Detailed Description
The invention provides a diamine monomer containing an asymmetric fluorophore structure, which has a structure shown in a formula I:
in the formula I, R
1Is composed of
In the present invention, the diamine monomer containing an asymmetric fluorophore structure includes N-4-methoxyphenyl-N-4- (3, 5-diaminobenzamido) phenyl-1-aminopyrene, N-1- (2-methoxynaphthyl) -N-4- (3, 5-diaminobenzamido) phenyl-1-aminonaphthalene, or N-1-aminoanthracene-N-4- (3, 5-diaminobenzamido) phenyl-1-aminopyrene.
The invention also provides a preparation method of the diamine monomer containing the asymmetric fluorophore structure, which comprises the following steps:
4-fluoronitrobenzene and R2-NH2Mixing triethylamine and dimethyl sulfoxide to perform nucleophilic substitution reaction I to obtain a compound with a structure shown in a formula II;
mixing a compound with a structure shown in formula II, copper powder, potassium carbonate, 18-crown-6 and R1Mixing the-X and the o-dichlorobenzene to perform Ullmann reaction to obtain a compound with a structure shown in a formula III;
mixing a compound with a structure shown in a formula III, Pd/C, hydrazine hydrate and dioxane, and carrying out a reduction reaction I to obtain a compound with a structure shown in a formula IV;
mixing a compound with a structure shown in a formula IV, triethylamine, N-dimethylformamide and 3, 5-dinitrobenzoyl chloride to perform nucleophilic substitution reaction II to obtain a compound with a structure shown in a formula V;
mixing a compound with a structure shown in a formula V, Pd/C, hydrazine hydrate and dioxane to perform a reduction reaction II to obtain a compound with a structure shown in a formula I;
in the present invention, all the raw materials are commercially available products well known to those skilled in the art unless otherwise specified.
The invention uses 4-fluoronitrobenzene and R2-NH2Mixing triethylamine and dimethyl sulfoxide to perform nucleophilic substitution reaction I to obtain a compound with a structure shown in a formula II. In the invention, the 4-fluoronitrobenzene and R2-NH2And triethylamine are preferably present in a molar ratio of 1: (1.3-1.5): (1.3 to 1.5), more preferably 1: (1.35-1.45): (1.35-1.45). In the invention, the volume ratio of the amount of the 4-fluoronitrobenzene substance to the dimethyl sulfoxide is preferably (0.9-0.94) mol:1L, more preferably (0.91 to 0.93) mol:1L of the compound.
In the invention, the 4-fluoronitrobenzene and R2-NH2The total solid content of the reaction system obtained by mixing triethylamine and dimethyl sulfoxide is preferably 15-28%, more preferably 16-27%, and most preferably 18-26%.
In the invention, the 4-fluoronitrobenzene and R2-NH2And triethylamine is used as a reactant, and dimethyl sulfoxide is used as a reaction solvent.
The order of addition of the above-mentioned raw materials is not particularly limited in the present invention, and the addition can be carried out by the order of addition well known to those skilled in the artMixing; in the invention, firstly, 4-fluoronitrobenzene and R are mixed2-NH2And triethylamine were mixed, and then dimethyl sulfoxide was added to the resulting mixture.
In the present invention, the mixing is preferably carried out in a protective atmosphere, and the present invention does not limit the kind of the protective gas for providing the protective atmosphere in any way, and a protective gas known to those skilled in the art, such as nitrogen, may be used.
The mixing method and the mixing conditions are not particularly limited in the present invention, and the mixing may be performed by a mixing method and mixing conditions known to those skilled in the art.
In the invention, the temperature of the nucleophilic substitution reaction I is preferably 80-100 ℃, more preferably 85-95 ℃, and most preferably 88-92 ℃; the time of the nucleophilic substitution reaction I is preferably 30-45 h, more preferably 35-42 h, and most preferably 38-40 h.
In the present invention, the nucleophilic substitution reaction i is preferably carried out in a protective atmosphere, and the kind of the protective gas for providing the protective atmosphere is not particularly limited, and a protective gas known to those skilled in the art, such as nitrogen, may be used. In the present invention, the nucleophilic substitution reaction i is preferably performed under stirring conditions; the stirring is not particularly limited in the present invention, and the stirring may be carried out under stirring conditions known to those skilled in the art.
The device for the nucleophilic substitution reaction I is not limited in any way, and the reaction can be carried out by adopting a device which is well known by the technical personnel in the field and can realize the reaction; in the present invention, a three-neck flask equipped with mechanical stirring can be specifically selected.
After the nucleophilic substitution reaction i is completed, the present invention preferably subjects the resulting product system to a post-treatment, which preferably comprises the steps of:
and mixing the product system with an ice-water mixture, carrying out suction filtration on the obtained material, and recrystallizing the obtained filter cake to obtain the compound with the structure shown in the formula II.
The mixing method and conditions are not limited in any way, and the mixing method and conditions known to those skilled in the art can be used.
The invention does not have any special limitation on the suction filtration, and the aim of solid-liquid separation can be achieved by adopting suction filtration conditions well known to those skilled in the art.
In the present invention, the agent for recrystallization is preferably ethanol and/or N, N-dimethylformamide; when the recrystallization reagent is ethanol and N, N-dimethylformamide, the volume ratio of the two substances is preferably (0.5-2): 1, more preferably (0.8 to 1.2): 1.
after the compound with the structure shown in the formula II is obtained, the invention uses the compound with the structure shown in the formula II, copper powder, potassium carbonate, 18-crown-6 and R1Mixing the-X and o-dichlorobenzene to perform Ullmann reaction to obtain a compound with a structure shown in a formula III; the R is1X in X is Cl, Br or I.
In the present invention, the compound having the structure represented by the formula II, copper powder, potassium carbonate, 18-crown-6 and R1The molar ratio of-X is preferably (1.1-1.5): (3-6): (3-6): (0.5-1): 1, more preferably (1.2 to 1.4): (4-5.5): (4-5.5): (0.6-0.8): 1.
in the present invention, the volume ratio of the amount of the compound having the structure represented by formula ii to o-dichlorobenzene is preferably (0.1 to 0.7) mol:1L, more preferably (0.2 to 0.6) mol:1L of the compound.
In the invention, the compound with the structure shown in the formula II, copper powder, potassium carbonate, 18-crown-6 and R1The total solid content of the reaction system obtained after mixing-X and o-dichlorobenzene is preferably 15-30%, more preferably 18-25%, and most preferably 20-23%.
In the invention, the copper powder is used as a catalyst, potassium carbonate is used as a cocatalyst, 18-crown-6 is used as a phase transfer catalyst, and o-dichlorobenzene is used as a solvent.
The order of mixing is not particularly limited, and the mixing may be performed in any order. In the present invention, it can be specifically selected to firstA compound having a structure represented by formula II, copper powder, potassium carbonate, 18-crown-6 and R1-X and then o-dichlorobenzene is added to the resulting mixture.
In the present invention, the mixing is preferably carried out in a protective atmosphere, and the present invention does not limit the kind of the protective gas for providing the protective atmosphere in any way, and a protective gas known to those skilled in the art, such as nitrogen, may be used.
The mixing method and the mixing conditions are not particularly limited in the present invention, and the mixing may be performed by a mixing method and mixing conditions known to those skilled in the art.
In the invention, the temperature of the Ullmann reaction is preferably 140-180 ℃, more preferably 150-170 ℃, and most preferably 155-165 ℃; the time of the Ullmann reaction is preferably 12-20 h, and more preferably 14-18 h.
In the present invention, the ullmann reaction is preferably carried out in a protective atmosphere, and the kind of the protective gas for providing the protective atmosphere is not particularly limited, and a protective gas known to those skilled in the art, such as nitrogen, may be used. In the present invention, the ullmann reaction is preferably carried out under stirring conditions; the stirring is not particularly limited in the present invention, and the stirring may be carried out under stirring conditions known to those skilled in the art.
The device for the Ullmann reaction is not limited in any way, and the device which can realize the Ullmann reaction and is well known to the technical personnel in the field can be used for carrying out the reaction; in the present invention, a three-necked flask equipped with a magnetic stirrer, a thermometer and a condenser can be specifically selected.
After the Ullmann reaction is finished, the invention preferably carries out post-treatment on the obtained product system, wherein the post-treatment comprises the following steps:
and carrying out suction filtration on the product system, carrying out reduced pressure distillation on the obtained filtrate, and recrystallizing the obtained residue to obtain the compound with the structure shown in the formula III.
The invention does not have any special limitation on the suction filtration, and the aim of solid-liquid separation can be achieved by adopting suction filtration conditions well known to those skilled in the art.
The reduced pressure distillation is not particularly limited in the present invention, and the o-dichlorobenzene may be removed by reduced pressure distillation known to those skilled in the art.
In the present invention, the agent for recrystallization is preferably a mixture of ethanol and N, N-dimethylacetamide; in the present invention, the volume ratio of ethanol to N, N-dimethylacetamide is preferably 1: (1-3), more preferably 1: (1.5-2.5).
After the compound with the structure shown in the formula III is obtained, the compound with the structure shown in the formula III, Pd/C, hydrazine hydrate and dioxane are mixed to carry out reduction reaction I, and the compound with the structure shown in the formula IV is obtained. In the present invention, the hydrazine hydrate is preferably an aqueous solution of hydrazine hydrate; the mass fraction of hydrazine hydrate in the hydrazine hydrate aqueous solution is preferably 70-90%, more preferably 75-85%, and most preferably 78-92%.
In the present invention, the mass ratio of Pd to C in the Pd/C is preferably (0.05-0.2): 1, more preferably (0.08-0.15): 1, most preferably (0.1 to 0.12): 1.
in the present invention, the mass ratio of the compound having the structure represented by the formula iii to Pd/C is preferably 1: (0.3 to 0.4), more preferably 1: (0.32 to 0.38), most preferably 1: (0.34-0.36).
In the present invention, the molar ratio of the compound having the structure represented by formula iii to hydrazine hydrate is preferably 1: (5-20), more preferably 1: (8-16), most preferably 1: (12-14).
In the present invention, the volume ratio of the amount of the substance of the compound having the structure represented by the formula III to dioxane is preferably (0.1 to 0.3) mol:1L, more preferably (0.15 to 0.25) mol:1L, most preferably (0.18 to 0.22) mol:1L of the compound.
In the invention, the total solid content of the reaction system obtained by mixing the compound with the structure shown in the formula III, Pd/C, hydrazine hydrate and dioxane is preferably 10-20%, more preferably 12-18%, and most preferably 14-16%.
In the invention, Pd/C is used as a catalyst, hydrazine hydrate is used as a reducing agent, and dioxane is used as a solvent.
In the present invention, the order of mixing is preferably to mix the compound having the structure shown in formula iii, Pd/C and dioxane, and then to drop hydrazine hydrate into the obtained mixture, and the dropping of hydrazine hydrate is performed by using a dropping manner and a dropping rate well known to those skilled in the art without any particular limitation in the present invention.
In the present invention, the mixing is preferably performed under stirring conditions, and the stirring conditions in the present invention are not particularly limited, and stirring may be performed under stirring conditions known to those skilled in the art.
The mixing manner and mixing conditions are not particularly limited in the present invention, and mixing may be performed by using a mixing manner and mixing conditions known to those skilled in the art.
In the invention, the temperature of the reduction reaction I is preferably 70-90 ℃, more preferably 75-85 ℃, and most preferably 78-82 ℃; in the present invention, the reduction reaction i is preferably carried out under reflux. In the invention, the time of the reduction reaction I is preferably 1-24 h, more preferably 5-20 h, and most preferably 10-15 h.
In the present invention, the reduction reaction i is preferably carried out under stirring; the stirring is not particularly limited in the present invention, and the stirring may be carried out under stirring conditions known to those skilled in the art.
The device for the reduction reaction I is not limited in any way, and the reaction can be carried out by adopting a device which is well known by the technical personnel in the field and can realize the reaction; in the present invention, a three-necked flask equipped with a magnetic stirrer and a condenser can be specifically selected.
After the reduction reaction i is completed, the present invention preferably performs a post-treatment of the resulting product system, said post-treatment comprising the steps of:
and filtering the product system, and carrying out reduced pressure concentration and cooling precipitation on the obtained filtrate to obtain the compound with the structure shown in the formula IV.
The present invention does not have any particular limitation on the filtration, and Pd/C can be removed by using filtration conditions well known to those skilled in the art. In the present invention, the filtration is preferably carried out while it is hot after the reduction reaction I is completed.
In the present invention, the concentration under reduced pressure is performed so that the ratio of the volume of the concentrated filtrate to the original volume is preferably less than 1, more preferably less than 0.8, and most preferably less than 0.4; the concentration under reduced pressure in the present invention is not particularly limited, and may be a concentration under reduced pressure known to those skilled in the art.
In the present invention, the cooling precipitation is preferably performed in a protective atmosphere, and the present invention does not limit the kind of the protective gas providing the protective atmosphere at all, and a protective gas known to those skilled in the art, such as nitrogen, may be used.
After the compound with the structure shown in the formula IV is obtained, the compound with the structure shown in the formula IV, triethylamine, N-dimethylformamide and 3, 5-dinitrobenzoyl chloride are mixed to carry out nucleophilic substitution reaction II, and the compound with the structure shown in the formula V is obtained. In the present invention, the molar ratio of the compound having the structure represented by formula iv, triethylamine and 3, 5-dinitrobenzoyl chloride is preferably 1: (1-1.7): (1 to 1.7), more preferably 1: (1.2-1.3): (1.2-1.3).
In the invention, the volume ratio of the amount of the compound having the structure shown in formula IV to N, N-dimethylformamide is preferably (0.4-0.7) mol:1L, more preferably (0.45 to 0.65) mol:1L, most preferably (0.5-0.6) mol:1L of the compound.
In the invention, the total solid content of the reaction system obtained by mixing the compound having the structure shown in the formula IV, triethylamine, N-dimethylformamide and 3, 5-dinitrobenzoyl chloride is preferably 15-30%, more preferably 20-28%, and most preferably 22-26%.
In the invention, the compound with the structure shown in the formula IV and 3, 5-dinitrobenzoyl chloride are used as reactants, the N, N-dimethylformamide is used as a solvent, and the triethylamine is used as a catalyst.
In the present invention, the mixing sequence is preferably that the compound having the structure represented by formula IV, triethylamine and N, N-dimethylformamide are mixed, and then 3, 5-dinitrobenzoyl chloride is added dropwise to the obtained mixture. In the present invention, the volume ratio of the amount of the triethylamine to the N, N-dimethylformamide is preferably (0.6 to 1.0) mol: 1mL, more preferably (0.7 to 0.9) mol:1L, most preferably (0.75-0.85) mol:1L of the compound. The concentration of the N, N-dimethylformamide solution of the 3, 5-dinitrobenzoyl chloride in the invention is preferably (1-3.5) mol/L, more preferably (1.5-3) mol/L, and most preferably (2-2.5) mol/L. The addition temperature of the solution of 3, 5-dinitrobenzoyl chloride in N, N-dimethylformamide in the present invention is preferably room temperature. The N, N-dimethylformamide solution of the 3, 5-dinitrobenzoyl chloride is preferably added dropwise; in the invention, the dripping time is preferably 0.5-3 h, more preferably 1-2.5 h, and most preferably 1.5-2 h.
After the dropwise addition is finished, the obtained system is subjected to temperature rise reaction; the reaction temperature is preferably 130-150 ℃, and more preferably 135-145 ℃; in the present invention, the reaction is preferably carried out under reflux. The reaction time is preferably 12-20 h, more preferably 14-18 h, and most preferably 15-16 h.
In the present invention, the nucleophilic substitution reaction II is preferably carried out in a protective atmosphere, and the kind of the protective gas for providing the protective atmosphere is not particularly limited, and a protective gas known to those skilled in the art, such as nitrogen, may be used.
The device for the nucleophilic substitution reaction II is not limited in any way, and the reaction can be carried out by adopting a device which is well known by the technical personnel in the field and can realize the reaction; in the present invention, a three-necked flask equipped with a magnetic stirrer, a thermometer and a condenser can be specifically selected.
After the nucleophilic substitution reaction II is completed, the present invention preferably performs a post-treatment of the resulting product system, said post-treatment comprising the steps of:
and mixing the product system with ethanol, carrying out suction filtration on the obtained material, and recrystallizing the obtained filter cake to obtain the compound with the structure shown in the formula V.
The mixing method and conditions are not limited in any way, and the mixing method and conditions known to those skilled in the art can be used. The amount of ethanol used in the present invention is not particularly limited, and may be an amount well known to those skilled in the art.
The invention does not have any special limitation on the suction filtration, and the aim of solid-liquid separation can be achieved by adopting suction filtration conditions well known to those skilled in the art.
In the present invention, the agent for recrystallization is preferably ethanol and N, N-dimethylacetamide; in the present invention, the volume ratio of ethanol to N, N-dimethylformamide is preferably 1: (2-4), more preferably 1: (2.2 to 3.8), most preferably 1: (2.8 to 3.2)
After the compound with the structure shown in the formula V is obtained, the compound with the structure shown in the formula V, Pd/C, hydrazine hydrate and dioxane are mixed to carry out reduction reaction II, and the compound with the structure shown in the formula I is obtained. In the present invention, the mass ratio of Pd to C in the Pd/C is preferably (0.05-0.2): 1, more preferably (0.5-0.15): 1, most preferably (0.8 to 0.12): 1.
in the present invention, the mass ratio of the compound having the structure represented by formula v to Pd/C is preferably 1: (0.1 to 0.4), more preferably 1: (0.2 to 0.3), most preferably 1: (0.24-0.26).
In the present invention, the molar ratio of the compound having the structure represented by formula v to hydrazine hydrate is preferably 1: (15-40), more preferably 1: (20-30), and most preferably 1: (23-27).
In the present invention, the volume ratio of the amount of the substance of the compound having the structure represented by formula V to dioxane is preferably (0.1 to 0.2) mol:1L, more preferably (0.12 to 0.18) mol:1L, most preferably (0.14-0.16) mol:1L of the compound.
In the invention, the total solid content of the reaction system obtained by mixing the compound with the structure shown in the formula V, Pd/C, hydrazine hydrate and dioxane is preferably 10-20%, more preferably 12-18%, and most preferably 14-16%.
In the invention, Pd/C is used as a catalyst, hydrazine hydrate is used as a reducing agent, and dioxane is used as a solvent.
In the present invention, the mixing sequence is preferably that the compound having the structure represented by formula V, Pd/C and dioxane are mixed first, and then hydrazine hydrate is added dropwise to the resulting mixture.
In the present invention, the mixing is preferably performed under stirring conditions, and the stirring conditions in the present invention are not particularly limited, and stirring may be performed under stirring conditions known to those skilled in the art.
The mixing manner and mixing conditions are not particularly limited in the present invention, and mixing may be performed by using a mixing manner and mixing conditions known to those skilled in the art.
In the invention, the temperature of the reduction reaction II is preferably 75-95 ℃, more preferably 80-90 ℃, and most preferably 83-86 ℃; in the present invention, the reduction reaction II is preferably carried out under reflux. In the invention, the time of the reduction reaction II is preferably 3-30 h, more preferably 10-20 h, and most preferably 12-15 h.
In the present invention, the reduction reaction ii is preferably carried out under stirring; the stirring is not particularly limited in the present invention, and the stirring may be carried out under stirring conditions known to those skilled in the art.
The device for the reduction reaction II is not limited in any way, and the reaction can be carried out by adopting a device which is well known by the technical personnel in the field and can realize the reaction; in the present invention, a three-necked flask equipped with a magnetic stirrer and a condenser can be specifically selected.
After the reduction reaction II is completed, the invention preferably carries out post-treatment on the obtained product system, wherein the post-treatment comprises the following steps:
and filtering the product system, concentrating the obtained filtrate under reduced pressure, and cooling to precipitate the compound with the structure shown in the formula I.
The present invention does not have any particular limitation on the filtration, and Pd/C can be removed by using filtration conditions well known to those skilled in the art. In the present invention, the filtration is preferably a hot filtration after the completion of the reduction reaction II.
In the present invention, the concentration under reduced pressure is preferably such that the ratio of the volume of the filtrate after concentration to the original volume is preferably less than 1, more preferably less than 0.8, and most preferably less than 0.4; the concentration under reduced pressure in the present invention is not particularly limited, and may be a concentration under reduced pressure known to those skilled in the art.
In the present invention, the cooling precipitation is preferably performed in a protective atmosphere, and the present invention does not have any particular limitation on the type of protective gas used for providing the protective atmosphere, and protective gases well known to those skilled in the art, such as nitrogen; the specific process of cooling precipitation is not limited in any way, and the cooling precipitation process known to those skilled in the art can be adopted.
The invention also provides application of the diamine monomer containing the asymmetric fluorophore structure in electrochromic and electrically controlled fluorescent materials, wherein the electrochromic and electrically controlled fluorescent materials are polyamide or polyimide.
In the present invention, the polyamide has a structure represented by formula c:
n is an integer of 30 to 100.
The polyimide has a structure shown in a formula d:
m is an integer of 30 to 100.
In the present invention, the method for producing the polyamide preferably comprises the steps of:
mixing the diamine monomer containing the asymmetric fluorophore structure with a compound with a structure shown in a formula a, and carrying out polymerization reaction to obtain polyamide;
In the present invention, the molar ratio of the diamine monomer containing an asymmetric fluorophore structure to the compound having the structure represented by formula a is preferably 1: 1.
in the invention, the polymerization reaction temperature is preferably 110-130 ℃, more preferably 115-125 ℃, and most preferably 118-122 ℃; the time of the polymerization reaction is preferably 3 to 6 hours, more preferably 3.5 to 6 hours, and most preferably 4 to 5 hours.
In the present invention, the polymerization reaction is preferably carried out in the presence of a catalyst; in the present invention, the catalyst is preferably calcium chloride; in the invention, the ratio of the mass of the catalyst to the total mass of the diamine monomer containing the asymmetric fluorophore structure is preferably (0.15-0.35): 1, more preferably (0.18 to 0.3): 1.
in the present invention, the polymerization reaction is preferably carried out in the presence of a condensing agent; in the present invention, the condensing agent is preferably triphenyl phosphite and pyridine; in the invention, the volume ratio of triphenyl phosphite to pyridine is preferably (1.8-2.2): 1, more preferably (1.9 to 2.1): 1. in the present invention, the ratio of the volume of triphenyl phosphite to the amount of the diamine monomer containing an asymmetric fluorophore structure is preferably 1L: (0.8 to 1.2) mol, more preferably 1L: (0.9-1.1) mol.
In the present invention, the polymerization reaction is preferably carried out in the presence of an organic solvent; in the present invention, the organic solvent is preferably N-methylpyrrolidone; in the present invention, the ratio of the amount of the substance containing the diamine monomer having an asymmetric fluorophore structure to the volume of the solvent is preferably 1 mol: (2-3) L, more preferably 1 mol: (2.2-2.8) L, most preferably 1 mol: (2.4-2.6) L.
In the present invention, the total solid content of the reaction system of the polymerization reaction is preferably 15% to 30%, more preferably 18% to 28%, and most preferably 22% to 26%.
In the present invention, the polymerization reaction is preferably carried out in a protective atmosphere, and the kind of the protective gas for providing the protective atmosphere is not particularly limited, and a protective gas known to those skilled in the art, such as nitrogen, may be used. In the present invention, the polymerization reaction is preferably carried out under stirring conditions; the stirring is not particularly limited in the present invention, and the stirring may be carried out under stirring conditions known to those skilled in the art.
After the polymerization reaction is completed, the present invention preferably performs a post-treatment on the obtained product system, wherein the post-treatment comprises the following steps:
and mixing the product system with ethanol, washing and drying to obtain the polyamide.
The present invention does not have any particular limitation in the mixing, and the mixing may be carried out under mixing conditions well known to those skilled in the art; in the present invention, the purpose of mixing the product system with ethanol is to precipitate out the polyamide.
In the present invention, the washing liquid for washing is preferably ethanol and water; the invention does not have any special limitation on the washing times, and the obtained polyamide is washed cleanly.
The drying method of the present invention is not particularly limited, and drying may be carried out under drying conditions known to those skilled in the art.
In the present invention, the preparation method of the polyimide preferably includes the steps of:
mixing the diamine monomer containing the asymmetric fluorophore structure with a compound having a structure shown in a formula b, and carrying out polymerization reaction to obtain polyimide;
In the present invention, the molar ratio of the diamine monomer containing an asymmetric fluorophore structure to the compound having the structure represented by formula b is preferably 1: 1.
in the invention, the polymerization reaction temperature is preferably 160-180 ℃, more preferably 165-175 ℃, and most preferably 168-172 ℃; the time of the polymerization reaction is preferably 8-20 h, more preferably 10-18 h, and most preferably 13-16 h.
In the present invention, the polymerization reaction is preferably carried out in the presence of isoquinoline. In the invention, the molar ratio of the volume of the isoquinoline to the diamine monomer containing the asymmetric fluorophore structure is preferably (0.03-0.09) L: 1mol, more preferably (0.04 to 0.08) L:1 mol. In the invention, the addition time of the isoquinoline is preferably 12-20 h, more preferably 14-18 h, and most preferably 15-16 h after the diamine monomer containing the asymmetric fluorophore structure reacts with the compound having the structure shown in the formula b at room temperature.
In the invention, the reaction of the diamine monomer containing the asymmetric fluorophore structure and the compound with the structure shown in the formula b at room temperature is polycondensation reaction; the isoquinoline reacts with diamine monomer containing asymmetric fluorophore structure and dianhydride at room temperature for 12-20 h, and then is dehydrated.
In the present invention, the polymerization reaction is preferably carried out in the presence of an organic solvent; in the present invention, the solvent is preferably N-methylpyrrolidone; in the present invention, the volume ratio of the amount of the diamine monomer containing an asymmetric fluorophore structure to the solvent is preferably (0.4 to 0.6) mol:1L, more preferably (0.45 to 0.55) mol:1L, and most preferably (0.48 to 0.52) mol: 1L.
In the present invention, the total solid content of the reaction system of the polymerization reaction is preferably 25% to 40%, more preferably 28% to 35%, and most preferably 30% to 32%.
In the present invention, the polymerization reaction is preferably carried out in a protective atmosphere, and the kind of the protective gas for providing the protective atmosphere is not particularly limited, and a protective gas known to those skilled in the art, such as nitrogen, may be used. In the present invention, the polymerization reaction is preferably carried out under stirring conditions; the stirring is not particularly limited in the present invention, and the stirring may be carried out under stirring conditions known to those skilled in the art.
After the polymerization reaction is completed, the present invention preferably performs a post-treatment on the obtained product system, wherein the post-treatment comprises the following steps:
and mixing the product system with ethanol, washing and drying to obtain the polyimide.
The present invention does not have any particular limitation in the mixing, and the mixing may be carried out under mixing conditions well known to those skilled in the art; in the present invention, the purpose of mixing the product system with ethanol is to precipitate polyimide.
In the present invention, the washing liquid is preferably ethanol; the washing method is not limited in any way, and the washing method known to those skilled in the art is adopted for washing, and in the invention, the washing can be specifically reflux washing; the invention does not have any special limitation on the washing times, and the obtained polyimide is washed cleanly.
The drying method of the present invention is not particularly limited, and drying may be carried out under drying conditions known to those skilled in the art.
The diamine monomer containing an asymmetric fluorophore structure and the preparation method thereof provided by the present invention will be described in detail with reference to the following examples, which should not be construed as limiting the scope of the present invention.