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    • 专利摘要:
    The invention relates to a process for the solvothermal synthesis of polyimides by solution polymerization of monomers in a suitable solvent by mixing the solvent and the monomers and heating the mixture under pressure to above the respective boiling point at atmospheric pressure, characterized in that crystalline polyimides are prepared by a ) mixing and heating the solvent and the monomers is carried out by either a 1) heating the solvent to solvothermal conditions, after which the monomers are added to initiate the reaction, or a2) the monomers are mixed with the solvent and the mixture is heated to solvothermal conditions within 5 minutes, the reaction temperature TR being maintained in a solid state during the polymerization under the polymerization temperature TP of the monomers; and b) the solution polymerization is carried out until substantially complete, the conversion has been achieved.
    公开号:AT517148A2
    申请号:T20/2016
    申请日:2016-01-20
    公开日:2016-11-15
    发明作者:Miriam Margarethe Dr Unterlass；Bettina Bsc Baumgartner
    申请人:Technische Universität Wien；
    IPC主号:
    专利说明:

    The invention relates to the preparation of crystalline polyimides by solvothermal synthesis.
    STATE OF THE ART
    Polyimides are valuable materials for various applications. Their synthesis is usually carried out by polycondensation of diamines with dianhydrides in solution, in the melt or even in a solid state. Surprisingly, it was found several years ago that - despite the elimination of water during the condensation reaction - even water can be used as a solvent for the polyimide synthesis, when so-called "hydrothermal conditions" prevail, to understand a reaction under pressure at temperatures above 100 ° C. (See Hodgkin et al., "Water as a Polymerization Solvent-cyclization of Polyimides: Le Chatelier Confounded", Polym. Prep. (American Chemical Society, Division of Polymer Chemistry) 41, 208 (2000), and WO 99/06470). , When solvents other than water are used, the term "solvothermal conditions" is used at temperatures above their boiling points.
    The mechanism of this condensation reaction proceeds in two stages through the formation of amic acids, which subsequently undergo cyclodehydration to the corresponding imides. Dao et al. In 1999, factors significantly influencing the imidization reaction were investigated (Dao, Hodgkin and Morton, "Important Factors Controlling Synthesis of Imides in Water", High Perform Polym. 11, 205-218 (1999), "Dao 1999") and under Others noted that the higher the temperature of the imidization reaction, the more pure the products.
    The reason why the reaction equilibrium of this dehydration-proceeding cyclization, even in water, as a solvent on the product side, is the changed properties of the solvent under solvothermal conditions. For example, water behaves like a pseudo-organic solvent under these conditions (Hodgkin et al., Supra).
    Furthermore, it is customary to form a stoichiometric salt of diamide and dianhydride prior to the polymerization, which usually takes place by simply mixing the monomers into water and filtering off the salts precipitated in water. The anhydrides undergo hydrolysis to give the free tetracarboxylic acids, of which two carboxyl groups each having one amino group form an ammonium salt (Unterlass et al., "Mechanistic study of hydrothermal synthesis of aromatic polyimides", Polym. Chem. 2011,2, 1744). In the monomer salts thus obtained, which are sometimes referred to as "AH salts" (in analogy to polyamide and especially nylon synthesis), the two monomers are thus present exactly in a molar ratio of 1: 1, which is why their subsequent polymerization leads to very pure polyimides , Below is an example of the reaction scheme of two typical aromatic monomers:
    Diamine dianhydride monomer salt polyimide
    Another modern technology that has been used for several years to synthesize organic compounds and, more recently, polyimides is microwave radiation, which significantly reduces reaction times and increases the selectivity of reactions (Lindstrom et al., "Microwave Assisted Organic Synthesis: a Review ", Tetrahedron 57, 9225-9283 (2001); Perreux et al.," A Tentative Rationalization of Microwave Effects in Organic Synthesis According to the Reaction Medium and Mechanistic Considerations ", Tetrahedron 57, 9199-9223 (2001)). Microwaves have also been used in the synthesis of polyimides (Lewis et al., Accelerated Imidization Reactions using Microwave Radiation, J. Polym., Part A: Polym. Chem. 30, 1647-1653 (1992) and US 5,453. 161).
    However, so far only two reports of a microwave-assisted hydrothermal synthesis of polyimides are known: On the one hand, Dao et al. (Dao, Groth and Hodgkin, "Microwave-assisted Aqueous Polyimidization Using High-throughput Techniques", Macromol Rapid Commun., 28, 604-607 (2007); "Dao 2007") using a series trial of a ternary monomer mixture of a diamine (4,4-Oxydi-aniline, ODA) and two dianhydrides (4,4 '- (hexafluoroisopropylidene) diphthalsäureanhy-drid, 6-FDA, pyromellitic dianhydride, PMDA) at temperatures between 120 ° C and 200 ° C found that the best Results at 180-200 ° C can be achieved if the goal is the highest possible molecular weight of the thereby obtained random (block) copolymers of the following formula:
    And on the other hand, only a few years ago Brunei et al. (Brunei, Marestin, Martin and Mercier, "Waterborne Polyimides via Microwave-assisted Polymerization", High Perform Polym. 22, 82-94 (2010)) using a binary polyimide of ODA and 4,4 '- (4, 4'-isopropylidenediphenoxy) bis (phthalic anhydride) (bisphenol A dianhydride, BPADA)
    once again confirms that microwave use significantly reduces the reaction times, i. can be shortened from 4 to 12 h to only 5 to 10 min. The sales generated in this short time, however, are extremely low at only about 20%.
    In addition, the crystallinity of the products played no role in both microwave-assisted hydrothermal syntheses of polyimides: In Dao 2007 (see above), apart from the molecular weight and the solubility in organic solvents, there are no other details regarding the nature of the polyimides obtained. Of course, no crystalline product could be obtained with the ternary system investigated there-nor was it intended, since the polyimides prepared were investigated with a view to their use for membranes. For this, good solubility in organic solvents was the goal in order to be able to cast films by means of such solutions. And Brunei et al. (see above) explicitly disclose (see p. 89) that amorphous products have been obtained throughout. Since their goal was also cast polyimide films (from m-cresol solutions), the crystallinity of the polyimides also played no role in this case.
    A very recent technology is the production of covalent organic frameworks (COF), for which large-pore crystalline polyimides can sometimes be used (Fang et al., "Designed synthesis of large-pore crystalline polyimide covalent organic frameworks", Nature Communications 5, 4503 (2014)). For these purposes, of course, highly crystalline polyimides are needed and amorphous products or those with high amorphous shares completely unsuitable.
    Against this background, the aim of the invention was the development of an economical process for the production of highly pure, highly crystalline polyimides which are as pure as possible.
    DISCLOSURE OF THE INVENTION
    This object is achieved by providing a process for the solvothermal synthesis of crystalline polyimides by solution polymerization of monomers in a suitable solvent by mixing the solvent and the monomers and heating the mixture under pressure to temperatures above the respective boiling point at atmospheric pressure, characterized in that Substantially completely crystalline polyimides can be prepared by a) mixing and heating the solvent and monomers by either a1) heating the solvent to solvothermal conditions, after which the monomers are added to initiate the reaction, or a2 ) the monomers are mixed with the solvent and the mixture is heated to solvothermal conditions within 5 min, the reaction temperature Tr during the polymerization below the polymerization temperature or the polymerization temperature Tp of the monomers in fes condition is maintained; and b) the solution polymerization is carried out until substantially complete conversion has been achieved.
    This method is based on several new findings of the inventors: First, that the crystallinity of polyimides produced by solvothermal and in particular hydrothermal synthesis is higher, the lower the proportion of monomers dissolved in the solvent before reaching the solvothermal conditions. Therefore, either the monomers and the solvent should be brought together as quickly as possible to solvothermal conditions, i. within 5 minutes, preferably within 3 minutes, more preferably within 2 minutes and especially within only 1 minute, to heat to a temperature above the boiling point of the solvent. Or the solvent is actually heated separately from the monomers, and the latter are added only when solvothermal conditions exist. - Second, that when heated together monomers and solvents, the reaction temperature TR below the polymerization temperature Tp of the monomers in the solid state, which can be determined for example by means of thermogravimetric analysis (TGA), to hold, otherwise also increase the amorphous levels in the product. Preferably, therefore, in the above step a2) according to the present invention, the polymerization is carried out at a reaction temperature TR which is at least 5 ° C, more preferably at least 10 ° C, below the Tp to obtain as completely as possible crystalline polyimides.
    And thirdly, with separate heating of solvent and monomers and subsequent mixing, the monomers are heated so rapidly by the hot solvent that there is virtually no possibility for the monomers to go into solution before they reach reaction temperature and initiate the polymerization. In step a1) of the process according to the invention therefore no limitation of the reaction temperature is required.
    Such a limitation of the reaction temperature in the customary common heating according to step a2) of the process according to the invention is of course diametrically opposed to the accepted doctrine according to which the imidization reaction is to be carried out at as high a temperature as possible (Dao 1999, supra, Dao 2007, supra).
    For comparison: Brunei et al. Although their reaction mixtures were rapidly heated by microwave radiation, they chose - as taught by Dao et al. - A reaction temperature of 200 ° C and received throughout amorphous products. The present inventors have now determined by means of TGA (see FIG. 1) that the Tp of Brunei et al. used monomer mixture of ODA and BPADA at 148 ° C and Brunei et al. Thus, the polymerization reactions were carried out at a temperature which was 52 ° C above the Tp, and moreover, the reactions have ended after a few minutes, rather than waiting for substantially complete conversion, as provided for by the present invention.
    The present invention is not limited to the use of diamines and dianhydrides as monomers, but higher amines and / or anhydrides can be used, such. Tri- or tetraamine or anhydride. In order to obtain crosslinked polyimides which are suitable for use in the covalent organic networks (COF) mentioned in the beginning (see Fang et al., Supra), higher-valent monomers are even preferred according to the invention. The reaction mechanism in the polycondensation of higher-valent monomers or mixtures of di- and higher-valent monomers and the principle of the invention are of course substantially the same as for divalent educts, and therefore the latter examples will be used in the later examples for illustrative purposes. Nevertheless, when mention is made of "diamines", "dianhydrides" and "tetracarboxylic acids", higher-value monomers are also to be regarded as implicitly disclosed, unless the context does not exclude this. For obtaining substantially pure, highly crystalline
    In all cases, the most exact possible stoichiometry of the monomer mixtures is crucial in all cases.
    Preferably, therefore, according to the present invention, stoichiometric salts (monomer salts, "AH salts") having a molar ratio between diamine and dianhydride of 1: 1 are formed in a step a) preceding additional step from the monomers to reduce the proportion of unreacted monomers in To keep the polyimides as low as possible. When using higher-value monomers in the process of the present invention, of course, in this additional, preparatory process step, salts having other molar ratios corresponding to the valence of the monomers are obtained, that is to say with a ratio of 3: 2 for combination of diamines with trianhydrides (or conversely, dianhydrides with triamines ) etc.
    The solvent is limited in the process of the invention only in so far as the solubility of the monomers or of the stoichiometric salt thereof should be sufficiently low therein and, above all, the boiling point is below the Tp of the two monomer components. However, in view of the cost and possible environmental impact, preference is given to using water or else one or more alcohols or a mixture of water and alcohol (s) as solvent, in particular water, so that the present invention, in particularly preferred embodiments, a process for the hydrothermal synthesis of polyimides provides.
    As the monomer component (s), it is preferable to use an aromatic diamine and / or an aromatic tetracarboxylic dianhydride according to the present invention. Even more preferably, both components are aromatic, since on the one hand this increases the rigidity of the polymer chains, which promotes crystallization, and on the other hand reduces the solubility in the inventively preferred solvents water and alcohol. In particular, for the purposes of the present invention, the monomer used is a stoichiometric salt of an aromatic diamine and of an aromatic tetracarboxylic dianhydride or of higher aromatic amines and anhydrides.
    Since the heating time should be as short as possible until the solvothermal conditions according to the present invention are reached, so that only the smallest possible proportion of the monomer components can go into solution, the process of the invention comprises, in particular according to step a1) the separate heating of the solvent to solvothermal conditions and only subsequent addition of the monomers to the hot solvent, since such an in-solution migration of the monomers before reaching the solvothermal conditions is completely excluded. Owing to the fact that the equipment required is very high and the results achieved with the alternative according to step a2), the joint heating of monomers and solvent as rapidly as possible in some cases may also be preferred over a1).
    In this case, "as fast as possible joint heating" in preferred embodiments includes the use of microwave radiation, since this procedure (as mentioned above) is now a proven technique in organic synthesis and therefore particularly preferred according to the present invention. However, it will be apparent to those skilled in the art that, depending on the nature of the reactors, other types of rapid heating of reaction mixtures, e.g. optical heating methods by means of infrared lasers or the like, at least provide comparable results and are therefore to be considered in principle as equivalent to microwave radiation.
    Which method is used depends largely on the type of monomers and the resulting tendency of the polyimides to crystallize and the solubility of the monomers in the solvent. If the monomers are practically insoluble therein, then, with sufficiently high temperature difference between the heating medium and the desired solvent temperature during the polymerization reaction, conventional heating by means of (very hot) heating baths or forced air furnaces can give very good results. Especially if e.g. aromatic or other monomers with high rigidity of the molecular structure are used, as the later embodiments prove. Generally, however, as mentioned, care must be taken to ensure that the time until solvothermal conditions are reached is not more than 5 minutes, preferably not more than 3 minutes, more preferably not more than 2 minutes, in particular not more than 1 minute, when the solvent in step a2) is heated together with the monomers.
    BRIEF DESCRIPTION OF THE DRAWINGS
    In the following, the present invention will be further described with reference to specific embodiments and the accompanying drawings, the latter of which show the following.
    Fig. 1 is the TGA curve of the monomer mixture according to Brunei et al. (so.).
    Fig. 2 is the XRD pattern of the polyimide obtained in Example 1 of the invention.
    Fig. 3 is a SEM photograph of the polyimide of Example 1 of the invention.
    Fig. 4 is the XRD pattern of the polyimide obtained in Example 3 of the invention.
    Fig. 5 is an SEM photograph of the polyimide of Example 3 of the invention.
    Fig. 6 is the XRD pattern of the polyimide obtained in Example 4 of the invention.
    Fig. 7 is the XRD pattern of the polyimide obtained in Example 5 of the invention.
    Fig. 8 is the XRD pattern of the polyimide obtained in Example 6 of the invention.
    Fig. 9 is the XRD pattern of the polyimide obtained in Example 8 of the invention.
    Fig. 10 is the XRD pattern of the polyimide obtained in Example 9 of the invention.
    Fig. 11 is the XRD pattern of the polyimide obtained in Example 10 of the invention.
    Fig. 12 is the XRD pattern of the polyimide obtained in Example 11 of the invention.
    EXAMPLES
    All starting materials used for the following polyimide hydrothermal syntheses were obtained from a commercial source and used without further purification. Thermo-gravimetric analyzes were performed on a TG 209 Analyzer by Netzsch and IR spectroscopy on a Bruker Tensor 27. X-ray powder diffractograms were taken on an X'Pert Pro multi-purpose diffractometer from PANalytical, and Scanning Electron Microscopy was performed on a Quanta 200F FEI.
    Abbreviations HT: hydrothermal XRD: X-ray diffraction IR: Infrared spectrometry TGA: Thermogravimetric analysis SEM: Scanning electron microscopy PDA: p-phenylenediamine, 1,4-diaminobenzene PMA: pyromellitic acid, benzene-1,2,4,5-tetracarboxylic acid PMDA: pyromellitic dianhydride, benzene-1, 2,4,5-tetracarboxylic dianhydride PPPDI: poly (p-phenylene pyromellitic diimide) BTA: benzophenone-3,3 ', 4,4'-tetracarboxylic acid BTDA: benzophenone-3,3', 4,4'-tetracarboxylic dianhydride PPBTDI: poly (p -phenylenbenzophenontetracarbonsäurediimid)
    Bz: benzidine, 4,4'-diaminobiphenyl PBBTDI: poly (p-biphenylenebenzophenonetetracarboxylic acid diimide) TAPB 1,3,5-tris (4-aminophenyl) benzene PBTPPDI poly (benzenetri (p-phenylene) pyromellitic diimide)
    Xa: degree of crystallinity
    Example 1 - Preparation of poly (p-phenylene pyromellitic diimide), PPPDI
    PDA PMDA monomer salt PPPDI a) Preparation of the monomer salt [H2PDA2 + PMA2] 0.327 g of PMDA were placed under inert atmosphere in a three-necked flask with reflux condenser and dissolved in 15 ml of dist. Water dissolved. The solution was heated to 80 ° C and, with stirring, 0.162 g of PDA was added, immediately precipitating the monomer salt as a white powder. The mixture was stirred for a further 2 hours, after which the salt was filtered off and dried in vacuo. TGA of the dry monomer salt gave a polymerization temperature Tp in the solid state of 205 ° C. b) HT polymerization
    The monomer salt was distilled in 15 ml. Water, placed in a non-stirred autoclave and heated to HT conditions and finally to 200 ° C within 4.5 min. After 1 h at this reaction temperature, the autoclave was rapidly cooled to room temperature and the PPPDI formed was filtered off, washed with distilled water and dried in vacuo at 40 ° C overnight.
    The PPPDI was orange and fully imidated as determined by FT-ATR-IR (1783 cm'1 (C = 0 imide); 1709 cm * 1 (C = 0 imide); 1365 cm * 1 (CN)), where no vibrations of the monomers or the monomer salt were detectable. By means of powder XRD, complete crystallinity of the product, which was in the form of two solid crystalline phases, i. no amorphous shares detected. The degree of crystallinity χα was therefore> 99%. Fig. 2 shows the XRD pattern of the obtained polyimide. SEM showed a very homogeneous, ordered morphology of the obtained PPPDI, which is further proof of the extremely high degree of crystallinity. Fig. 3 shows the SEM image of the polyimide.
    Example 2 - Production of PPPDI on a larger scale
    PDA PMDA monomer salt PPPDI
    The procedure of Example 1 was substantially repeated except that the monomer salt was formed from 8.72 g of PMDA and 4.33 g of PDA in 400 distilled water. This monomer salt (Tp 205 ° C) was subsequently heated in a stirred reactor in an autoclave within 4 min on HT conditions and finally also to 200 ° C and the product was isolated and dried as in Example 1. The purity and crystallinity of this PPPDI determined by means of IR and XRD were in accordance with the product from Example 1: Xcr> 99%.
    Without wishing to be bound by theory, it is believed that, in addition to the low water solubility of the monomers, the high rigidity of the resulting polyimide is crucial for this high degree of crystallinity of the PPPDI obtained, since the repeating units in the polymer composition are largely planar due to mesomeric effects.
    Example 3 - Preparation of poly (p-phenylenebenzophenone tetracarboxylic acid diimide), PPBTDI
    PDA BTDA PPBTDI
    Analogously to the procedure of Example 1, 0.48 g (1.5 mmol) of BTDA in 15 ml of dist. Water with 0.11 g of PDA with stirring - but at room temperature - to the monomer salt [H2PDA2 + BTA2] reacted whose Tp was determined by TGA at 149 ° C and then in an autoclave in 15 ml of water without stirring within 5 min on HT And finally heated to 140 ° C and then polycondensed for 12 hours to the polyimide PPBTI. IR of the brownish crystals showed complete imidation (1781 cm -1 (C = 0 imide), 1717 cm -1 (C = 0 imide), 1378 cm -1 (CN)), since again no oscillations of the monomers or of the monomer salt were recognizable were. The crystallinity was examined by Pul-ver-XRD. Fig. 4 shows the XRD pattern of the PPBTDI, with the curve of the crystalline peaks being underlapped with a Gaussian curve representing approximately the proportion of amorphous structures. From the areas under the two curves a calculated crystallinity degree χα of about 62% was obtained. The SEM illustrated in FIG.
    However, incorporation of the polyimide still showed a highly ordered morphology of the resulting PPBTDI.
    Example 4 - Preparation of poly (p-biphenylenebenzophenonetetracarboxylic acid diimide), PBBTDI
    Bz BTDA PBBTDI
    Analogously to the procedure of Example 3 were 0.48 g (1.5 mmol) of BTDA in 15 ml of dist. Water with 0.22 g of Bz with stirring to the monomer salt [H2Bz2 + BTA2 '], whose Tp was determined by TGA at 172 ° C and then in non-stirred autoclave in 15 ml of water within 4.5 min on HT conditions and finally heated to 160 ° C and then polycondensed for 12 hours to the polyimide PBBTDI. IR of the brownish crystals in turn showed complete imidation (1786 cm'1 (C = 0 imide), 1709 cm'1 (C = 0 imide), 1389 cm-1 (CN)), since here too no vibrations of the monomers or of the monomer salt were recognizable. The crystallinity was examined by powder XRD. Fig. 6 shows the XRD pattern of the PBBTDI, again calculating the degree of crystallinity from the areas under the curve of the crystalline peaks and below the underlying Gaussian curve for the amorphous parts, giving an Xcr of about 61%.
    The significantly lower crystallinity of the PPBTDI from Example 3 and the PBBTDI from Example 4 compared to the PPPDI from Examples 1 and 2 is attributed to the higher water solubility of the benzophenone tetracarboxylic acid BTA without wishing to be bound by theory.
    Example 5 - Preparation of PPBTDI using microwave radiation
    PDA BTDA PPBTDI
    Example 3 was substantially repeated, but heating was by means of microwave radiation, so that the hydrothermal conditions were reached after less than 2 minutes, and the polymerization reaction was essentially complete after only 1 h.
    Full imidization was also detected by IR in this case, and Fig. 7 shows the powder XRD pattern of the obtained dried PPBTDI. From the areas under the curve of the crystalline peaks and the underlying Gaussian curve, a degree of crystallinity yCr of about 93% results, which is as much as 31 percentage points above the 62% of the product from example 3. The significantly faster microwave heating - 2 min in Example 5 instead of 4 min in Example 3 - thus caused a significant increase in crystallinity by 50%, as apparently even lower levels of the monomer salt could go into solution before HT conditions were reached ,
    Example 6 - Preparation of PBBTDI using microwave radiation
    Bz BTDA PBBTDI
    Example 4 was essentially repeated, but heating was by means of microwave radiation, so that the hydrothermal conditions were reached after less than 2 minutes, and the polymerization reaction was essentially complete after only 1 h.
    Full imidization was also detected by IR in this case, and Fig. 8 shows the powder XRD pattern of the obtained dried PBBTDI. The areas under the curve of the crystalline peaks and the underlying Gaussian curve give a degree of crystallinity Xcr of about 80%, which is a full 19 percentage points higher than the 61% of the product of example 4. The much faster heating by means of microwaves-2 min in Example 6 instead of 4.5 min in Example 4-resulted in a significant increase in crystallinity of about 30%, since apparently even lower proportions of the monomer salt could go into solution before HT- Conditions were reached.
    Example 7 - Preparation of PPPDI in ethanol
    PDA PMDA monomer salt PPPDI
    Example 2 was essentially repeated, except that the monomer salt was suspended in 400 ml of ethanol instead of in water for polymerization. The reaction (after heating within 4.5 min on HT conditions and finally to 200 ° C) and workup were also carried out analogously to Example 2.
    Complete imidization was also noted in this case by IR, and the powder XRD pattern almost exactly matched that of Example 1 (see Figure 2).
    Thus, it has been demonstrated that the polycondensation of PDA and PMDA to a highly crystalline polyimide can also be carried out in a protic solvent other than water with the same excellent results.
    Example 8 - Preparation of the crosslinked polyimide poly (benzenetri (p-phenylene) -pyromellitic diimide), PBTPPDI, using microwave radiation
    TAPB PMDA
    I 1
    PBTPPDI
    The procedure of Example 3 was substantially repeated except that 0.06 g (0.3 mmol) of PMDA was reacted with 0.07 g (0.2 mmol) of TAPB to form the monomer salt [(H3TAPB3 +) 2 (PMA2) 3] , whose Tp was determined by means of TGA at 152 ° C and then in non-stirred autoclave in 15 ml of water using microwaves in 2 min on HT conditions and finally heated to 140 ° C and then polycondensed for 12 hours to the polyimide PBTPPDI. IR of the dried brown crystals again showed complete imidation (1785 cnr1 (C = 0 imide), 1723 cm * 1 (C = 0 imide), 1390 cm'1 (CN)), as here too no vibrations of the monomers or of the monomer salt can be seen were. The crystallinity was examined by powder XRD. Fig. 9 shows the XRD pattern of the PBTPPDI, in which no amorphous portions are to be recognized, from which a degree of crystallinity χα of> 99% follows.
    Example 9 - Preparation of PPPDI by injection of the monomers into separately heated solvent
    PDA PMDA monomer salt PPPDI
    The monomer salt was prepared according to Example 1a), but in a 10-fold approach. The salt thus obtained was distilled in 100 ml. Water was dispersed, and the dispersion was transferred to a high-pressure steel pipette, which was connected to a stirrer equipped with a 1-liter steel reactor, but separated by a valve from the reaction chamber, in the 400 ml dist. Water were submitted. The apparatus was placed in an autoclave and the water in the reaction chamber under the appropriate autogenous pressure to 200 ° C heated. Upon reaching this reaction temperature, the valve was opened and the monomer dispersion was injected into the preheated solvent by inert gas pressure in less than 30 seconds. Subsequently, the reaction mixture was stirred for 1 h at 200 ° C, after which complete conversion was found and the product was isolated and dried as in Example 1.
    The purity and crystallinity of this PPPDI determined by IR and XRD were consistent with the product of Example 1 (the XRD pattern is shown in Figure 10). There were no oscillations of the monomers or the monomer salt and no amorphous shares recognizable, so that a degree of crystallinity χα was found to be close to 100%.
    Example 10 - Preparation of PPBTDI by injection of the monomers into separately heated solvent
    PDA BTDA PPBTDI
    Analogously to the procedure of Example 9, the reaction of PDA with BTDA in the ten-fold approach of Examples 3 and 5 was carried out, but after the injection of the monomer in the preheated solvent, the reaction mixture was stirred for 4 h at 200 ° C to complete conversion to guarantee.
    The IR and XRD peaks of the resulting PPBTDI were consistent with those of Examples 3 and 5, but in the present case, virtually no amorphous portions were observed, giving χα> 99%. The associated XRD pattern is shown in FIG. The product obtained after separate preheating of the solvent was thus still significantly purer than that of Example 5, since virtually no monomers had gone into solution.
    Example 11 - Preparation of PBBTDI by injection of the monomers into separately heated solvent
    Bz BTDA PBBTDI
    Analogously to the procedure of Example 9, the reaction of Bz with BTDA in the ten-fold approach of Examples 4 and 6 was carried out, but after the injection of the monomer dispersion in the preheated solvent, the reaction mixture was stirred for 4 h at 200 ° C to complete conversion to guarantee.
    The IR and XRD peaks of the PPBTDI obtained were in agreement with those of Examples 4 and 6, but in the present case even fewer amorphous fractions were detectable, whereby approximately a χσ> 90% was determined. The associated XRD pattern is shown in FIG. The product obtained after separate preheating of the solvent was thus still significantly purer than that of Example 6, since virtually no monomers had gone into solution, whereby the crystallinity compared to Example 6 could be increased by at least another 10 percentage points.
    In summary, the results of the above examples, as listed in Table 1 below, demonstrate the excellent crystallinity of the polyimides prepared according to the present invention, which can be further enhanced by increasing the rate of heating by microwave radiation and separately preheating the solvent. However, for structures with extremely low water solubility, heating by means of heating or circulating air is sufficient to achieve excellent degrees of crystallinity.
    Table 1
    Tp: polymerization temperature in the solid state
    Tr: reaction temperature MW: microwaves GE: separate heating of the solvent
    The advantages of preferred embodiments of the process according to the invention are particularly evident in comparisons of Examples 1, 2 and 9 for the production of PPPDI, Examples 3, 5 and 10 for the preparation of PPBTDI and de Examples 4, 6 and 11 for the production of PBBTDI. Rapid microwave heating significantly improves the crystallinity over conventional heating of the reaction mixtures. However, this can be further increased by separate preheating of the solvent to solvothermal conditions and subsequent addition of the monomer salt, since in this way virtually no monomers can go into solution before the polymerization temperature is reached.
    In the latter case, therefore, the reaction temperature need not be kept in a solid state below the polymerization temperature Tp of the monomers, although in certain cases this may still be preferred.
    The invention thus provides an improved process for the preparation of polyimides by solvothermal synthesis which provides products of significantly higher crystallinity than was possible in the prior art.
    权利要求:
    Claims (9)
    [1]
    A process for the solvothermal synthesis of polyimides by solution polymerization of monomers in a suitable solvent by mixing the solvent and the monomers and heating the mixture under pressure to above the respective boiling point at normal pressure, characterized in that crystalline polyimides are prepared by: a) the The solvent and the monomers are mixed and heated by either a1) heating the solvent to solvothermal conditions, after which the monomers are added to initiate the reaction, or a2) the monomers are mixed with the solvent and the mixture is heated to solvothermal conditions within 5 minutes, during which the reaction temperature Tr is kept in a solid state under the polymerization temperature Tp of the monomers; and b) the solution polymerization is carried out until substantially complete conversion has been achieved.
    [2]
    2. The method according to claim 1, characterized in that the mixture of monomers and solvent in step a2) within 3 min, preferably within 2 min, in particular within 1 min, is heated to solvothermal conditions.
    [3]
    3. The method according to claim 2, characterized in that the mixture of monomers and solvent in step a2) is heated by means of microwave radiation.
    [4]
    4. The method according to any one of claims 1 to 3, characterized in that in a Schitt a) preceding, additional step from the monomers stoichiometric salts in a molar ratio between diamine and dianhydride of 1: 1 are formed.
    [5]
    5. The method according to any one of the preceding claims, characterized in that the reaction temperature Tr is maintained at least 5 ° C, preferably at least 10 ° C, below the polymerization temperature Tp of the monomers in a solid state.
    [6]
    6. The method according to any one of the preceding claims, characterized in that the solvent used is water, one or more alcohols or a mixture of water and alcohol (s).
    [7]
    7. The method according to any one of the preceding claims, characterized in that as the monomer (s) an aromatic diamine and / or an aromatic tetracarboxylic dianhydride is / are used.
    [8]
    8. The method according to claim 7, characterized in that a stoichiometric salt of an aromatic di- or triamine and an aromatic tetracarboxylic dianhydride is used as the monomer.
    [9]
    9. The method according to any one of the preceding claims, characterized in that substantially completely crystalline polyimides are prepared.
    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    WO2016179625A1|2016-11-17|
    JP6994946B2|2022-01-14|
    BR112017024199A2|2019-01-22|
    AT517148A3|2019-04-15|
    CA2985820A1|2016-11-17|
    AT517146A2|2016-11-15|
    JP2018514635A|2018-06-07|
    US10563013B2|2020-02-18|
    EP3294794A1|2018-03-21|
    AT517148B1|2019-07-15|
    US20180112039A1|2018-04-26|
    EP3294794B1|2021-11-24|
    引用文献:
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    US5288843A|1987-05-20|1994-02-22|Mitsui Toatsu Chemicals, Inc.|Polyimides, process for the preparation thereof and polyimide resin compositions|
    JP2624852B2|1988-10-28|1997-06-25|三井東圧化学株式会社|Method for producing polyimide|
    US5069848A|1989-04-05|1991-12-03|Mitsui Toatsu Chemicals, Inc.|Extrusion process of polyimide and polyimide pellet used for the process|
    US5241040A|1990-07-11|1993-08-31|International Business Machines Corporation|Microwave processing|
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    JP2580535B2|1994-05-09|1997-02-12|東京工業大学長|Method for producing polyimide-silica composite|
    US10224258B2|2013-03-22|2019-03-05|Applied Materials, Inc.|Method of curing thermoplastics with microwave energy|
    CN104448310A|2013-09-16|2015-03-25|姜丹宁|Method for synthesis and copolycondensation of polyamide acid and polyimide through microwave radiation|
    JP2015098573A|2013-10-18|2015-05-28|株式会社Kri|High crystal polyimide fine particle and method for producing the same|
    AT519038B1|2016-08-19|2018-11-15|Univ Wien Tech|Production process for polyimides|CN107673417A|2017-08-23|2018-02-09|天津中油科远石油工程有限责任公司|The preparation method of quick deoiling agent|
    AT520472A2|2017-09-20|2019-04-15|Univ Wien Tech|Process for the preparation of polybenzimidazoles|
    US20200291182A1|2017-09-20|2020-09-17|Technische Universitaet Wien|Process for preparing polybenzimidazoles|
    KR102050660B1|2018-01-22|2019-12-02|연세대학교 원주산학협력단|Preparation method for polyimide|
    KR102198357B1|2018-12-17|2021-01-04|연세대학교 원주산학협력단|Preparation method for polyimide|
    AT522304A2|2019-03-15|2020-10-15|Univ Wien Tech|Process for the production of polyimides|
    CN110218317A|2019-06-06|2019-09-10|南京邮电大学|A kind of polyimide type covalent organic frame material and the preparation method and application thereof|
    WO2021141807A1|2020-01-09|2021-07-15|Exxonmobil Research And Engineering Company|METHODS FOR PREPARING MIXED POLYAMIDES, POLYIMIDES AND POLYAMIDEIMlDES VIA HYDROTHERMAL POLYMERIZATION|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA304/2015A|AT517146A2|2015-05-13|2015-05-13|Process for the preparation of crystalline polyimides|BR112017024199A| BR112017024199A2|2015-05-13|2016-05-13|process for the preparation of polyimides|
    CA2985820A| CA2985820A1|2015-05-13|2016-05-13|Process for producing polyimides|
    EP16732915.0A| EP3294794B1|2015-05-13|2016-05-13|Process for producing polyimides|
    US15/573,273| US10563013B2|2015-05-13|2016-05-13|Process for producing polyimides|
    JP2017559457A| JP6994946B2|2015-05-13|2016-05-13|How to prepare polyimide|
    PCT/AT2016/050140| WO2016179625A1|2015-05-13|2016-05-13|Process for producing polyimides|
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