CN114790290B - Synthesis method of hydroxyl modified biphenyl structure PBO composite monomer - Google Patents

Synthesis method of hydroxyl modified biphenyl structure PBO composite monomer Download PDF

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CN114790290B
CN114790290B CN202210513685.4A CN202210513685A CN114790290B CN 114790290 B CN114790290 B CN 114790290B CN 202210513685 A CN202210513685 A CN 202210513685A CN 114790290 B CN114790290 B CN 114790290B
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biphenyl structure
composite monomer
modified biphenyl
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pbo composite
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CN114790290A (en
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赵德明
杜文杰
张建庭
吴纯鑫
金宁人
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Zhejiang University of Technology ZJUT
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G73/00Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
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    • C08G73/22Polybenzoxazoles
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    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/88Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/94Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of other polycondensation products

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Abstract

A synthetic method of a hydroxyl modified biphenyl structure PBO composite monomer comprises the following steps: taking 2, 5-dihydroxyterephthalic acid as a raw material, adding sodium hydroxide and deoxidized water in a nitrogen atmosphere, and then heating to 30-50 ℃ for neutralization reaction for 0.2-0.5 hour to obtain an intermediate sodium 2, 5-dihydroxyterephthalate; then, intermediate sodium 2, 5-dihydroxyterephthalate and 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride are used as raw materials, stannous chloride is added in a nitrogen atmosphere, and the mixture reacts for 0.3 to 0.6 hour at the temperature of 60 to 80 ℃ to obtain a white solid product of the hydroxyl modified biphenyl structure PBO composite monomer. The reaction process parameters of the scheme of the invention are easy to control, no toxic byproducts are generated, the atomic utilization rate is high, the yield is high, the purity is high, and the post-treatment is simple.

Description

Synthesis method of hydroxyl modified biphenyl structure PBO composite monomer
Field of the art
The invention relates to a synthesis method of a hydroxyl modified biphenyl structure PBO composite monomer.
(II) background art
The compound monomer shown in the formula (1) is a raw material for preparing the hydroxy-modified poly-p-phenylene benzobisoxazole by polymerization, and can be applied to the fields of high-performance fibers, photoelectric materials, heat-resistant materials and the like (Lu Shanshan, wang Yangong, hu Zhen. Research progress of poly-p-phenylene benzobisoxazole fiber modification technology, synthetic fiber industry, 2018,41 (1): 47-52.).
At present, the polymerization method of the hydroxyl modified poly (p-phenylene benzobisoxazole) carries out mixed polycondensation reaction in polyphosphoric acid at high temperature by using 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 2, 5-dihydroxyterephthalic acid, and has the defects that the equal equivalent ratio of two monomers is difficult to uniformly polycondense to influence the polymerization effect, the HCl removal process influences the fiber strength and the like. Therefore, starting from the polymerization method of PBO fiber, a hydroxyl modified biphenyl structure PBO composite monomer is synthesized, and the composite monomer is utilized to carry out self-polycondensation reaction under the condition of high temperature in polyphosphoric acid. (Wu Chunxin, chang Yuxi, chen Di, supra.) Synthesis of hydroxy-modified poly (p-phenylene benzobisoxazole) monomer 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride, chemical progress, 2020,39 (2): 696-701.
In view of the above-described situation of hydroxy-modified poly-p-phenylene benzobisoxazole, we have sought to provide a new method for synthesizing hydroxy-modified biphenyl structural PBO complex monomers that is industrially easy to achieve more rationally.
Content of the invention
The invention aims to provide a method for preparing a high-purity hydroxyl modified biphenyl structure PBO composite monomer, which ensures the equivalent ratio of two monomers, has high reaction selectivity, short reaction time, high atom utilization rate, simple post-treatment and high yield and is industrially feasible.
In order to achieve the aim, the invention adopts the following technical scheme:
in a first aspect, the invention provides a hydroxyl modified biphenyl structure PBO composite monomer shown in formula (1),
in a second aspect, the present invention provides a method for synthesizing a hydroxy-modified biphenyl structure PBO monomer represented by the above formula (1), where the method is as follows:
taking 2, 5-dihydroxyterephthalic acid as a raw material, adding sodium hydroxide and deoxidized water in a nitrogen atmosphere, and then heating to 30-50 ℃ (preferably 40-50 ℃) to perform neutralization reaction for 0.2-0.5 hour (preferably 0.3-0.4 h) to obtain a solution containing an intermediate sodium 2, 5-dihydroxyterephthalate; adding 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and a reducing agent, reacting for 0.3-0.6 hours (preferably 0.5-0.6 hours) at 60-80 ℃ (preferably 70-80 ℃), and performing post-treatment on the obtained reaction liquid to obtain the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1); the mass ratio of the 2, 5-dihydroxyterephthalic acid to the sodium hydroxide is 1:0.3 to 0.5 (preferably 1:0.4 to 0.45); the mass ratio of the 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride to the 2, 5-dihydroxyterephthalic acid is 1:0.6 to 0.9 (preferably 1:0.7 to 0.74); the mass ratio of the reducing agent to the 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride is 1: 90-110 (preferably 1:100-110); the reducing agent is stannous chloride, ferrous sulfate or sodium sulfate (preferably stannous chloride).
Further, the volume of the deoxidized water is 20 to 40mL/g (preferably 25.5 mL/g) based on the mass of the 2, 5-dihydroxyterephthalic acid.
Further, the post-treatment is as follows: filtering the obtained reaction liquid with deoxidized water, and vacuum drying the obtained filter cake to obtain the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1).
The invention is to wash and filter with deoxidized water after the reaction is finished to remove sodium chloride which is a water-soluble product and a reducing agent which is added, and obtain the water-insoluble hydroxyl modified biphenyl structure PBO composite monomer. In addition, the reducing agent such as stannous chloride has a reducing property of preventing the amino group of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride from being oxidized.
The invention also provides an application of the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1) in preparing modified PBO fibers.
Specifically, the application is: under the protection of nitrogen, stirring and reacting a polyphosphoric acid mixture containing phosphorus pentoxide, a hydroxyl modified biphenyl structure PBO composite monomer shown in a formula (1) and phosphorus pentoxide for 1 hour at 100 ℃, continuously heating to 120 ℃ and reacting for 1 hour, 140 ℃ and reacting for 1 hour, 160 ℃ and reacting for 1 hour, 180 ℃ and reacting for 1 hour, and then manually drawing, washing and drying the liquid crystal stock solution obtained after the liquid crystal stock solution is heated to 190 ℃ and reacting for 1 hour to obtain the hydroxyl modified biphenyl structure PBO fiber;
the total mass of phosphorus pentoxide and phosphorus pentoxide contained in the phosphorus pentoxide-containing polyphosphoric acid mixture is 85-90% (preferably 87%) of the total mass of phosphorus pentoxide-containing polyphosphoric acid mixture and phosphorus pentoxide; the mass of the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1) is 10-20% (preferably 16%) of the total mass of the polyphosphoric acid mixture containing phosphorus pentoxide, the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1) and phosphorus pentoxide.
Further, the polyphosphoric acid mixture containing phosphorus pentoxide (polyphosphoric acid in the examples) was purchased from Shanghai Michelia Biochemical technology Co., ltd., lot#: C12710785, and the phosphorus pentoxide content was not less than 85%.
Compared with the prior art, the invention has the beneficial effects that: the invention provides a method for preparing a high-purity hydroxyl modified biphenyl structure PBO composite monomer, which ensures the equivalent ratio of two monomers, has high reaction selectivity, short reaction time, high atom utilization rate, simple post-treatment, high yield and industrial feasibility, and the obtained PBO composite monomer has better polymerization effect for synthesizing modified PBO fibers, improves thermal stability and reflects the larger molecular weight of polymers.
(IV) description of the drawings
Fig. 1: for the HPLC diagram of example 1, the analysis conditions were: column temperature 35 ℃, mobile phase 60% methanol-water buffer solution, ODS C 18 The detection wavelength of the chromatographic column (6.0X106 mm) was 254nm, and the flow rate was 1.0mL/min.
Fig. 2: for the HPLC diagram of example 2, the analysis conditions were: column temperature 35 ℃, mobile phase 60% methanol-water buffer solution, ODS C 18 The detection wavelength of the chromatographic column (6.0X106 mm) was 254nm, and the flow rate was 1.0mL/min.
Fig. 3: for the HPLC diagram of example 3, the analysis conditions were: column temperature 35 ℃, mobile phase 60% methanol-water buffer solution, ODS C 18 The detection wavelength of the chromatographic column (6.0X106 mm) was 254nm, and the flow rate was 1.0mL/min.
Fig. 4: for the HPLC diagram of example 4, the analysis conditions were: column temperature 35 ℃, mobile phase 60% methanol-water buffer solution, ODS C 18 The detection wavelength of the chromatographic column (6.0X106 mm) was 254nm, and the flow rate was 1.0mL/min.
Fig. 5: for the HPLC diagram of example 5, the analysis conditions were: column temperature 35 ℃, mobile phase 60% methanol-water buffer solution, ODS C 18 The detection wavelength of the chromatographic column (6.0X106 mm) was 254nm, and the flow rate was 1.0mL/min.
(fifth) detailed description of the invention
The present invention will be described in more detail by way of examples, but the scope of the present invention is not limited by the examples.
Example 1
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and 3.63g of white solid product hydroxyl modified biphenyl structure PBO composite monomer is obtained, the mass fraction of HPLC analysis is 98.36%, and the yield is 80.10%.
FT-IR(KBr,cm -1 ):3610.8(s),3368.9(s),1658.8(s),1417.8(s),1355.1(s),1108.3(s)。
1 H-NMR(DMSO,δ,ppm):7.23(2H,s,CH),6.91(2H,s,CH),6.75(4H,s,CH)。
HPLC analysis conditions of the hydroxyl modified biphenyl structure PBO composite monomer: ODS C 18 Column, 6.0X105 mm, mobile phase: methanol/water buffer=60/40 (V/V), detection wavelength 254nm, flow rate 1.0mL/min.
Examples 2 to 10
Examples 2 to 10, which are obtained by using the same operation steps as in example 1 and taking different parameters according to the parameter ranges described in the present invention, show that the purity of the obtained hydroxy-modified biphenyl structure PBO composite monomer is above 91% under these process conditions, and the net yield of the hydroxy-modified biphenyl structure PBO composite monomer product is above 67%, and can be applied to the industrial synthesis of the hydroxy-modified biphenyl structure PBO composite monomer.
Example 2
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 40 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and 3.64g of white solid product of hydroxyl modified biphenyl structure PBO composite monomer is obtained, and the HPLC analysis mass fraction is 96.73%, and the yield is 78.99%.
Example 3
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.5h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, and a filter cake is dried in vacuum to obtain a white solid product, namely 3.55g of the hydroxyl modified biphenyl structure PBO composite monomer, wherein the mass fraction of the HPLC analysis is 94.10%, and the yield is 74.95%.
Example 4
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 60 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, and a filter cake is dried in vacuum to obtain 3.43g of white solid product, namely the hydroxyl modified biphenyl structure PBO composite monomer, with the mass fraction of 93.99 percent by HPLC analysis, and the yield is 72.33 percent.
Example 5
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride are added into a four-neck flask, and the temperature is continuously increased to 80 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, and a filter cake is dried in vacuum to obtain 3.44g of white solid product, namely the hydroxyl modified biphenyl structure PBO composite monomer, with the mass fraction of 91.08 percent by HPLC analysis, and the yield is 70.29 percent.
Example 6
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride are added into a four-neck flask, and the temperature is continuously increased to 70 ℃ to react for 0.3h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and 3.23g of white solid product hydroxyl modified biphenyl structure PBO composite monomer is obtained, the mass fraction of HPLC analysis is 93.21%, and the yield is 67.55%.
Example 7
Into a four-neck flask equipped with a stirring, condensing tube and thermometer, 2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 0.94g of sodium hydroxide are added, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and 3.38g of white solid product of hydroxyl modified biphenyl structure PBO composite monomer is obtained, the mass fraction of HPLC analysis is 95.56%, and the yield is 72.47%.
Example 8
2.35g of 2, 5-dihydroxyterephthalic acid, 47mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, and a filter cake is dried in vacuum to obtain 3.47g of white solid product, namely the hydroxyl modified biphenyl structure PBO composite monomer, with the mass fraction of 94.78 percent by HPLC analysis, and the yield is 73.79 percent.
Example 9
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 2.61g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.03g of stannous chloride are added into a four-necked flask, and the temperature is continuously increased to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and 3.28g of white solid product of hydroxyl modified biphenyl structure PBO composite monomer is obtained, the mass fraction of HPLC analysis is 93.72%, and the yield is 68.97%.
Example 10
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.05g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, and a filter cake is dried in vacuum to obtain 3.68g of white solid product, namely the hydroxyl modified biphenyl structure PBO composite monomer, with the mass fraction of 92.34 percent by HPLC analysis, and the yield is 76.24 percent.
Examples 11 to 13
The preparation process of example 1 was adopted, and conditions outside the parameters described in the present invention were adopted for the test, so that the obtained product was poor in effect.
Example 11
2.35g of 2, 5-dihydroxyterephthalic acid, 30mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.05g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, and a filter cake is dried in vacuum to obtain 3.27g of white solid product, namely the hydroxyl modified biphenyl structure PBO composite monomer, with the mass fraction of 82.34 percent by HPLC analysis, and the yield is 60.41 percent.
Example 12
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 2g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.05g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 70 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and a white solid product of the hydroxyl modified biphenyl structure PBO composite monomer 3.67g is obtained, and the HPLC analysis mass fraction is 80.56 percent, and the yield is 66.33 percent.
Example 13
2.35g of 2, 5-dihydroxyterephthalic acid, 60mL of deoxidized water and 1g of sodium hydroxide are added into a four-neck flask with a stirring pipe, a condensing pipe and a thermometer, nitrogen is introduced, stirring is started, heating is carried out, the reaction temperature is controlled to be 50 ℃, and neutralization reaction is carried out for 0.3h. 3.2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 0.05g of stannous chloride were added into a four-necked flask, and the temperature was continuously raised to 90 ℃ to react for 0.6h. After the reaction is finished, the mixture is filtered by deoxidized water, a filter cake is dried in vacuum, and 3.52g of white solid product of hydroxyl modified biphenyl structure PBO composite monomer is obtained, the mass fraction of HPLC analysis is 78.67%, and the yield is 62.13%.
Example 14
Weighing 3.55g of synthesized PBO composite monomer with a hydroxyl modified biphenyl structure, 2.70g of phosphorus pentoxide (the content is more than or equal to 98 percent), 15.70g of polyphosphoric acid (Hn+2PnO3n+1, shanghai microphone Biochemical technology Co., ltd., lot#: C12710785, the phosphorus pentoxide content is more than or equal to 85 percent), sequentially adding the mixture into a glass reactor, introducing nitrogen into the reactor, starting stirring, heating to 100 ℃ for reaction for 1h, blackening the reaction system mixture, continuously heating to 120 ℃ for reaction for 1h, 140 ℃ for reaction for 1h, 160 ℃ for reaction for 1h, and 180 ℃ for reaction for 1h, and heating to 190 ℃ for reaction for 1h to obtain yellow fluorescence, thereby reaching the reaction end point. After the polymerization reaction is finished, the liquid crystal stock solution is manually drawn by a clean glass rod, and the obtained monofilament fiber is put into hot water to wash out excessive polyphosphoric acid. The monofilament fiber was dried in vacuo at 100℃to give a reddish brown modified PBO fiber.
Comparative example 1
2g of 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and 15g of polyphosphoric acid (Hn+2PnO3n+1, shanghai microphone Biochemical technology Co., ltd., lot#: C12710785, phosphorus pentoxide content more than or equal to 85%) are weighed and added into a glass reactor, nitrogen is introduced into the reactor, stirring is started, the temperature is raised to 80 ℃ for carrying out a HCl removal process, after 7h, pH test paper is used for detecting to be neutral, 1.5g of 2, 5-dihydroxyterephthalic acid is added, 2.5g of phosphorus pentoxide (content more than or equal to 98%) is added, the temperature is raised to 100 ℃ for reaction for 1h, the reaction system mixture turns black, the temperature is raised to 120 ℃ for reaction for 1h, the temperature is raised to 140 ℃ for reaction for 1h, the temperature is raised to 160 ℃ for reaction for 1h, the temperature is raised to 190 ℃ for reaction for 1h, and a small amount of yellow fluorescence is generated until the reaction end point is reached. After the polymerization reaction is finished, the liquid crystal stock solution is manually drawn by a clean glass rod, and the monofilament fiber is put into hot water to wash out excessive polyphosphoric acid, so that small-section solid is obtained. The small solid segments were dried in vacuo at 100deg.C to give purple modified PBO fibers.
TABLE 1
Compared with the two monomer mixing polycondensation methods, the method has the following positive effects: (1) The reaction process parameters of the composite monomer method provided by the invention are easy to control, the equivalent ratio polymerization of the two monomers is ensured, the degassing process is avoided, the reaction time can be greatly shortened, the reaction efficiency is improved, the energy consumption is less, and the industrial feasibility is higher. (2) The composite monomer method adopted by the invention for synthesizing the modified PBO fiber has better wiredrawing effect, improves the thermal stability and reflects the larger molecular weight of the polymer.

Claims (6)

1. A synthesis method of a hydroxyl modified biphenyl structure PBO composite monomer shown in a formula (1) is characterized by comprising the following steps:
taking 2, 5-dihydroxyterephthalic acid as a raw material, adding sodium hydroxide and deoxidized water in a nitrogen atmosphere, and then heating to 30-50 ℃ for neutralization reaction for 0.2-0.5 hour to obtain a solution containing an intermediate sodium 2, 5-dihydroxyterephthalate; adding 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride and a reducing agent, reacting for 0.3-0.6 hour at 60-80 ℃, and performing post-treatment on the obtained reaction liquid to obtain the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1); the mass ratio of the 2, 5-dihydroxyterephthalic acid to the sodium hydroxide is 1:0.3 to 0.5; the mass ratio of the 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride to the 2, 5-dihydroxyterephthalic acid is 1:0.6 to 0.9; the mass ratio of the reducing agent to the 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride is 1: 90-110; the reducing agent is stannous chloride, ferrous sulfate or sodium sulfate.
2. The method for synthesizing the hydroxy-modified biphenyl structure PBO composite monomer shown in formula (1) in claim 1, which is characterized in that: the volume of the deoxidized water is 20-40 mL/g based on the mass of the 2, 5-dihydroxyterephthalic acid.
3. The method for synthesizing the hydroxy-modified biphenyl structure PBO composite monomer shown in formula (1) in claim 1, which is characterized in that: the reducing agent is stannous chloride.
4. The method for synthesizing the hydroxy-modified biphenyl structure PBO composite monomer shown in formula (1) in claim 1, which is characterized in that: the mass ratio of the 2, 5-dihydroxyterephthalic acid to the sodium hydroxide is 1:0.4 to 0.45.
5. The method for synthesizing the hydroxy-modified biphenyl structure PBO composite monomer shown in formula (1) in claim 1, which is characterized in that: the mass ratio of the 3,3 '-diamino-4, 4' -dihydroxybiphenyl hydrochloride to the 2, 5-dihydroxyterephthalic acid is 1:0.7 to 0.74.
6. The method for synthesizing a hydroxyl-modified biphenyl structure PBO composite monomer represented by formula (1) according to claim 1, wherein the post-treatment is: filtering the obtained reaction liquid with deoxidized water, and vacuum drying the obtained filter cake to obtain the hydroxyl modified biphenyl structure PBO composite monomer shown in the formula (1).
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