Specific embodiment
The present invention provides a kind of diamine monomers containing asymmetric fluorophore structure, have structure shown in formula I:
In formula I, R1For
R2For
In the present invention, the diamine monomer containing asymmetric fluorophore structure include N-4- methoxyphenyl-N-4- (3,
5- diaminobenzene formamido) phenyl -1- amino pyrene, N-1- (2- methoxyl group naphthalene)-N-4- (3,5- diaminobenzene formamide
Base) phenyl -1- amino naphthalenes or N-1- amino anthracene-N-4- (3,5- diaminobenzene formamido) phenyl -1- amino pyrene.
The present invention also provides the preparation methods of the diamine monomer containing asymmetric fluorophore structure, including following step
It is rapid:
By 4- fluoronitrobenzene, R2-NH2, triethylamine and dimethyl sulfoxide mixing, occur nucleophilic substitution I, had
There is the compound of structure shown in formula II;
By compound, copper powder, potassium carbonate, 18- crown ether -6, R with structure shown in formula II1- X, o-dichlorohenzene mixing, hair
Raw ullmann reaction, obtains the compound with structure shown in formula III;
Compound, Pd/C, hydrazine hydrate and dioxane with structure shown in formula III are mixed, reduction reaction I occurs, obtains
To the compound with structure shown in formula IV;
By compound, triethylamine, N,N-dimethylformamide and 3,5- dinitrobenzene first with structure shown in formula IV
Acyl chlorides mixing, occurs nucleophilic substitution II, obtains the compound with structure shown in formula V;
Compound, Pd/C, hydrazine hydrate and dioxane with structure shown in formula V are mixed, reduction reaction II occurs,
Obtain the compound with structure shown in formula I;
In the present invention, if without specified otherwise, commercial product that all raw materials are well known to the skilled person.
The present invention is by 4- fluoronitrobenzene, R2-NH2, triethylamine and dimethyl sulfoxide mixing, occur nucleophilic substitution I,
Obtain the compound with structure shown in formula II.In the present invention, the 4- fluoronitrobenzene, R2-NH2With mole of triethylamine
Than being preferably 1:(1.3~1.5): (1.3~1.5), more preferably 1:(1.35~1.45): (1.35~1.45).In the present invention
In, the amount of the substance of the 4- fluoronitrobenzene and the volume ratio of dimethyl sulfoxide are preferably (0.9~0.94) mol:1L, more preferably
For (0.91~0.93) mol:1L.
In the present invention, the 4- fluoronitrobenzene, R2-NH2, obtained reaction after triethylamine and dimethyl sulfoxide mixing
The total solid content of system is preferably 15%~28%, and more preferably 16%~27%, most preferably 18%~26%.
In the present invention, the 4- fluoronitrobenzene, R2-NH2It is reactant with triethylamine, the dimethyl sulfoxide is anti-
Answer solvent.
The present invention does not have any special restriction to the addition sequence of above-mentioned raw materials, and it is known that those skilled in the art can be used
Addition sequence mixed;In the present invention, specially first by 4- fluoronitrobenzene, R2-NH2It mixes with triethylamine, then exists
Dimethyl sulfoxide is added in obtained mixture.
In the present invention, the mixing carries out preferably in protective atmosphere, guarantor of the present invention to the offer protective atmosphere
Shield gaseous species do not have any special restriction, specific such as nitrogen using protective gas well known to those skilled in the art.
The present invention does not have any special restriction to the hybrid mode and mixing condition, using those skilled in the art institute
Well known hybrid mode and mixing condition are mixed.
In the present invention, the temperature of the nucleophilic substitution I is preferably 80~100 DEG C, and more preferably 85~95 DEG C, most
Preferably 88~92 DEG C;The time of the nucleophilic substitution I is preferably 30~45h, more preferably 35~42h, most preferably
38~40h.
In the present invention, the nucleophilic substitution I carries out preferably in protective atmosphere, and the present invention is to the offer protection
The protective gas type of atmosphere does not have any special restriction, using protective gas well known to those skilled in the art, tool
Body such as nitrogen.In the present invention, the nucleophilic substitution I preferably carries out under stirring conditions;The present invention is to the stirring
There is no any special restriction, is stirred using stirring condition well known to those skilled in the art.
The present invention does not have any special restriction to the device of the nucleophilic substitution I, using those skilled in the art
The well known device that can be realized above-mentioned reaction is reacted;In the present invention, it can be selected specifically to stir equipped with machinery
The three-neck flask mixed.
After the completion of nucleophilic substitution I, the present invention preferably post-processes obtained product system, and the post-processing is excellent
Choosing the following steps are included:
The product system is mixed with mixture of ice and water, resulting material is filtered, gained filter cake is tied again
Crystalline substance obtains the compound with structure shown in formula II.
The present invention does not have any special restriction to the hybrid mode and condition, and use is well known to those skilled in the art
Hybrid mode and condition mixing.
The present invention filters no any special restriction to described, real using suction filtration condition well known to those skilled in the art
The purpose being now separated by solid-liquid separation.
In the present invention, the reagent of the recrystallization is preferably ethyl alcohol and/or n,N-Dimethylformamide;When the heavy knot
When brilliant reagent is ethyl alcohol and n,N-Dimethylformamide, the present invention is preferably (0.5 to the dosage volume ratio of described two substances
~2): 1, more preferably (0.8~1.2): 1.
After obtaining the compound with structure shown in formula II, the present invention by with structure shown in formula II compound, copper powder,
Potassium carbonate, 18- crown ether -6, R1- X and o-dichlorohenzene mixing, occur ullmann reaction, obtain the chemical combination with structure shown in formula III
Object;The R1X is Cl, Br or I in-X.
In the present invention, compound, copper powder, potassium carbonate, 18- crown ether -6 and the R with structure shown in formula II1- X's
Molar ratio is preferably (1.1~1.5): (3~6): (3~6): (0.5~1): 1, more preferably (1.2~1.4): (4~5.5):
(4~5.5): (0.6~0.8): 1.
In the present invention, the amount of the substance of the compound with structure shown in formula II and the volume ratio of o-dichlorohenzene are excellent
It is selected as (0.1~0.7) mol:1L, more preferably (0.2~0.6) mol:1L.
In the present invention, compound, copper powder, potassium carbonate, the 18- crown ether -6, R with structure shown in formula II1- X with
The total solid content of the reaction system obtained after o-dichlorohenzene mixing is preferably 15%~30%, and more preferably 18%~25%, most
Preferably 20%~23%.
In the present invention, the copper powder is catalyst, and potassium carbonate is co-catalyst, and 18- crown ether -6 is phase transfer catalyst,
O-dichlorohenzene is solvent.
The present invention does not have any special restriction to the mixed sequence, can be mixed in any order.In this hair
In bright, it can be selected specifically to compound, copper powder, potassium carbonate, 18- crown ether -6 and R with structure shown in formula II first1- X is mixed
It closes, o-dichlorohenzene then is added in obtained mixture.
In the present invention, the mixing carries out preferably in protective atmosphere, guarantor of the present invention to the offer protective atmosphere
Shield gaseous species do not have any special restriction, specific such as nitrogen using protective gas well known to those skilled in the art.
The present invention does not have any special restriction to the hybrid mode and mixing condition, using those skilled in the art institute
Well known hybrid mode and mixing condition are mixed.
In the present invention, the temperature of the ullmann reaction is preferably 140~180 DEG C, and more preferably 150~170 DEG C, most
Preferably 155~165 DEG C;The time of the ullmann reaction is preferably 12~20h, more preferably 14~18h.
In the present invention, the ullmann reaction carries out preferably in protective atmosphere, and the present invention is to the offer protection gas
The protective gas type of atmosphere does not have any special restriction, using protective gas well known to those skilled in the art, specifically
Such as nitrogen.In the present invention, the ullmann reaction preferably carries out under stirring conditions;The present invention is to the stirring without appointing
What special restriction, is stirred using stirring condition well known to those skilled in the art.
The present invention does not have any special restriction to the device of the ullmann reaction, using known to those skilled in the art
The device that can be realized above-mentioned reaction reacted;In the present invention, can be selected specifically to equipped with magnetic stir bar,
The three-neck flask of thermometer and condenser pipe.
After the completion of ullmann reaction, the present invention preferably post-processes obtained product system, and the post-processing includes
Following steps:
The product system is filtered, gained filtrate is evaporated under reduced pressure, obtained residue is tied again
Crystalline substance obtains the compound with structure shown in formula III.
The present invention filters no any special restriction to described, real using suction filtration condition well known to those skilled in the art
The purpose being now separated by solid-liquid separation.
The present invention steams the no any special restriction of vacuum distillation using decompression well known to those skilled in the art
It evaporates except o-dichlorohenzene.
In the present invention, the reagent of the recrystallization is preferably the mixture of ethyl alcohol and n,N-dimethylacetamide;At this
In invention, the volume ratio of the ethyl alcohol and n,N-dimethylacetamide is preferably 1:(1~3), more preferably 1:(1.5~2.5).
After obtaining the compound with structure shown in formula III, the present invention by with structure shown in formula III compound, Pd/C,
Hydrazine hydrate and dioxane mixing, occur reduction reaction I, obtain the compound with structure shown in formula IV.In the present invention, institute
State the aqueous solution that hydrazine hydrate is preferably hydrazine hydrate;In the hydrazine hydrate aqueous solution mass fraction of hydrazine hydrate be preferably 70%~
90%, more preferably 75%~85%, most preferably 78%~92%.
In the present invention, the mass ratio of the Pd in the Pd/C and C is preferably (0.05~0.2): 1, more preferably (0.08
~0.15): 1, most preferably (0.1~0.12): 1.
In the present invention, it is described have the compound of structure and the mass ratio of Pd/C shown in formula III be preferably 1:(0.3~
0.4), more preferably 1:(0.32~0.38), most preferably 1:(0.34~0.36).
In the present invention, it is described have the compound of structure and the molar ratio of hydrazine hydrate shown in formula III be preferably 1:(5~
20), more preferably 1:(8~16), most preferably 1:(12~14).
In the present invention, the amount of the substance of the compound with structure shown in formula III and the volume ratio of dioxane are excellent
It is selected as (0.1~0.3) mol:1L, more preferably (0.15~0.25) mol:1L, most preferably (0.18~0.22) mol:1L.
In the present invention, compound, Pd/C, hydrazine hydrate and the dioxane with structure shown in formula III is mixed to get
The total solid content of reaction system be preferably 10%~20%, more preferably 12%~18%, most preferably 14%~16%.
In the present invention, the Pd/C is catalyst, and hydrazine hydrate is reducing agent, and dioxane is solvent.
In the present invention, the mixed sequence is preferably first by compound, Pd/C and two with structure shown in formula III
The mixing of six ring of oxygen, is then added dropwise hydrazine hydrate, the present invention is not any to the dropwise addition of the hydrazine hydrate in obtained mixture again
Special restriction is added dropwise using dropwise addition mode well known to those skilled in the art and drop rate.
In the present invention, the mixing preferably carries out under stirring conditions, and the present invention does not have the condition of the stirring
Any special restriction, is stirred using stirring condition well known to those skilled in the art.
The present invention does not have any special restriction to the hybrid mode and mixing condition, ripe using those skilled in the art
The hybrid mode and mixing condition known are mixed.
In the present invention, the temperature of the reduction reaction I is preferably 70~90 DEG C, and more preferably 75~85 DEG C, most preferably
It is 78~82 DEG C;In the present invention, the reduction reaction I preferably carries out under conditions of reflux.In the present invention, the reduction
The time of reaction I is preferably 1~for 24 hours, more preferably 5~20h, most preferably 10~15h.
In the present invention, the reduction reaction I preferably carries out under stirring conditions;The present invention is to the stirring without appointing
What special restriction, is stirred using stirring condition well known to those skilled in the art.
The present invention does not have any special restriction to the device of the reduction reaction I, using known to those skilled in the art
The device that can be realized above-mentioned reaction reacted;In the present invention, it can be selected specifically to that magnetic stir bar is housed
With the three-neck flask of condenser pipe.
After the completion of reduction reaction I, the present invention preferably post-processes obtained product system, it is described post-processing include with
Lower step:
The product system is filtered, gained filtrate is concentrated under reduced pressure, cools down precipitation, is obtained with IV institute of formula
Show the compound of structure.
The present invention goes the no any special restriction of filtering using filter condition well known to those skilled in the art
Except Pd/C.In the present invention, the filtering is preferably filtered after the completion of reduction reaction I while hot.
It is in the present invention, described to be concentrated under reduced pressure to make the ratio of filtrate volume and original volume after concentration be preferably less than 1,
More preferably less than 0.8, most preferably less than 0.4;No any special restriction is concentrated under reduced pressure to described in the present invention, using this
It is concentrated under reduced pressure known to the technical staff of field.
In the present invention, cooling be precipitated carries out preferably in protective atmosphere, and the present invention is to the offer protective atmosphere
Protective gas type there is no any special restriction, using protective gas well known to those skilled in the art, specifically such as
Nitrogen.
After obtaining the compound with structure shown in formula IV, the present invention is by the compound with structure shown in formula IV, three second
Base amine, n,N-Dimethylformamide and 3, the mixing of 5- dinitrobenzoyl chloride, occur nucleophilic substitution II, obtain with formula V
The compound of shown structure.In the present invention, compound, the triethylamine and 3 with structure shown in formula IV, 5- dinitro
The molar ratio of chlorobenzoyl chloride is preferably 1:(1~1.7): (1~1.7), more preferably 1:(1.2~1.3): (1.2~1.3).
In the present invention, the amount and n,N-Dimethylformamide of the substance of the compound with structure shown in formula IV
Volume ratio is preferably (0.4~0.7) mol:1L, more preferably (0.45~0.65) mol:1L, most preferably (0.5~0.6)
Mol:1L.
In the present invention, compound, the triethylamine, n,N-Dimethylformamide and 3 with structure shown in formula IV,
The total solid content of the reaction system obtained after the mixing of 5- dinitrobenzoyl chloride is preferably 15%~30%, more preferably 20%~
28%, most preferably 22%~26%.
In the present invention, the compound and 3 with structure shown in formula IV, 5- dinitrobenzoyl chloride are reactant,
The n,N-Dimethylformamide is solvent, and the triethylamine is catalyst.
In the present invention, the order by merging be preferably first by with structure shown in formula IV compound, triethylamine and
N,N-Dimethylformamide mixing, then 3,5- dinitrobenzoyl chloride is added dropwise in obtained mixture.In the present invention, described
The amount of the substance of triethylamine and the volume ratio of n,N-Dimethylformamide are preferably (0.6~1.0) mol:1mL, more preferably
(0.7~0.9) mol:1L, most preferably (0.75~0.85) mol:1L.The DNBC 3,5 dinitrobenzoylchloride in the present invention
N,N-Dimethylformamide solution concentration be preferably (1~3.5) mol/L, more preferably (1.5~3) mol/L, most preferably
For (2~2.5) mol/L.The addition of the N,N-dimethylformamide solution of the DNBC 3,5 dinitrobenzoylchloride in the present invention
Temperature is preferably room temperature.The addition side of the N,N-dimethylformamide solution of the DNBC 3,5 dinitrobenzoylchloride in the present invention
Formula is preferably added dropwise;In the present invention, the time of the dropwise addition is preferably 0.5~3h, more preferably 1~2.5h, most preferably
1.5~2h.
After completion of dropwise addition, system temperature reaction that the present invention will obtain;The temperature of the reaction is preferably 130~150 DEG C,
More preferably 135~145 DEG C;In the present invention, the reaction preferably carries out under conditions of reflux.The time of the reaction is excellent
It is selected as 12~20h, more preferably 14~18h, most preferably 15~16h.
In the present invention, the nucleophilic substitution II carries out preferably in protective atmosphere, and the present invention is to the offer guarantor
The protective gas type of shield atmosphere does not have any special restriction, using protective gas well known to those skilled in the art,
Specific such as nitrogen.
The present invention does not have any special restriction to the device of the nucleophilic substitution II, using those skilled in the art
The well known device that can be realized above-mentioned reaction is reacted;In the present invention, it can be selected specifically to stir equipped with magnetic force
Mix the three-neck flask of son, thermometer and condenser pipe.
After the completion of nucleophilic substitution II, the present invention preferably post-processes obtained product system, the post-processing
The following steps are included:
The product system is mixed with ethyl alcohol, resulting material is filtered, obtained filter cake is recrystallized, is obtained
To the compound with structure shown in formula V.
The present invention does not have any special restriction to the hybrid mode and condition, and use is well known to those skilled in the art
Hybrid mode and condition mixing.The present invention does not have any special restriction to the dosage of the ethyl alcohol, using this field skill
Dosage known to art personnel.
The present invention filters no any special restriction to described, real using suction filtration condition well known to those skilled in the art
The purpose being now separated by solid-liquid separation.
In the present invention, the reagent of the recrystallization is preferably ethyl alcohol and n,N-dimethylacetamide;In the present invention, institute
The volume ratio for stating ethyl alcohol and n,N-Dimethylformamide is preferably 1:(2~4), more preferably 1:(2.2~3.8), most preferably
1:(2.8~3.2)
After obtaining the compound with structure shown in formula V, the present invention by with structure shown in formula V compound, Pd/C,
Hydrazine hydrate and dioxane mixing, occur reduction reaction II, obtain the compound with structure shown in formula I.In the present invention, institute
The mass ratio for stating the Pd and C in Pd/C is preferably (0.05~0.2): 1, more preferably (0.5~0.15): 1, most preferably (0.8
~0.12): 1.
In the present invention, it is described have the compound of structure and the mass ratio of Pd/C shown in formula V be preferably 1:(0.1~
0.4), more preferably 1:(0.2~0.3), most preferably 1:(0.24~0.26).
In the present invention, it is described have the compound of structure and the molar ratio of hydrazine hydrate shown in formula V be preferably 1:(15~
40), more preferably 1:(20~30), most preferably 1:(23~27).
In the present invention, the amount of the substance of the compound with structure shown in formula V and the volume ratio of dioxane are excellent
It is selected as (0.1~0.2) mol:1L, more preferably (0.12~0.18) mol:1L, most preferably (0.14~0.16) mol:1L.
In the present invention, compound, Pd/C, hydrazine hydrate and the dioxane with structure shown in formula V is mixed to get
The total solid content of reaction system be preferably 10%~20%, more preferably 12%~18%, most preferably 14%~16%.
In the present invention, the Pd/C is catalyst, and hydrazine hydrate is reducing agent, and dioxane is solvent.
In the present invention, the order by merging is preferably the compound, Pd/C and dioxy that will first have structure shown in formula V
The mixing of six rings, is then added dropwise hydrazine hydrate in obtained mixture again.
In the present invention, the mixing preferably carries out under stirring conditions, and the present invention does not have the condition of the stirring
Any special restriction, is stirred using stirring condition well known to those skilled in the art.
The present invention does not have any special restriction to the hybrid mode and mixing condition, ripe using those skilled in the art
The hybrid mode and mixing condition known are mixed.
In the present invention, the temperature of the reduction reaction II is preferably 75~95 DEG C, and more preferably 80~90 DEG C, most preferably
It is 83~86 DEG C;In the present invention, the reduction reaction II preferably carries out under conditions of reflux.In the present invention, described to go back
The time of original reaction II is preferably 3~30h, more preferably 10~20h, most preferably 12~15h.
In the present invention, the reduction reaction II preferably carries out under stirring conditions;The present invention does not have the stirring
Any special restriction, is stirred using stirring condition well known to those skilled in the art.
The present invention does not have any special restriction to the device of the reduction reaction II, using known to those skilled in the art
The device that can be realized above-mentioned reaction reacted;In the present invention, it can be selected specifically to that magnetic stir bar is housed
With the three-neck flask of condenser pipe.
After the completion of reduction reaction II, the present invention preferably post-processes obtained product system, and the post-processing includes
Following steps:
The product system is filtered, gained filtrate is concentrated under reduced pressure, cooling be precipitated obtains with shown in formula I
The compound of structure.
The present invention goes the no any special restriction of filtering using filter condition well known to those skilled in the art
Except Pd/C.In the present invention, the filtering is preferably filtered after the completion of the reduction reaction II while hot.
In the present invention, the reduced pressure is preferably preferably less than the ratio of filtrate volume and original volume after concentration
1, more preferably less than 0.8, most preferably less than 0.4;No any special restriction is concentrated under reduced pressure to described in the present invention, uses
Reduced pressure well known to those skilled in the art.
In the present invention, cooling be precipitated carries out preferably in protective atmosphere, and the present invention is to the offer protective atmosphere
Protective gas type there is no any special restriction, using protective gas well known to those skilled in the art, specifically such as
Nitrogen;The present invention does not have any special restriction to the cooling detailed process being precipitated, using known to those skilled in the art
Cooling precipitation process.
The present invention also provides the diamine monomers containing asymmetric fluorophore structure in electrochromism and automatically controlled phosphor
Application in material, the electrochromism and automatically controlled fluorescent material are polyamide or polyimides.
In the present invention, the polyamide has structure shown in formula c:
Ar is in the formula c
N is the integer between 30~100.
The polyimides has structure shown in formula d:
Ar' is in the formula d
M is the integer between 30~100.
In the present invention, the preparation method of the polyamide preferably includes following steps:
The diamine monomer containing asymmetric fluorophore structure and the compound with structure shown in formula a are mixed, occurred
Polymerization reaction obtains polyamide;
Ar is in the formula a
In the present invention, the diamine monomer containing asymmetric fluorophore structure and the compound with structure shown in formula a
Molar ratio be preferably 1:1.
In the present invention, the temperature of the polymerization reaction is preferably 110~130 DEG C, more preferably 115~125 DEG C, optimal
It is selected as 118~122 DEG C;The time of the polymerization reaction is preferably 3~6h, more preferably 3.5~6h, most preferably 4~5h.
In the present invention, the polymerization reaction preferably existing for the catalyst under the conditions of carry out;In the present invention, described to urge
Agent is preferably calcium chloride;In the present invention, the quality of the catalyst with containing asymmetric fluorophore structure diamine monomer with
Total mass ratio be preferably (0.15~0.35): 1, more preferably (0.18~0.3): 1.
In the present invention, the polymerization reaction preferably existing for the condensing agent under the conditions of carry out;In the present invention, the contracting
Mixture is preferably triphenyl phosphite and pyridine;In the present invention, the volume ratio of the triphenyl phosphite and pyridine is preferably
(1.8~2.2): 1, more preferably (1.9~2.1): 1.In the present invention, the volume of the triphenyl phosphite with containing asymmetry
The mass ratio of the material of the diamine monomer of fluorophore structure is preferably 1L:(0.8~1.2) mol, more preferably 1L:(0.9~1.1)
mol。
In the present invention, the polymerization reaction preferably existing for the organic solvent under the conditions of carry out;In the present invention, described
Organic solvent is preferably N-Methyl pyrrolidone;In the present invention, the object of the diamine monomer containing asymmetric fluorophore structure
The amount of matter and the volume ratio of solvent are preferably 1mol:(2~3) L, more preferably 1mol:(2.2~2.8) L, most preferably 1mol:
(2.4~2.6) L.
In the present invention, the total solid content of the reaction system of the polymerization reaction is preferably 15%~30%, more preferably
18%~28%, most preferably 22%~26%.
In the present invention, the polymerization reaction carries out preferably in protective atmosphere, and the present invention is to the offer protective atmosphere
Protective gas type there is no any special restriction, using protective gas well known to those skilled in the art, specifically such as
Nitrogen.In the present invention, the polymerization reaction preferably carries out under stirring conditions;The present invention is to the no any spy of stirring
Different restriction is stirred using stirring condition well known to those skilled in the art.
After the completion of polymerization reaction, the present invention preferably post-processes obtained product system, it is described post-processing include with
Lower step:
The product system is mixed with ethyl alcohol, is washed, is dry, obtains polyamide.
The present invention is mixed using mixing condition well known to those skilled in the art to the no any special restriction of mixing
Conjunction;It in the present invention, is in order to which polyamide is precipitated by the purpose that the product system is mixed with ethyl alcohol.
In the present invention, the cleaning solution of the washing is preferably second alcohol and water;The present invention does not have the number of the washing
Any special restriction, the polyamide washes clean that will be obtained.
The present invention any special restriction no to the drying, using drying condition well known to those skilled in the art into
Row is dry.
In the present invention, the preparation method of the polyimides preferably includes following steps:
The diamine monomer containing asymmetric fluorophore structure is mixed with the compound with structure shown in formula b, is occurred
Polymerization reaction obtains polyimides;
Ar' is in the formula b
In the present invention, the diamine monomer containing asymmetric fluorophore structure and the compound with structure shown in formula b
Molar ratio be preferably 1:1.
In the present invention, the temperature of the polymerization reaction is preferably 160~180 DEG C, more preferably 165~175 DEG C, optimal
It is selected as 168~172 DEG C;The time of the polymerization reaction is preferably 8~20h, more preferably 10~18h, most preferably 13~
16h。
In the present invention, the polymerization reaction preferably existing for the isoquinolin under the conditions of carry out.In the present invention, described different
The volume of quinoline and the molar ratio of the diamine monomer containing asymmetric fluorophore structure are preferably (0.03~0.09) L:1mol, more excellent
It is selected as (0.04~0.08) L:1mol.In the present invention, the addition time of the isoquinolin is preferably containing asymmetric fluorescence unity
After the diamine monomer of structure reacts 12~20h at room temperature with the compound with structure shown in formula b, more preferably 14~18h is optimal
It is selected as 15~16h.
In the present invention, the diamine monomer containing asymmetric fluorophore structure and the compound with structure shown in formula b
Reaction at room temperature is polycondensation reaction;Isoquinolin reacts 12 with dianhydride in the diamine monomer containing asymmetric fluorophore structure at room temperature
The effect being added after~20h is dehydration.
In the present invention, the polymerization reaction preferably existing for the organic solvent under the conditions of carry out;In the present invention, described
Solvent is preferably N-Methyl pyrrolidone;In the present invention, the substance of the diamine monomer containing asymmetric fluorophore structure
Volume ratio preferably (0.4~0.6) mol:1L, more preferably (0.45~0.55) mol:1L of amount and solvent, most preferably
(0.48~0.52) mol:1L.
In the present invention, the total solid content of the reaction system of the polymerization reaction is preferably 25%~40%, more preferably
28%~35%, most preferably 30%~32%.
In the present invention, the polymerization reaction carries out preferably in protective atmosphere, and the present invention is to the offer protective atmosphere
Protective gas type there is no any special restriction, using protective gas well known to those skilled in the art, specifically such as
Nitrogen.In the present invention, the polymerization reaction preferably carries out under stirring conditions;The present invention is to the no any spy of stirring
Different restriction is stirred using stirring condition well known to those skilled in the art.
After the completion of polymerization reaction, the present invention preferably post-processes obtained product system, it is described post-processing include with
Lower step:
The product system is mixed with ethyl alcohol, is washed, is dry, obtains polyimides.
The present invention is mixed using mixing condition well known to those skilled in the art to the no any special restriction of mixing
Conjunction;It in the present invention, is that polyimides is precipitated by the purpose that the product system is mixed with ethyl alcohol.
In the present invention, the cleaning solution of the washing is preferably ethyl alcohol;The present invention does not have any spy to the mode of washing
Different restriction is washed using mode of washing well known to those skilled in the art, and in the present invention, the washing can be specific
For reflux washing;The present invention does not have any special restriction to the number of the washing, the polyimides washes clean that will be obtained
?.
The present invention any special restriction no to the drying, using drying condition well known to those skilled in the art into
Row is dry.
Below with reference to embodiment to a kind of diamine monomer and its preparation containing asymmetric fluorophore structure provided by the invention
Method is described in detail, but they cannot be interpreted as limiting the scope of the present invention.