiator solution
Content be 730ppm.
(2) 250mL three-necked flasks are placed in temperature control in -80 DEG C to -85 DEG C of low temperature cryostat, to be burnt successively to three mouthfuls
It is added that 85mL is cooled to -80 DEG C of n-hexane, 15mL is cooled to -80 DEG C of isobutene and 0.5mL is cooled to -20 DEG C different in advance in bottle
Pentadiene is uniformly mixed, obtains monomer solution.Initiator solution prepared by 10mL steps (1), mixing are added into monomer solution
Reaction 30min is stood after uniformly, it is in -80 DEG C to -85 DEG C that control cryostat temperature in initiator solution and reaction process, which is added dropwise,
Within the scope of.The methanol solution that 5mL contains 0.5 weight %NaOH is added into reaction mixture after reaction, to terminate
Polymerisation.Then mixed solution is placed in hot bath and removes solvent, after obtained solid is washed, in vacuum drying oven
In it is dry to constant weight in 60 DEG C, obtain monoolefine-conjugated diene copolymer.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 1.
Comparative example 1
Initiator solution is prepared using method same as Example 6 and is polymerize, unlike, in step (1) not
Use 2,3-, bis- chloro- 5,6- dicyano p-benzoquinones.The molecular weight of polymer yield and polymer, molecular weight distributing index and not
As a result saturation degree is listed in table 1.
Comparative example 2
Initiator solution is prepared using method same as Example 6 and is polymerize, unlike, in step (1) not
It is replaced using the ethyl aluminum dichloride of diethyl aluminum chloride, i.e. diethyl aluminum chloride equimolar amounts.Polymer yield and polymerization
Molecular weight, molecular weight distributing index and the degree of unsaturation of object, are as a result listed in table 1.
Embodiment 7
It is polymerize using method same as Example 6, unlike, in step (2), initiator solution is added dropwise and gathers
It closes in reaction process, by the control of cryostat temperature within the scope of -60 DEG C to -70 DEG C, the dosage of initiator solution is
15mL, polymerization reaction time 40min.The molecular weight of polymer yield and polymer, molecular weight distributing index and unsaturation
Degree, is as a result listed in table 1.
Embodiment 8
It is polymerize using method same as Example 6, unlike, in step (1), the n-hexane of ethyl aluminum dichloride
A concentration of 0.9mol/L of solution, dosage 2mL;A concentration of 1.0mol/L of the n-heptane solution of diethyl aluminum chloride, dosage
For 1.8mL.The molecular weight of polymer yield and polymer, molecular weight distributing index and degree of unsaturation, as a result arrange in table 1
Go out.
Embodiment 9
It is polymerize using method same as Example 8, unlike, in step (2), initiator solution is added dropwise and gathers
It closes in reaction process, by the temperature control of cryostat within the scope of -60 DEG C to -70 DEG C, polymerization reaction time is
40min.The molecular weight of polymer yield and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 10
It is polymerize using method same as Example 8, unlike, in step (2), initiator solution is added dropwise and gathers
It closes in reaction process, by the temperature control of cryostat within the scope of -40 DEG C to -50 DEG C, polymerization reaction time is
50min.The molecular weight of polymer yield and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 11
It is polymerize using method same as Example 6, unlike, in step (1), the n-hexane of ethyl aluminum dichloride
A concentration of 0.9mol/L of solution, dosage 1.2mL;A concentration of 1.0mol/L of the n-heptane solution of diethyl aluminum chloride is used
Amount is 2.5mL.The molecular weight of polymer yield and polymer, molecular weight distributing index and degree of unsaturation, as a result arrange in table 1
Go out.
Embodiment 12
It is polymerize using method identical with 6, unlike, in step (1), digestion time 60min.It polymerize produce
The molecular weight of rate and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 13
It is polymerize using method same as Example 6, unlike, in step (1), digestion time 30min.It is poly-
Produce rate and molecular weight, molecular weight distributing index and the degree of unsaturation of polymer are closed, is as a result listed in table 1.
Embodiment 14
It is polymerize using method same as Example 6, unlike, in step (1), the time of ageing is 10min.
The molecular weight of polymer yield and polymer, molecular weight distributing index and degree of unsaturation, are as a result listed in table 1.
Embodiment 15
It is polymerize using method same as Example 6, unlike, unlike, in step (1), 2,3- bis- is chloro-
5,6- dicyanos with etc. the tetrahydrochysene 1,4-benzoquinone of weight replace.The molecular weight of polymer yield and polymer, molecular weight distribution refer to
Number and degree of unsaturation, are as a result listed in table 1.
Embodiment 16
It is polymerize using method same as Example 6, unlike, unlike, in step (1), 2,3- bis- is chloro-
5,6- dicyanos with etc. the four cyano 1,4-benzoquinone of weight replace.The molecular weight of polymer yield and polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 1.
Embodiment 17
(1) by 0.0576g 2, bis- chloro- 5,6- dicyano p-benzoquinones of 3- be dissolved in 80g and containing HCl it is (a concentration of
In dichloromethane 0.0044mol/L), obtained solution is cooled to -85 DEG C in advance, 0.4mL is sequentially then added into the solution
N-heptane solution (the EADC of the DEAC of a concentration of 1.0mol/L of hexane solution and 3.2mL of the EADC of a concentration of 0.9mol/L
Molar ratio with DEAC is 1/9), after mixing, obtained mixed liquor to be placed in -85 DEG C of cryostat and is aged 60min.Its
In, by weight, the content of 2,3-, bis- chloro- 5,6- dicyano p-benzoquinones is 700ppm in initiator solution.
(2) 200mL two mouth flasks are placed in temperature control in -80 DEG C to -85 DEG C of low temperature cryostat, to be burnt successively to two mouthfuls
N-hexane/monochloro methane mixed solution (wherein, volume ratio of n-hexane/monochloro methane that 85mL is cooled to -85 DEG C is added in bottle
For 9/1), 15mL is cooled to -85 DEG C of isobutene and 0.5mL is cooled to -20 DEG C of isoprene in advance, be uniformly mixed, obtain monomer
Solution.Initiator solution prepared by 10mL steps (1) is added into monomer solution, stands reaction 30min after mixing, is added dropwise
It is within the scope of -80 DEG C to -85 DEG C that cryostat temperature is controlled in initiator solution and reaction process.After reaction to anti-
It answers and the methanol solution that 5mL contains 0.5 weight %NaOH is added in mixture, to terminate polymerisation.Then mixed solution is set
Solvent is removed in hot bath, it is dry to constant weight in 60 DEG C in vacuum drying oven after obtained solid is washed, obtain list
Alkene-conjugated diene copolymer.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Comparative example 3
It is polymerize using with 17 identical method of embodiment, unlike, in step (1), 2,3- bis- chloro- 5 is not used,
6- dicyano p-benzoquinones.The weight of obtained polymer is measured, polymer yield is calculated, and measures the molecular weight of polymer, divide
Son amount profile exponent and degree of unsaturation, are as a result listed in table 2.
Embodiment 18
It is polymerize using with 17 identical method of embodiment, unlike, in step (2), keep n-hexane and a chlorine
The total amount of methane is constant, and the volume ratio for adjusting n-hexane and monochloro methane is 8/2.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 19
It is polymerize using with 17 identical method of embodiment, unlike, in step (2), keep n-hexane and a chlorine
The total amount of methane is constant, and the volume ratio for adjusting n-hexane and monochloro methane is 7/3.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 20
It is polymerize using with 17 identical method of embodiment, unlike, in step (2), keep n-hexane and a chlorine
The total amount of methane is constant, and the volume ratio for adjusting n-hexane and monochloro methane is 6/4.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 21
It is polymerize using with 17 same procedure of embodiment, unlike, in step (2), keep n-hexane and a chloromethane
The total amount of alkane is constant, and the volume ratio for adjusting n-hexane and monochloro methane is 5/5.
The weight of obtained polymer is measured, polymer yield is calculated, and measures the molecular weight and molecular weight point of polymer
As a result cloth index is listed in table 2.
Embodiment 22
(1) by 0.0652g 2, bis- chloro- 5,6- dicyano p-benzoquinones of 3- be dissolved in 80g and containing HCl it is (a concentration of
In dichloromethane 0.0044mol/L), obtained solution is cooled to -85 DEG C in advance, 2.8mL is sequentially then added into the solution
The DEAC of a concentration of 0.9mol/L of hexane solution and 1.2mL of the EADC of a concentration of 0.9mol/L toluene solution (EADC with
The molar ratio of DEAC is 7/3), after mixing, obtained mixed liquor to be placed in -85 DEG C of cryostat and is aged 60min.Its
In, by weight, the content of 2,3-, bis- chloro- 5,6- dicyano p-benzoquinones is 800ppm in initiator solution.
(2) 200mL two mouth flasks are placed in temperature control in -80 DEG C to -85 DEG C of low temperature cryostat, to be burnt successively to two mouthfuls
N-hexane/monochloro methane mixed solution (wherein, volume ratio of n-hexane/monochloro methane that 85mL is cooled to -85 DEG C is added in bottle
For 9/1), 15mL is cooled to -85 DEG C of isobutene and 0.5mL is cooled to -20 DEG C of isoprene in advance, be uniformly mixed, obtain monomer
Solution.Initiator solution prepared by 10mL steps (1) is added into monomer solution, stands reaction 40min after mixing, is added dropwise
It is within the scope of -80 DEG C to -85 DEG C that cryostat temperature is controlled in initiator solution and reaction process.After reaction to anti-
It answers and the methanol solution that 5mL contains 0.5 weight %NaOH is added in mixture, to terminate polymerisation.Then mixed solution is set
Solvent is removed in hot bath, it is dry to constant weight in 60 DEG C in vacuum drying oven after obtained solid is washed, obtain list
Alkene-conjugated diene copolymer.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 23
It is polymerize using with 22 identical method of embodiment, unlike, in step (1), keep EADC's and DEAC
Total amount is constant, and the molar ratio for adjusting EADC and DEAC in initiator solution is 5/5.Measure the weight of obtained polymer, meter
Polymer yield is calculated, and measures the molecular weight, molecular weight distributing index and degree of unsaturation of polymer, is as a result listed in table 2.
Embodiment 24
It is polymerize using with 22 identical method of embodiment, unlike, in step (1), keep EADC's and DEAC
Total amount is constant, and the molar ratio for adjusting EADC and DEAC in initiator solution is 3/7.Measure the weight of obtained polymer, meter
Polymer yield is calculated, and measures the molecular weight, molecular weight distributing index and degree of unsaturation of polymer, is as a result listed in table 2.
Embodiment 25
(1) 0.0651g chloranils are dissolved in 80g and the dichloromethane for containing HCl (a concentration of 0.0042mol/L) is molten
In liquid, obtained solution is cooled to -85 DEG C in advance, the EADC of a concentration of 0.9mol/L of 2.8mL is then sequentially added into the solution
Hexane solution and a concentration of 1.0mol/L of 1.1mL DEAC n-heptane solution (EADC/DEAC molar ratios be 7/3),
After mixing, obtained mixed liquor is placed in -85 DEG C of ageing 60min.Wherein, by weight, tetrachloro pair in initiator solution
The content of benzoquinones is 800ppm.
(2) using being polymerize with 22 identical method of embodiment, unlike, keep the total of n-hexane and monochloro methane
Measure constant, the volume ratio for adjusting n-hexane and monochloro methane is 6/4.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 26
It is polymerize using with 25 identical method of embodiment, unlike, in step (1), keep EADC's and DEAC
Total amount is constant, and the molar ratio for adjusting EADC/DEAC is 5/5.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 27
It is polymerize using with 25 identical method of embodiment, unlike, in step (1), keep EADC's and DEAC
Total amount is constant, and the molar ratio for adjusting EADC/DEAC is 3/7.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Comparative example 4
It is polymerize using with 27 identical method of embodiment, unlike, in step (1), initiator solution is free of four
Chlorine 1,4-benzoquinone.The weight of obtained polymer is measured, polymer yield is calculated, and measures the molecular weight of polymer, molecular weight point
As a result cloth index and degree of unsaturation are listed in table 2.
Embodiment 28
It is polymerize using with 25 identical method of embodiment, unlike, digestion time 30min.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 29
It is polymerize using with 25 identical method of embodiment, unlike, digestion time 10min.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 30
It is polymerize using with 25 identical method of embodiment, unlike, in step (1), the weights such as chloranil uses
The tetrahydrochysene 1,4-benzoquinone of amount replaces.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
Embodiment 31
It is polymerize using with 25 identical method of embodiment, unlike, in step (1), the weights such as chloranil uses
The four cyano 1,4-benzoquinone of amount replaces.
The weight of obtained polymer is measured, calculates polymer yield, and measure the molecular weight of polymer, molecular weight distribution
As a result index and degree of unsaturation are listed in table 2.
The preferred embodiment of the present invention has been described above in detail, still, during present invention is not limited to the embodiments described above
Detail can carry out a variety of simple variants to technical scheme of the present invention within the scope of the technical concept of the present invention, this
A little simple variants all belong to the scope of protection of the present invention.
It is further to note that specific technical features described in the above specific embodiments, in not lance
In the case of shield, can be combined by any suitable means, in order to avoid unnecessary repetition, the present invention to it is various can
The combination of energy no longer separately illustrates.
In addition, various embodiments of the present invention can be combined randomly, as long as it is without prejudice to originally
The thought of invention, it should also be regarded as the disclosure of the present invention.
Claims (31)
1. a kind of cationic polymerization process, this method are included under solution polymerization condition, by least one monoolefine and at least one
Kind conjugated diene is contacted with each component in initiator system in polymer solvent,
The initiator system contains at least one compound for being capable of providing proton, at least one lewis acid and at least one
The molar ratio of activator, the compound for being capable of providing proton and the activator is 1:0.01~3, it is described to be capable of providing matter
The compound of son is 0.01~1 with the lewis acidic molar ratio:1, the compound for being capable of providing proton is H2O and/
Or Bronsted acid, the activator are selected from -2 compound represented of -1 compound represented of Formulas I and Formulas I,
In Formulas I -1 and Formulas I -2, R1、R2、R3、R4、R5、R6、R7And R8Respectively-H ,-X1、-NO2、With one in-CN
Kind, X1And X2One kind respectively in halogen group;
The lewis acid of 10~90 moles of % is lewis acid shown in Formula II,
In Formula II, R9And R10Respectively C1~C8Linear or branched alkyl group, X3For one kind in halogen group;
Remainder lewis acid is formula III compound represented,
In formula III, R11For C1~C8Linear or branched alkyl group, X41And X42One kind respectively in halogen group;
The monoolefine is selected from formula IV compound represented,
In formula IV, R13And R14Respectively C1~C5Linear or branched alkyl group;Or R13For hydrogen, R14For C3~C5Branched alkane
Base;
The conjugated diene is selected from Formula V compound represented,
In Formula V, R15、R16And R17Respectively hydrogen or C1~C5Linear or branched alkyl group.
2. according to the method described in claim 1, wherein, mole of the compound for being capable of providing proton and the activator
Than being 1:0.1~2.8.
3. according to the method described in claim 2, wherein, mole of the compound for being capable of providing proton and the activator
Than being 1:0.2~2.5.
4. according to the method described in claim 3, wherein, mole of the compound for being capable of providing proton and the activator
Than being 1:0.8~1.5.
5. the method according to any one of Claims 1 to 4, wherein the activator is selected from tetrahydrochysene benzoquinones, tetrachlorobenzene
Quinone, four cyano benzoquinones and dichlorocyanobenzoquinone.
6. according to the method described in claim 1, wherein, in Formula II, X3For-Cl.
7. according to the method described in claim 6, wherein, lewis acid shown in Formula II is diethyl aluminum chloride.
8. according to the method described in any one of claim 1,6 and 7, wherein remainder lewis acid is Dichloroethyl
Aluminium.
9. according to the method described in any one of claim 1,6 and 7, wherein the lewis acid of 20~80 moles of % is formula
Lewis acid shown in II.
10. according to the method described in claim 9, wherein, the lewis acid of 30~70 moles of % is Louis shown in Formula II
Acid.
11. according to the method described in any one of claim 1,6 and 7, wherein the compound for being capable of providing proton with
The lewis acidic molar ratio is 0.02~0.5:1.
12. according to the method for claim 11, wherein the compound for being capable of providing proton with it is described lewis acidic
Molar ratio is 0.04~0.3:1.
13. according to the method for claim 12, wherein the compound for being capable of providing proton with it is described lewis acidic
Molar ratio is 0.05~0.1:1.
14. the method according to any one of Claims 1 to 4, wherein the compound for being capable of providing proton is
HCl。
15. according to the method described in claim 1, wherein, the contact carries out within the temperature range of -120 DEG C to 20 DEG C.
16. according to the method for claim 15, wherein the contact carries out within the temperature range of -100 DEG C to 0 DEG C.
17. according to the method for claim 16, wherein the contact carries out within the temperature range of -100 DEG C to -40 DEG C.
18. according to the method for claim 17, wherein the contact carries out within the temperature range of -90 DEG C to -60 DEG C.
19. according to the method described in any one of Claims 1 to 4 and 15~18, wherein by least one monoolefine and extremely
A kind of method that conjugated diene is contacted with each component in the initiator system includes less:It will be in the initiator system
Each component is dissolved in solvent, and obtained mixture is aged, and obtains initiator solution;By the initiator solution and dissolving
The monoolefine in polymer solvent and conjugated diene mixing.
20. according to the method for claim 19, wherein the time of the ageing is 10 minutes to 10 hours.
21. according to the method for claim 20, wherein the time of the ageing is 30 minutes to 5 hours.
22. according to the method for claim 21, wherein the time of the ageing is 60 minutes to 120 minutes.
23. according to the method for claim 19, wherein the ageing carries out within the temperature range of -100 DEG C to 20 DEG C.
24. according to the method for claim 23, wherein the ageing carries out within the temperature range of -100 DEG C to 0 DEG C.
25. according to the method for claim 24, wherein the ageing carries out within the temperature range of -100 DEG C to -50 DEG C.
26. according to the method for claim 25, wherein the ageing carries out within the temperature range of -90 DEG C to -70 DEG C.
27. according to the method described in claim 1, wherein, on the basis of the total amount of the monoolefine and the conjugated diene,
The content of the monoolefine is 80~99.5 weight %;The content of the conjugated diene is 0.5~20 weight %.
28. according to the method for claim 27, wherein using the total amount of the monoolefine and the conjugated diene as base
The content of standard, the monoolefine is 90~98 weight %;The content of the conjugated diene is 2~10 weight %.
29. according to the method described in any one of Claims 1 to 4,15~18,27 and 28, wherein the conjugated diene
For isoprene;And/or
The monoolefine is isobutene.
30. according to the method described in claim 1, wherein, the polymer solvent is selected from alkane and halogenated alkane.
31. according to the method for claim 30, wherein the polymer solvent is selected from C1~C10Halogenated alkane and C3~C10
Alkane.
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